Top Banner
I 7 I E E - E t - --1t. . ,';i:::: -.r,..-'-;;,r&. .r/C* N*w York Chichester STRUCTURAL ANALYSIS AND DESIGN OF PROCESS EQUIPMENT Mqon H. Jowod Nooter Corporation St. Louis, M issouri Jomes R. Fqrr Babcock & Wilco.r Company Barberton, Ohio A Wiley-lnterscience Publicqtion JOHN WILEY & SONS Brisbone Toronto Singopore
360
Welcome message from author
This document is posted to help you gain knowledge. Please leave a comment to let me know what you think about it! Share it to your friends and learn new things together.
Transcript
Page 1: Process Equipment

I

7I

E

E

-E

t

-

--1t. .

,';i::::-.r,..-'-;;,r&.

.r/C* N*w York Chichester

STRUCTURALANALYSIS AND DESIGN

OF PROCESS EQUIPMENT

Mqon H. JowodNooter CorporationSt. Louis, M issouri

Jomes R. FqrrBabcock & Wilco.r Company

Barberton, Ohio

A Wiley-lnterscience Publicqtion

JOHN WILEY & SONS

Brisbone Toronto Singopore

Page 2: Process Equipment

Copyright O 1984 by hhn Wilev & Sons, Inc

All righis reserve{]. Publishcd simultaneously in Canada

Reproduction or transiation ()f any part oi this work

hcyond that permitted by Secton 107 or 108 of ihe

It)?6 linited States Copyrighl Act wrthout lhe permrssron

,,1 rlr .i't)\rfi!hl owner is unl.rwlul Requests iot

| ,"' ,1,,, !,, lrrrhcr infomati,)n sbould be addrcssed lo

'! | ', L , , I'1 t,.,rlrjitrrl. John Wil'v & Sons, lnc

| ,r,, .., , .r , , ,'r', , ( nitrl.'riins in l\rhlication Data:

',|,l ,r'' 'l '!!! \ Lil'rrl)r"crl

\ \\ '1, r I i, | , ', 'r, ' 1,, I lr,.rlr"rr

| ',

1",1, l,rl,lr,,fr,r|l'r., .rrrl rirtl.\I ( lrcr)rcrl t,hnts lilLrrl)rrrcrn :trrl s(ri)l)lr(5 l)esirn

arrl conslroction L Farr. James R ll. lrllc

'tPr55.5.J.14 lq8l 660.2'83 83 12475

lslJN (, .171 (lt).)07 x

l,riIl.rl r!r rln | "rr,al \rlrr'\ lrl America

l09lJ/r)'il1 |

To Our Wives,

Dixie and Barbara

Page 3: Process Equipment

PREFACE

We wrote this book to serve three purposes. The first purpose is to providestructural and mechanical engineers associated with the petrochemical industrya reference book for the analysis and design of process equipment. The secondis to give graduate engineering students a concise introduction to the theory ofplates and shells and its industrial applications, The third purpose is to aidprocess engineers in understanding the background of some of the design equa-tions in the ASME Boiler and hessure Vessel Code. Section VIII.

The topics presented are separated into four parts. Part 1 is intended tofamiliarize the designer with some of the common "tools of the hade." ChapterI details the history ofpressure vessels and various applicable codes from aroundthe world. Chapter 2 discusses design specifications furnished in purchasingprocess equipment as well as in various applicable codes. Chapter 3 establishesthe strength criteria used in different codes and the theoretical backgroundneeded in developing design equations in subsequent chapters. Chapter 4 in-cludes different materials of construction and toughness considerations.

Part 2 is divided into three chapters outlining the basic theory of plates andshells. Chapter 5 develops the membrane and bending theories of cylindricalshells. Chapter 6 discusses various approximate theories for analyzing heads andtransition sections, and Chapter 7 derives the equations for circular and rectan-gular plates subjected to various loading and support conditions. These threechapters form the basis from which most of the design equations are derived inthe other chapters.

Part 3, which consists of flve chapters, details the design and analysis ofcomponents. Chapters 8 and 9 derive the design equations established by theASME Code, VI[-l and -2, for cylindrical shells as well as heads and transitionsections. Chapter 10 discusses gaskets, bolts, and flange design. Chapter llpresents openings and their reinforcement; Chapter l2 develops design equationstor support systems.

Part 4 outlines the design and analysisof some specialized process equipment.Chapter 13 describes the design of flat bottom tanks; Chapter 14 derives the

Page 4: Process Equipment

ftitAct

cquations for analyzing hest transfer equipment. Chapter l5 describes the theory

of thick cylindrical shells in high-pressure applications. Chapter l6 discusses the

stress analysis of tall vessels. Chapter 17 outlines the procedure of the ASMECode, VI[-l, for designing rectangular presswe vessels.

To simplify the use of this book as a reference, each chapter is written so that

it stands on its own as much as possible. Thus, each chapter with design or other

mathematical equations is written using terminology frequently used in industryfor that particular type of equipment or component discussed in the pertinent

chapter. Accordingly, a summary of nomenclature appears at the end of most ofthe chapters in which mathematical expressions are given.

In using this book as a textbook for plates and shells, Chapters 3, 5,6 md7form the basis for establishing the basic theory. Instructors can select otherchapters to supplement the theory according to the background and needs of thegraduate engineer.

In deriving the background of some of the equations given in the ASMEBoiler and Pressure Vessel Code, attention was focused on Section VIII, Di-visions 1 and 2. Although these same equations do occur in other sections of the

ASME Code, such as the Power and Heating Boilers, no consideration is given

in this book regarding other sections unless specifically stated'

MAAN JAWAD

JAMES FARRSaint Louit, MissouriBarberton, OhioSeptember 1983

ACKNOWLEDGMENTS

We are indebted to many people and organizations for their help in preparing this

book. A special thanks is given to the Nooter Corporation for generous support

rluring the preparation of the manuscript. Also a special thanks is given to the

American Society of Mechanical Engineers for supplying many of the illustra-tions used in this book and also to the American Petroleum Institute and the

Tubular Exchangers Manufacturers Association.We also give thanks to Messrs. W. D. Doty, G. Hays, G. G. Karcher, T. W.

[,odes, H. S. Olinger, and R. F. O'Neill for reviewing the manuscript, and to

Mr. W. H. Schawacker for supplying many of the photographs.

We would also like to extend our appreciation to Mrs' Y. Batteast for typingportions of the manuscript.

M. J.

Page 5: Process Equipment

PART I

Chopter Il.l1.2

CONTENTS

BACKGROUND AND BASIC

CONSIDERATIONS

Hisiory ond Orgonizotion of Codes

Use of Process Vessels and Equipment

History of Pressure Vessel Codes in the United

States

Organization of the ASME Boiler and Pressure

Vessel Code

Organization of the ANSI B31 Code for Pressure

Piping

Some Other Pressure Vessel Codes and Standards

in tie United States

Worldwide Pressure Vessel Codes

ReferencesBibliograPhY

3

4

l314

14

l5l5t616

1.3

1.4

1.5

1.6

8

9'r0

ll

Chopter 2 Selection of Vessel, Specificotions'

Reports, ond Allowoble Slresses

Selection of Vessel

Which Pressure Vessel Code Is Used

Design Specifications and Purchase Orders

Special Design Requlrements

Design RePons and Calculatjons

Materials' SPecifi cations

2.1

2.22.32.42.52.6

Page 6: Process Equipment

CONTINT!

2.72.82.92.10

2.11

2.12

Chopter 3

Dcsign Data tbr Ncw MaterialsFactors of Safety

Allowable Tensile Stresses in the ASME Code

Allowable Extemal Pressure Stress and AxialCompressive Stress in the ASME Boiler and Pres-sure Vessel Code

Allowable Stresses in the ASME Code for PressurePiping B31

Allowable Stress in Other Codes of the WorldReferences

Strength Theories, Design Criierio, ondDesign Equotions

Strength Theories

Design CriteriaDesign Equations

Stress-Strain Relationships

Strain-Defl ection Equations

Force-Stress Expressions

References

Bibliography

Moteriqls of Construction

Material Selection

4,l.l Corrosion

4.1.2 Strength

4. 1 .3 Material Cost

Nonferrous Alloys4.2.1 Aluminum Alloys

't7

17

t7

l9

22

22

26

3.1

3.23.33.43.53.6

29

303l33

33

35

39

42

43

45

4646495253

53

3J5656606l63

68

Chopter 4

4.1

4.2

4.2.2 Copper and Copper Alloys4.2.3 Nickel and High-Nickel Alloys4.2,4 Titanfum and Zirconium Alloys

4.3 Ferrous Alloys4.4 Heat Treating of Steels

4.5 Brittle Fracture

4.5. I ASME Presssure Vessel Criteria

4.64.7

4.5.2 'l'heory ol' Brittle Fracture

4.5.3 Hydrostatic Testing

4.5.4 Factors Influencing Brittle Fracture

Hydrogen Embrittlement

Nonmetallic Vessels

References

Bibliography

ANAIYSIS OF COMPONENTS

Slress in Cylindricol Shells

Ends5.3.3 Pressure on Ends OnlyThermal Stress

5.4.1 Uniform Change in Temperature

5.4.2 Gradient in Axial Direchon5.4.3 Gradient in Radial DirectionNomenclature

References

Bibliography

CONTENTS xlll

7074

75

76

7778

79

8l

83

116lr8119

124127

r30137

r38139

PART 2

Chopfer 5

5.1

5.2

5.3

5.4

Stress Due to Intemal Pressure 84Discontinuity Analysis 925.2.1 Long Cylinders 965.2.2 Short Cylinders lO7Buckling of Cylindrical Shells I 145.3.1 Uniform Pressure Applied to Sides Only 1145.3.2 Uniform Pressure Applied to Sides and

Chopter 6 Anolysis of Formed Heods ond TronsitionSections

6. I Hemispherical Heads

6.1 . I Various Loading Conditions6.1.2 Discontinuity Analysis

6.1.3 Thermal Stress

6.1.4 Buckling Strength

141

142146r52158

159

Page 7: Process Equipment

xiv CONTENTS

6.26.36.4

Chopter 7

7.1

7.27.37.4

PART 3

Ellipsoidal Heads

Torispherical Heads

Conical Heads

6.4.1 Unbalanced Forces at Cone{o-CylinderJunction

6.4.2 Discontinuity Analysis

6.4.3 Cones Under Extemal Pressure

Nomenclature

References

Bibliography

Stress in Flot Plotes

Introduction

Circular Plates

Rectangular Plates

Circular Plates on Elastic Foundation

Nomenclature

References

Bibliography

DESIGN OF COMPONENTS

163

167

r68

169

172

175178'r80

t8t

183

184

184

193

197

200201

201

203

20520620821822623r

235238240240241

Chopter 8 Design of Cylindricol Shells

8.1 ASME Design Equations

8.2 Evaluation of Discontinuity Stresses

8.3 ASME hocedure for Extemal Pressure Design

8.4 Design of Stiffening Rings

8.5 Allowable Gaps in Stiffening Rings

8.6 Out-of-Roundness of Cylindrical Shells underExternal Pressure

8.7 Design for Axial Compression

Nomenclature

References

Bibliography

Chopier 9 Design of Formed Heods ond TronsifionSeclions

Introduction

ASME Equations for Hemispherical Head

Design

ASME Design Equations for Ellipsoidal and

Flanged and Dished Heads

9.3.1 Ellipsoidal and Torispherical Heads

Analysis due to Intemal Pressure

9.4.2 Conical Shells under External Pressure

9.4.3 ASME Simplification of DiscontinuityAnalysis due to External Pressure

Nomenclature

References

Bibliography

CONTENTS xv

243244

247

249

25626r

261

265266267

9.1

9.2

9.3

under External Pressure 255

9.4 ASME Equations for Conical Head Design 256

9.4.1 ASME Simplification of Discontinuity

Chopter l0l0.lro.2

Bfind Flonges, Cover Ploles, ond Flonges 269

Introduction 270

Circular Flat Plates and Heads with UniformLoading

ASME Code Formula for Circular Flat Heads

and Coversr0.3

10,4 Comparison of Theory and ASME Code Formulafor Circular Flat Heads and Covers withoutBolting

10,5 Bolted Flanged Connections

10.6 Contact Facings

1O.7 Gaskets

10.7.1 Rubber O-Rings

10.7.2 Metallic O- and C-Rings

10.7.3 Compressed Asbestos Gaskets

10.7.4 Flat Metal Gaskets

10.7.5 Spiral-Wound Gaskets

274

276

278278279281

281

281

282283285

Page 8: Process Equipment

CONTENTS

1O.7.6 Jacketed Gaskets

10.7.7 Metal Ring Gaskets

10.7.8 High-Pressure Gaskets

10.7.9 Lens Ring Gaskets'10.7. I0 Delta Gaskets

10.7.1I Double-Cone Gaskets

I0.7. l2 Gasket Design

10.8 Bolting Design

10.9 Blind Flanges

10. 10 Bolted Flanged Connections with Ring-TypeGaskets

l0.l I Reverse Flanges

10. l2 Full-Face Gasket Flange

10. l3 Flange Calculation Sheets

10, l4 FlatFace Flange with Metal-to-Metal ContactOutside of the Bolt Circle

10.15 Spherically Dished Covers

Nomenclature

References

Bibliography

285285285286287288290292

294

298307310317

317324330332332

335

336338

343346

349

359

368

379

383

Chopter I I Openings, Nozzles, ond Externol[oodings

General

Stresses and Loadings at Openings

Theory of Reinforced Openings

Reinforcement LimitsI I .4. I Reinforcement Rules for ASME.

Section II I .4.2 Reinforcement Rules for ASME,

Section VIII, Division Il l.4.3 Reinforcement Rules for ASME,

Section VIII, Division 2

I I .4.4 Reinforcement Rules for ANSUASME831. I

I L4.5 Reinforcement Rules for ANSI/ASME83 t.3

ll.lI 1.2

I 1.3'| 1.4

I I.5I 1.6

1t.7

CONTENTS xvii

Ligament Efficiency of Openings in Shells 387Fatieue Evaluation of Nozzles under Internal

Chopter l212.1

12.2

Pressure

Extemal Loadings

11 .7.1 Local Stresses in the Shell or Head

I 1.7.2 Stresses in the Nozzle

Nomenclature

References

Bibliography

Vessel Supports

Introduction

Skirt and Base Ring Design

12.2.1 Anchor Chair Design

12.3 Design of Support Legs

12.4 Lug-SupportedVessels

12.5 Ring Girders

12.6 Saddle Supports

Nomenclature

References

Bibliography

PART 4 THEORY AND DESIGN OF SPECIALEQUIPMENT

Chopter l3 Flot Bottom Tonks

13.1 Introduction

13.2 API 650 Tanks

13.2.1 Roof Design

13.2.2 Shell Design

13.2.3 Annular Plates

13.3 API 620 Tanks

13.3. I Allowable Stress Criteria

I 3.3.2 Compression Rings

13.4 ANSI 896.1 Aluminum Tanks

13.4. I Design Rules

392394394407

415416417

421

422423434438442443449456456457

459

461

462462462470476482487

490496496

Page 9: Process Equipment

-

xviii coNTENrs

13.5 AWWA Standard D100

References

BibliograPhY

Chopter 14 Heql Tronsfer Equipmeni

l4.l TYPes of Heat Exchangers

14.2 TEMA Design of Tubesheets in U-Tube

Exchangers

14.3 Theoretical Analysis of Tubesheets in U-Tube

Exchangers

14.4 Background of the ASME Design Equations for

Tubesheets in U-Tube Exchangers

14.5 Theoretical Analysis of Fixed Tubesheets

14.6 TEMA Fixed Tubesheet Design

l4'6'l Local Equivalent Pressure

l4'6'2 General Equivalent Pressure

14'6'3 Relationship Between Local and

Equivalent Pressure

14.7 ExPansion Joints

Nomenclature

References

BibliograPhY

Chopfer 15 Vessels for High Pressure

15.l Basic Equations

15.2 Pres$essing of Solid Wall Vessels

15.3 Layered Vessels

15.4 Prestressing of Layered Vessels

Nomenclature

Biblio$aphY

Chopter 16 Toll Vessels

l6.l DesignConsiderations

16.2 Earthquake Loading

16.3 Wind Loading

16.3'1 Bxternal Forces from Wind Loading

498499

499

501

502

505

508

514519523523527

533537

537

538539

541

541

543547

558562563

565

566567

573573

CONTENTS

I 6.3.2 Dynamic Analysis from Wind Effects16.4 Vessel Under Intemal Pressure Only16.5 Vessel Under Internal Pressure and Extemal

Loading

16,6 Vessel Under External Pressure Only16.7 Vessel Under External Pressure and External

Loading

References

Bibliography

Chopter 17 Vessels of Noncirculor Cross Section

17,1 Types of Vessels

17.2 Rules in Codes

17.3 Openings in Vessels with Noncircular CrossSection 601

17.4 Ligament Efficiency for Constant DiameterOpenings 601

17.5 Ligament Efficiency for Multidiameter OpeningsSubject to Membrane Stress 603

17,6 Ligament Efficiency for Multidiameter OpeningsSubject to Bending Stress 606Design Methods and Allowable Stresses 610Basic Equations 612Equations in the ASME Code, VIII-I 619Design of Noncircular Vessels in Other Codes 626I 7. 10. I Method in Swedish Pressure Vessel

Code 627I 7. 10.2 Design by Lloyd's Register of Shipping

Rules 630References 633Bibliography 633

577581

595

596601

585588

591

593593

17.717.817.9t7.to

APPENDICES 635

Appendix A Guide to Various Codes 636Appendix B Sample of Heat Exchanger Speciflcation Sheet U6Appendix C Sample of an API Specification Sheet 648

Page 10: Process Equipment

-

II CONIENTS

Appendix D Sample of a Pressure Vessel Design Data Sheet

Appendix E Sample of Various Materials for Process Equipment

Appendix F Required Data for Material Approval in the ASME

Section VIII Code

Appendix G Procedure for Providing Data for Code Charts for

Extemal Pressure Design

Appendix H Corrosion Charts

Appendix I Various ASME Design Equations

Appendix J Joint Efficiency Factors

Appendix K Simplified Curves for Extemal Loading on Cylindrical

Shells

Appendix L Conversion Tables

INDEX

652668

675

678683

686

689698

PART

BACKGROUNDAND BASIC

CONSIDERATIONS

Page 11: Process Equipment

CHAPTER

HISTORY ANDORGANIZATION OF CODES

-OtD TIMERS [(lop) Courtesy Bobcock & Witcox Compony, (bol|or,) ( iuroly ,",r,,, , ,"r,,,,r,,,1

2

Page 12: Process Equipment

-Y

HISTORY AND ORGANIZATION OF CODES

I.I USE OF PROCESS VESSELS AND EQUIPMENT

'I'hroughout the world, the use of process equipment has expanded considerably.ln the petroleum industry, process vessels are used at all stages of processing oil.At the beginning of the cycle, they are used to store crude oil Many differenttypes of these vessels process the crude oil into oil and gasoline for the con-

surner. The vessels store petroleum at tank farms after processing and, finally,scrvc to hold the gasoline in service stations fol the consumer's use. The use ofDroccss vessels in the chemical business is equally extensive. Process vessels are

uscd everywhere.Prcssure vessels are made in all sizes and shapes. The smaller ones may be

no larger than a fraction of an inch in diameter, whereas the larger vessels may

be 150 ft or more in diameter. Some are buried in the ground or deep in the

occan; most are positioned on the ground or supported on platforms; and some

lctually are found in storage tanks and hydraulic units in aircraftThe internal pressure to which process equipment is designed is as varied as

thc size and shape. Intemal pressure may be as low as I in water gage pressure

to as high as 300,000 psi or more. The usual range of pressure for monoblock

construction is about 15 to about 5000 psi, although there are many vessels

designed for pressures below and above that range. The ASME Boiler and

Itcssure Code, Section VIII, Division t*, specifies a range of intemal pressure

liom 15 psi at the bottom to no upper limit; however, at an intemal pressure

abovc 3000 psi, the ASME Code, VIII-I, requires that special design consid-

crations may be necessary.r However, any pressure vessel that meets all the

rrquircrncnts of the ASME Codc. regardless of the intemal or external design

prcssuro. rnay slill bc acccptcd by thc authorized inspector and stamped by the

nrlrnrllclurcr with thc ASMI'l ('rxlc syrttbol. Some other pressure equlpment,srrch as Al'l'' sl(nagc t Dks. rrriry bc dcsigned and contain no more intemalpf('ssur( llriur lhitl gcncrirlc(l l)y lllc sllllic hcird of fluid contained in the tank.

I,2 HISIORY OF PRISSURE VESSET CODES IN THT UNITED STATES

llrt(,rt1lr llr( lrlr' lS(X):, ;rrrrl lrrtlv ltX)O\. (\l)losiotls in boilers and pressure

vcsscls rlcrc lr({tr{nt /\ lrrctrllx lrorlt t trplosiott tlrr thc Mississippi River:,1{rlrlx);rt .\rtlt,ttt,t.t '\1rrrl .'/ lStr5. rcsttllctl itt thc boat's sinking within 20

nrnrt(.\,rr,l tlrrr|..rtlr,,l |')l)ilr,(,llr(r\JtoittlllrotrtcaliertheCivilWar.Thistyper,l r rrtrr,,tr,rlrlrl r.trltttttr'rl un,rl)irl( (l rrrlo tlrc clrr'ly 1900s. In 1905, a destructive

, rlrl,,.r,,rr (,1 .r lr, lrlr( l!,rl(-r rrr ir sllrr'' lltellrly in Brockton, Massachusetts (Fig.

I l r. l rlllrl ''Il rr ,'r'l( . rrrlrrr, rl l l / otlrcls. and did Xi400,000 in property damage

'1,' rlL, r,\r \'.Alt r,rl, \'lll l,rrrrl VIII .'. rsrrrie(l lo (lcscribc thc ASME Boilcr and I'rcsstrrc

Vi....tl(,trit ,, l',," \'ftl ffl\, r'r l. /,,,'r.vt( V, rfry'.r, and l)ivisitttl2, Alk'r'ttttiK |tttll li'r/!,11r,, l, \ \, /,

Fisure l.l Firerub€ boiler explosion in sho€ focrory in Brockron, Md!3ochuseits in 1905. (Courlesy HorrfordSt@m Boiler Inrpection ond Insurdn.e Co., Horrford, Cr.)

Page 13: Process Equipment

6 HISIORY AND ORGANT/N rION Of CODTS

Irr l(X)(r, l'r.llre'cx;rkrsi.rr irr . rlrr)c llrel.ry i'l,yrrrr. Massirclrrtsc.s, r.cs.ltcdirr dcalh, injrlry, a|ld cxtcnsivc propcrty darragc. Aticr this accidcnr, the Massa_clrusctt$ governor directed the fbrmation of a Board of Boiler Rules. The first setof rules for the design and construction of boilers was approved in Massachusettson August 30, l9O7 . This code was three pages long-!-

In 1911, Colonel E. D. Meier, the president of-the American Society ofMechanical Engineers, established a committee to write a set of rules tbr thedesign and construction of boilers and pressure vessels. On February 13, 1915,the first ASME Boiler Code was issuid. It was entitled ,,Boiler ConstructionCode, 1914 Edition." This was the beginning of the various sechons of theASME Boiler and Pressure Vessel Code, which ultimately became Section 1,Power Boilers.3

^ The first ASME Code for pressure vessels was issued as ,,Rules fbr the

construction ofUnfired Pressure Vessels,', Section VIII, 1925 edition. The rulesapplied to vessels over 6 in. in diameter, voiume ove. 1.5 ft3, and pressure over30 psi. In December 1931, a Joint API_ASME Committee wis ibrmed todevelop an unfired pressure vessel code for the petroleum indusiry. .l.he firstedition was issued in 1934. For the next 17 years,iwo separate unfiied pre;surevessel codes existed. In 1951, the last API_ASME Code ;as issued as a separaredocument.a In 1952, the two codes were consolidated into one code_the ASMEUnfired Pressure Vessel Code, Section VIII. This continued until the 196gedition. At that time, the original code became Section VIII, Oivislon I , pres_sure Vessels, and another new part was issued, which was Seciion VI II, Division2, Alternatiye Rules for pressure Vessels.

The ANSUASME Boiler and pressure Vessel Code is issued by the AmericanSociety of Mechanical Engineers with approval by the American'National Stan_dards lnshtute (ANSI) as an ANSI/ASME document. One or morc sections ofthe ANSI/ASME Boiler and pressure Vessel Code have been established as thelegal requirements in 47 of the 50 states in the United Str,", ,,",f in all theprwinces of Canada. Also, in many other countries of the worlti, the ASMEBoiler and Pressure Vessel Code is used to construct boilcrs arrc pressurevessels.

In the United States most piping systems are built to the ANSI/ASME Codefor P.ressure Piping B3l . There are a number of different piping couc sectronsfor different types of systems. The piping section that i" ,ir".i tiu. boiiers incombination with Section I of the ASME Boiler and pressure Vcsscl (ixle is the!o09 fo1!-o1er Piping, 831.1.5 The piping secrion thar is olicn uscrt withSection VIII, Division I , is the code for

-Cheniical piant and lretnricLrrrr t{clinery

Piping, 831.3.6

I,3 ORGANIZATION OF THE ASME BOILER AND PRESSUREVESSET CODE

The ASME Boiler ancl pressure Vessel Code is clivided into many sectrons,divisions, parts, and subparts. Some ofthese sections relat",u

" ro"lrti. tina of

T].4 ORGANIZATION OF THT ANSI 83 ] CODI] IOR PRISST'RE PIPINO 7

cqUipl c|l{ irrrtl ir;lrlielrliorr; olllcrs fctalc lo sl)ccilic Illillcliltls all(l tlrclll{xls l()f

applicatiOn rn(l cot)trol ol cclt'tiprnctrt; lnd tlthcrs rclate ttt care !lnd inspoctioll ()l

installed cquipnrctrt. 'l'hc tirllowing sections specifically relate to boiler and

pressure vessel design and constructlon:

Section I. Power Boilers (one volume)

Section IIIDivision 1. Nuclear Power Plant Components (7 volumes)

Division 2. Concrete Reactor Vessels dnd Containment (one volume)

Code Case Class I Components in Elevated Temperature Service (tn

N-47 Nuclear Code Case book)

Section IV, Heating Boilers (one volume)

Section VIIIDivision 1. Pressure Vessels (one volume)Division 2. Alternative Rules for Pressure Vessels (one volume)

Section X. Fiberglass-Reinforced Plastic Pressure Vessels (one vol-ume)

A new edition of the ASME Boiler and Pressure Vessel Code is issued on July

I every three years and new addenda are issued every six months on January I

and July l. A new edition incorporates all the changes made by the addenda to

the previous edition; it does not incorporate, however, anything new beyond that

coniained in the previous addenda except for some editorial corections or a

change in the numbering system. The new edition of the code becomes manda-

tory when it appears. The addenda are permissive at the date of issuance and

become mandatory six months after that date.

Code CasesT are also issued periodically after each code meeting They

contain permissive rules for materials and special constructions that have not

been sufficiently developed to place them in the code itself. Finally, there are the

Code Interpretations8 which are issued every six months These are in the form

of questions and replies that further explain items in the code that have been

misunderstood.

I.4 ORGANIZATION OF THE ANSI 83I CODE TOR

PRESSURE PIPING

In the United States the most frequently used design rules for pressure piping are

the ANSI 83l Code for Pressure Piping. This code is divided into many sections

for different kinds of piping applications Some sections are related to specific

sections of the ASME Boiler and Pressure Vessel code as follows:

Page 14: Process Equipment

HISTORY AND ORGANIZATION OF CODES

R!1.1. Power Piping (which is related to Section I)

F.31.2. Fuet Gas Piping (which may be related to Section VIII)

831.3. Chemical Plant an(l Petoleum Refnery Piping (which may be

related to Section VIII)R31.4. Liquitl Petroleum Transporting Prping (which may be related to

Section VIII)831.5. Refrigeration Piping (which may be related to Section VIII)831.7, Nuclear Power Piping (which has been discontinued and incorpo-

rated into Section III)B31,8. Gas Transmission and Distribution Piping Systems (which may be

related to Section VIII)

The ANSI B31 Piping Code Committee prepares and issues new editions and

addenda with addenda dates that correspond with the ASME Boiler and Pressure

Vessel Code and addenda. However, the issue dates and mandatory dates do not

always correspond with each other.

I.5 SOME OTHER PRESSURE VESSEL CODES AND STANDARDS IN

THE UNITED STATES

In addition to the ANSVASME Boiler and Pressure Vessel Code and the ANSI

B31 Code for Pressure Piping, many other codes and standards are commonly

used for the design of process vessels in the United States. Some of them are:

ANSUAPI Standard 620. "Recommended Rules for Design and Construction

of Large, Welded, Low-Pressure Storage Tanks," American Petroleum Insti-

tute (API), Washington, D.C.

ANSVAPI Standard 650. "Welded Steel Tanks for Oil Storage," American

Petroleum Institute, Washington, D.C.

ANSI-AWWA Standard D100. "Water Steel Tanks for Water Storage"'

American Water Works Association (AWWA), Denver, Colorado'

ANSVAWWA Standard D101. "Inspecting and Repairing Steel Water Tanks,

Standpipes, Reservoirs, and Elevated Tanks, for Water Storage," American

Water Works Association, Denver, Colorado.

ANSI 896.1. "specification for Welded Aluminum-Alloy Field Erected Stor-

agc Tanks," American National Standards Institute, New York'

lll, (A4. Standartl for Conk ner Assemblies.lor I'P-Gas, 4th ed, Under-

wlitcrs Laboratories. Nolthbrook, Illinois.

I.6 WORLDWIDE PRESSURE VESSEI CODES q

Stanlarh of Tubular Exchanger Manufacturers Association, 6th ed., Tu_bular Exchanger Manufacturer's Association, New york.Standnrds of the Expqnsion Joint Manufacturers Associ(ltion, 4th ed. , Exoan_sion Joint Manufacturer's Association, New york.

I.6 WORI-DWIDE PRESSURE VESSEL CODES

In addition to the ASME Boiler and Pressure Vessel Code, which is usedworldwide, many other pressure vessel codes have been legally adopted invarious countries. Difficulty often occurs when vessels are designed in onecolntry, built in another country, and installed in still a different country. Withthis worldwide construction this is often the case.

The following list is a partial summary of some of the various codes used indifferent countries:

Australia.

Australian Code for Boilers and Pressure Vessels, SAA Boiler Code (SeriesAS 1200): AS 1210, Unf.red Pressure Vessels and Class 1 H, pressareVessels of Advanced Design and Constuction, Standards Association ofAustralia.

Belgium.

Code for Good Practice for the Construction of Pressure Vessels, BelgianStandard Institute (IBN), Brussels, Belgium,

France.

Constructton Code Calculation Rules for Unfred pressure Vessels, SyndicatNational de la Chaudronnerie et de la Tuyauterie Industrie e (SNCT), paris,France.

Germany.

A.D. Merkblatt Code, Carl Heymanns Verlag KG, Koln/Berlin, FederalRepublic of Germany.

haly.

Itqlian Pressure Vessel Code, National Association for Combustion Control(ANCC), Milan, Iraly.

Page 15: Process Equipment

t0HISTORY AND ORGANTZATION OF CODES BIBTIOGRAPHY ll,ltpun.

,lqnnt'st' l)tt,.t,rurt Vt,l;scl Code. Ministry of Labor, published by JapanlJoilcr Associution. Tokyo, Japan.Juyuu'ts-t' Standarrl, Construction of pressure Vessels,JIS B g24j, publishedby the Jupan Srandards Association. Tokyo, Japan.

"- - e' 'J' Y'

Jap,ayle High pressure Gas Control Law, Ministry of International Trade1i1,1,".t":,ry.Jibtished by rhe rnstitution for sffi

"r riigi;;Jrr*" c",tngtneering, Tokyo, Japan.

Netherlands.

f,:|;:#i:"*-e vessets. Dienst voor het stoomwezen, The Hague, the

Sweden.

Swedish Pressure Vessel Code,-Tryckkarls kommissioner, the Swedish pres-sure Vessel Commission, Stockholm, Sweden.

United Kingdom.

British Code 85.5500, British Standards Institution, London, England.

More complete details. discussions of factors of safety. and applications ofthe codes mentioned are given in Section 2.7. e summ,lry of iti. p_ug.upt,which.ar.e appticable for ihe various,.reqrl;il ;'r#J # ,ti .o0., ur.oaround the world is given in Appendix A.

REFERENCES

f. ASME Boiler and pressure Uo*] "aT.:

,:".,,:n. Unr, Division l, pressure Vessets,ANSVASME BpV-Vm_1, Americar2. Apr srandard 620, "R""",*";;;'R';:"i."iiirT"firi,"ffilffi;TiJi:i,*Li.;,

.;: j::::"[iJ:** tanks," ANsr,/Apr srd. 620,;.;;;";-;;;;;; i,i.tr"iot", wu,r,ing_

l. ASME Boiler and pressure Vesset Code, Section_|, power Boileru, ANSTASME BPV_I,_ nlll*,*n Sociery of Mechanicat Engrneers. New york, 1983.

" lilHy3,::ff '.{iX::#l#f#*y:::k-!y ^Pa'r:teu!

Liq.uids and Gases, 5th ed.,1951. gmeers and American petroleum Institute, New york,

S, ASME Code for hessure pipinq BJl.ol Mechanicar Engineers, Niw-york, 73l;;"'0"'ANSL/ASME

B31 l' American societv

6. ASME Code for hessure pioins B3l, g!t:m:cal. ptant and petroleunt Refinery piping,

- ^NSvASME 83t.3. American Siciety of Mechanical ;;C;;, ;u;;"lo.k,r,,*0.7' A_SME Boije-r and hessure vesser code,

-cod? cases, Boirers antr pre,rrrre y€$dh, AmericanSocicty of lvlechanicaj En8incers, Ncw york, 19g3.

8. ASME Boiler and pressure Vessel Code, _fu terpretations, (isstred every six months), AmedcanSociety of Mechanial Engineers, New york.

BIBTIOGMPHY

' Steel Tanks for Liquid Stoege', in Steel plate Engifieerin| Data, Vol. l, 1976 ed., American Ironand Sreel lnslirute, Washingron, D.C.

is

Page 16: Process Equipment

CHAPTE R 2SELECTION OF VESSEL,

SPECI FICATIONS, REPORTS,AND ALLOWABLE STRESSES

l3

Page 17: Process Equipment

l4 SttECTlON OF VESSIL, SPECIFICAIl()N". rtlr",lrr'., nND ALLOWABLE STRESSES

2.1 SELECTION OF VTSSI I

Although nrlrrly lttr l t. ,,'rrlrl,rt, 1,, llr( \( lL'clion of pressure vessels, the twobasic r.r;rrirr.rrfrrt,, tlr,rt ,rll,, t tlr, ,( [.r lion are safety and economics. Manyit(.Drs i||r. r rr,,rrI r,,l rr,tr,r', rrrrrtcrials' availability, corrosion resistance,lrltllrrl,, rrr, rrl,tlr r11, . .rr,l rrrrrgnitudes of loadings, location of installationrr, lr,lprl, ( rnl I,r.r,l'rt' ,"r,t r.rrr'(lrquake loading, location of fabrication_(shoD"r 1., l,lr t", rrr,,r ,,t \i.,,s(.1 installation, and availability of labor supply at the

\l rrt, rrr, r, ,r'.rrr1' rrsc of special pressure vessel in the petrochemical and otherrrr,lrr rl, , rtr. ;rvrilability of the proper materials is fast becomrng a maJor1,r,,t,1,,,' I lr(. nrost usual material for vessels is carbon steel. Many other special_r,,, l r r,rr{ rlls iLre also being used for corrosion resistance or the abilily ro conmln.r tlrrrr I wrthout degradation of the material's properties. Substitution of materialsr'. I x (.vl lent and cladding and coatings are used extensively. The design engineerrrrrrst lrc in communication with the process engineer in order that all materialsrrsctl will contribute to the overall integrity of the vessel. For those vessels thatrctluire field assentbly in contrast to those that can be built in the shop, proper(luality assurancc must be established for acceptable welding regardless;f iheadverse condilions under which the vessel is made_ provisions must be estab_lished for ftrrliography, stress relieving, and other operations required in thefield.

For thost. vcssels that will operate in climates where low temperatures areencounlcr((l r)f contain fluids operating irt low temperatures, special care mustbe takc rr Ir crrsure impact resistance of the materials at low timperatures. Toohlirirr tlrs l,r()l)crty, the vessel may require a special high-alloy steel, nonferrousrrrirlcrirrl, rrr some special heat treatment.

2.? WHICH PRESSURE VESSEL CODE IS USED?

'l lrc lrrst consideration must be whether or not there is a pressute vessel law atllrc lo( irt ion of the installation. If there is, the applicable iodes are stated in thel:rw. ll thc jurisdiction has adopted the ASME Code, Section VIII, the decisionrrrly bc narowed down to selecting whether Division I or Division 2 is used.

. I'here are many opinions regarding the use of Division I versus Division 2,but the "bottom line" is economics. In the article ,.ASME pressure_Vessel Code:Which Division to Choose?",r the authors have listed a number of factors forconsideration. Division I uses approximate formulas, charts, and graphs insimple calculations. Division 2, on the other hand, uses a complex methocl offbrmulas, charts, and design-by-analysis which must be describcd in ir stressreport. Sometimes so many additional requirements are addcd lo tltc rriuirnumspecifications of a Division I vessel that it might bc rnorc ccorrorrrir.rrl to supplylu I)ivision 2 vcssel and lake advantage of thc highcr itlL)rvrl)l(. strrsscs.

2.4 SPECIAL DESIGN REQUIREMENTS

2.3 DESIGN SPECIFICATIONS AND PURCHASE ORDERS

Currently, the only pressure vessel code, exclusive of the ASME Code, III-l-NB, Nuclear Vessels, which specifically requires formal design specifications as

part of the code requirements is the ASME Code, VIII-2, Alternative Rules forPressure Vessels. This code requires a User's Design Specification to be pre-pared and certified by a registered professional engineer experienced in pressurevessel design. This certification by the professional engineer is given on theASME Manufacturer's Data Report, Form A- 1. The manufacturer is responsiblefor retaining the User's Design Specification for five years.

For other codes and standards, design specifications and design requirementsare not well defined. For the ASME Code, VIII-1, there is no specific statementthat any design specifications are required. The only indication of some sort ofdesign specifications is the list of minimum loadings in UG-22 that is consideredfor all construction . Sectron l, Power Eoilers, is less definitive on what loadingsare necessary to consider and what shall be included in a design specification orpurchase order. PG-22 of Section I states that loadings that cause stresses to gohigher than 107o above those stresses caused by internal design pressure shall beconsidered. The Manufacturer's Data Report, Form U-1 for the ASME Code,V I-1, requires many items to be listed, which means that most of the basicdesign information must be given in a design specification or purchase order.Although some codes help the purchaser regarding what data are needed forinclusion in the design specifications, this is usually done by mutual agreementbetween the purchaser and the manufacturer.

"For those process vessels that do not have a "suggested" list of items in designrequirements and specifications as part of code requirements, it is necessary toestablish them in the purchase order or contract agreement. The contract infor-mation is supplied by the purchaser or user with the manufacturer's help as towhat is needed and what shall be considered. Some design standards help theuser and manufacturer by offering fill-in forms that specifically list the require-ments for designing a process vessel. Design specification forms for a heatexchanger built to the standards of the Tubular Manufacturers Associationz aregiven in Appendix B and lor an API Srandard 650 Storage Tanki are given inAppendix C. It is always necessary to maintain a document containing designspeciflcations so that a permanent record is kept for reference. Often on a largeprocess vessel, some loadings from attached or supported equipment are notknown until after the job has started.

2.4 SPECIAL DESIGN REOUIREMENTS

In addition to the standard information required on all units, such as designpressure, design temperature, geometry, and size, many other items of infbrma-tion are necessary and must be recorded. The (xrrrosion and erosion amounts arc

l5

Page 18: Process Equipment

16 sfl,tcTtoN Ot Vtssll, st,tctt tcaTtoNs, RfpoRTs, AND AU-OWABLE STRTSSES

l, lx' *,u,.,, rrrrrl rr srrrtirlrlt. r'irlcri.l uld method of protection are to be noted. Thelyl)c (,l lllrirl tlrrrl will lrc t,0|llainctl, such as lethal, must be noted because ofthercqltitc(l slx\.ili(.rk.sigrr tlctaiis. Supported position, vertical or honzontat, ands[pl)oll lor.rrtiorrs rlusl bc listed as well as any iocal loads from supportedcrltip,rc,t rrrrtl piping. Site locatiorr is given so that wind, *o*, una

"u.tnquut"lcquircntcots ctrn lre determined. Impact loads and cyclic requirements are alsoinclurlcd.lirr thc ASME Code, VIII-2, a statement as to whether or not a tatigue

:::'.r,:::'.-"111r'llo according.to AD_160 is given. rf u rutilu" analysis isrc(lurrc(t. lhe specitlc cycles and loadings will be given. In addiiion, the designspccilications state whether or not certain loadings ire sustained or transrent. Theallowable stresses vary with the type of loadinls.

2.5 DESIGN REPORTS AND CATCULATIONS

T:,1YE ,C"1.. .VII.2. requires a formal design report with rhe assumptionsrn.the User's Design Specification incorporated in the stress analysis calcu_lations. These calculaiions are prepared and certified by a registered professionalengrneer experienced in pressure vessel design. As with the Usir,s DesignSpecification, the Manufacturer's Design Report is mandatory and thecertification reported on the Manufactu.".i Datu Repo.t. This is kept on file bythe manufacturer for five years.

- For vessels not requidng design reports, the manufacturer has available forthe- Authorized Inspector's review those necessary calculations for satisfyingU-2(g) or other design formulas. The pressure vessel design sheets shouldcontain basic design and materials data and at least the basic calculations ofpressure parts as given in the design formulas and procedures in the applicable

:_od^. onT.nd1d_fg. a simple vessel, an example of calculation sheets rs given

ll ilp"yiT D. This example depicts only those calculations that are requiredfor the Authorized Inspector and for construction. Other vessels may requrernuch more extensive calculations depending upon the complexity and con_(raclutl greements.

2.6 MATTRIALS' SPECIFICATIONS

All crxles itnd standards have materials, specifications and requirements de_sclibirrg whirl rrralcrials are permissible. Those material, tirut *"i"r_rtt"O *ittir sp(.( rli( ((xlc arc cither listed or limited to the ones that have aliowable stressvrrlrrts liivcrr. l)upcnding upon the code or standard, permitted rnatenas tor apirrtit rrliu plxt.ss vcsscl are limited. For instan"., o;i.;";;, Jin an se orljll (lcsif nirrior crr bc uscd in ASME Boiler and piersir" V"rr"i-Cot "rnr,_"_:]:lil...Y:::,:t l:,lf ::l',t

SI) specifications are the same u';;;, B specifi-flltlotl rr lltc ASIM Stirrrtlirltls a On specific instances, certain materiais thatItttvc lrt'rr rr.rlrril( r'r'r(r to sonrc other spccification, such as the DIN standard..

2.9 ATLOWABLE TENSITE STRESSES IN THE ASMI CODE 17

may be recertified to an SA or SB specification for an ASME certified vessel.Depending upon the contract specifications, permissible materials for construc-tion are given in lists such as that shown in Appendix E.

2.7 DESIGN DATA FOR NEW MATERIALS

When design data, such as allowable stresses, are requested for a new material,that is, one not presently in the code, extensive information must be supplied tothe Code Committee for evaluation. The ASME Code Committee lists thisinformation to develop allowable stresses, strength data, and other requiredproperties for accepting a new material into the code. Each section of the codecontains an appendix listing these requirements such as the one for the ASMECode, VIII-I, in Appendix F. The code also provides data to establish extemalpressure charts for new materials; this is given to those who want to establishnew external pressure charts. The required information is given in Appendix G.It is the person's responsibility requesting the addirion to supply all the dataneeded to establish those properties required in the code.

2.8 FACTORS OF SAFETY

In order to provide a margin of safety between exact formulas, which are basedon complex theories and various modes of failure , and the actual design formulasused for setting the minimum required thicknesses and the stress levels, a factorof safety (FS) is applied to various materials' properties that are used to set theallowable stress values. The factors of safety are directly related to the theoriesand modes of failure, the specific design criteria of each code, and the extent tox.hich various levels of actual stresses are determined and evaluated.

2.9 ALLOWABTE TENSILE STRESSES IN THE ASME CODE

As previously discussed, the basis for setting the allowable stress values or thedesign stress intensity values is directly related to many different factors de-pending upon the section of the code used. The criteria for setting allowabletensile stresses for each section of the ASME Boiler and Pressure Vessel Codeare as follows:

For Section I, Power Boilers, the ASME Code, YIll-l , Pressure Vessels, andSection III, Division 1, Subsections NC, ND, and NE, except for bolting whosestrength has been enhanced by heat treatment, the factors used to set the allow-able tensile stresses are summarized below.

At temperatures in the tensile strength and yield strength range, the least of:

1. j of the specified minimum tensile strength.2. j of the tensile strength at remperarure.3. ! of the specified minimum yield strength.

Page 19: Process Equipment

I8 SEI.TCTION OI VESSEL, SPECITICATIONS, REPORTS, AND AttOWABtE STRESSES

4. r{ ol thc yicld strength at temperature (except as noted below where 90Zois uscd).

At temperatures ip the creep and rupture strength range, the least of:

l, l00qa of the average stress to produce a creep rate of 0.0l per l000 hours(l7o in 105 hour).

2. 67Ea of the average stress to produce rupture at the end of 100,000 hours.3. 80Vo of the rninimum stress to produce rupture at the end of 100,000

hours.

,_ In the temperature range in which tensile strength or yield shength sets the

allowable stresses, higher allowable stresses are permitted for austenitic stainlesssteels and nickel-alloy materi-als where gleater deformation is not objectionable.

!9h:l*,the criterion of I yield strength at lemperature may be increased to9oVo,yield strength at temperature. However, the factor ! spicified minimumyield strength is still maintained.

For the ASME Code, VIII-I, bolting material whose slrength has been en_hanced by heat treatment or strain hardening have the addition; criteria of (l) jof the specified minimum tensile strength and (2) t of the specified minimumyield strength.

For the ASME Code, VIII-2, and Section III, Division 1, Subsection NB andNC-3200 of Subsection NC, the factor used to set the design stress intensityvalues for all materials except bolting is the least of:

1. i of the specified minimum tensile strength.2. ] of the tensile strength at remperarure.3. .2 of the specified minimum yield strength.4. J of the yielded strength at temperature except as noted in the tbllowing

paragraph.

Higher design stress intensity values are permitted for austenitic stainlesssteels and nickel-alloy materi€ls where greater deformation is not objectionable.In this_ case, the criterion of J yield strength at temperature may be increased toas high as 90Vo yield strength at temperature or any value beiween ! and gOVoyield strength at temperatue depending upon the acceptable amount of defor-mation. However, the factor of j specified minimum yield strength is stillmaintained.

There are two criteria for setting bolting design stress intensity values in theASME Code, VIII-2. For design by Appendix 3, the criteria are the same as forthe ASME Code, VI -1, because these values are used for the tlcsign of boltsfor flangjs. Ior design by Appendix 4 of the ASMII (ixlc. VIII_2, and bySectirrn III, Division -l

, Slbsdition NB ancl NC-32(X) ot' Sutiscc.riirn IrtC. thecrilcria lirr setting bolting design stress intcnsity vitlucs urc thc lesscr of the

2.IO ALLOWABLE EXTERNAI PRESSURE STRESS AND AXIAI. STRESS I9

following: (1) | of the specified minimum yield strength and (2) j of the yieldstrength at temperature.

For Section IV, Heating Boilers, the criterion for setting the allowablestresses is much more simple: (1) I /5 of the specified minimum tensile strength.

2.IO ALTOWABLE EXTERNAL PRESSURE STRESS AND AXIALCOMPRESSIVE STRESS IN THE ASME BOILER AND PRESSUREVESSEL CODE

Within the ASME Boiler Code, simplified methods are given to determine themaximum allowable external pressure and the maximum allowable axial com-pressive stress on a cylindrical shell without having to resort to complex ana-lytical solutions. Various geometric values are contained in the geometry chart,whereas materials' properties are used to develop the materials charts.

Allowable stresses in the materials charts are based on the followine criteriaFor cylindrical shells under external pressure, the least of:

l. 33Vo of the critical buckling stress with a factor of 807o for tolerance.2, 33Va of the specified minimum yield strength and yield strength at tem-

perature.

3. 67Vo of the average stress to produce a creep rate of 0.01%/1000 hours(17ol 100,000 hours).

4. IOOVo of the allowable stress in tension.

- For spheres and spherical portions of heads under extemal pressure, the least

OI:

l. 25Eo of the critical buckling stress with a factor of 607o for tolerance.2. 25Va of the specified minimum yield strength and yield strength at tem-

perature.

3. 507o of the average stress to produce a creep rate of 0.017o/1000 hours(17ol100,000 hours).

4. IOOVo of the allowable stress in tension.

For cylindrical shells under axial compression, the least ol

l. 259o of the critical buckling stress with a factor of 5OVo for tolerance.2. 50Vo of the specified minimum yield strength and yield strength at tem-

perature.

3. 1007o of the average stress to produce a creep rate of 0.017o/1000 hrs( l7ol 100,000 hours).

4. ljQVo of the allowable stress in tension.

Page 20: Process Equipment

(-)

z

-{ *sZ *9.. d':a ov.,. i.:Y : ir a5d .9- E E=3.! * a E eaz .;T .9ir^l$-. o6; tE ;c===-?!: Eg €Et5;;'

;€i :EH3;E6EE>'< ri :E!l-.r'!55::-6 O. \:' E-= O o o o 6.

=g+ P-+tstE333E,.Eo,; ;.:!do0EEEE

4t4il i-oi.lR4 Eoo+ !,'H; i.g I.g PF H i.=.=.r a

eEeEg,:EiEEfEEEEE(aG6.6*d-EG?q<<<.

d---oinEG*rj

F3trF ctrEEEE2CCCqE I C C E E E

' CJ

=r5===S=55-E=g=3

tItl

tt||l

ttltl

.oP.ocoto'\-j'\'\'\NONa{:

.\..\-\.\ |

.\.\.\.\ |

;d

21

20

;6 ;5 ;6 Ed-iA-i-l

t-. F- a- tr\o \o \o \o-i -i .l ^'

.i "i -; .-'

s3ss5ss r sgss

rrtt|tl

ltltitll

rl||tl

..'\fra\ot\ooo1 :

a- cr\o \o

eqg

.o..).o.i66+ii>;h\> I

<qc!o

ao

" 5oN bo '-i-- d* g? g :is =P9 c3 I ."4 o F -; EE €.i la€ .0 .0.q.i d

E gv e g qOv) u) ,5 ,5

t)

0rt5

6€EtF

F:

.:9

:

3Eq(/)F

.=9

120

z

o

;ta

.9ooo

@

-g

q,Fg

'=

x

=

oooo.-o.E6

!ao

->

.g

oo

:, .o

i;=<t-.E;

oon=doF>

Page 21: Process Equipment

22 STI.TCIION Ot VTSSTI-, SPTCIFICATIONS, REPORTS, AND ALLOWABIE STRESSES

2.I I ALLOWABLE STRESSTS IN THE ASME CODE FOR PRESSUREPIPING 83I

'I'hc ullowrrblc sircsscs given in various sections of the ASME 831 Code forl\'csnulc I'ipirrg urc sinrilar to the corresponding sections of the ASME Boilernrtl l\'cssurc Vcssel Code; however, in some sections, the basis is different. Inthc (lxlc lirf Power Piping B31.l, the allowable tensile stresses are set by thesrrrrrc crilcria as used for ASME Code, Section I. In the Code for Chemical plantrn(l llctrolcum Refinery Piping B31.3, the allowable tensile stresses for otherth n bolting are set on a similar basis as used for ASME Section VIII, Divisionl, sxcept a factor of i is substituted for j on the tensile strength. The factor ofi on yield strength is used in both codes. This makes 831.3 in the tensile andyield strength range is similar to Division 2 and in the creep and rupture strengthrange similar to Division 1.

2.12 ALLOWABLE STRESS IN OTHER CODES OF THE WORLD

Throughout the world, various factors of safety are applied to materials' data toestablish allowable shesses for the design of boilers, pressure vessels, andpiping. For the temperature range to that temperature where creep or rupture setsthe allowable stresses, the universal factor for setting allowable stresses is basedon yield strength. In some countries, a factor is applied to sets of data that havebeen established from many tests; in others, the data are determined by the lowyield point or the high yield point. In still other countries, the actual data for thecomponent being designed have its yield strength determined by tests . The actualdata of the part are then factored into the design formulas. Not all countrieschoose to use the ultimate tensile strength as a criterion for setting allowablestresses. When they do, the factor of safety between various countries rs some-times very different. In order to show these differences, a discussion followsregarding the allowable stress basis of several different countries.

The ierms, symbols, and definitions used are as follows:

UTS : ultimate tensile strength (either specified minimum or data at designtemperature)

y5 = yield strength (either specified minimum or data at design tem-perature)

R = stress to cause rupture in 100,000 hoursC : stress to cause total creep or creep rate in 100,000 hours

na : not applicablen : none or not used

2.12 ATLOWABTE STREss IN OTHER CODES OF THE WORI.D

Australia

rs

23

The rules used for the design of boilers ald pressure vessels set by the StandardsAssociation of Australia are called the SAA Standards Series AS 1200. Thefactors of safety used to set the allowable stresses for the various sections are:

RUTS

AS 1210_1977Pressure Vessels

Class lH-1979AS 1228-1980Boilers

Belgium

nn

The Belgian rules issued by The Belgian Standards Institute (IBN) permir amixture of code rules from various other countries. The allowable stressesdepend usually upon the codes used. However, the basic allowable smesses areset as follows:

42.4

2.7

1.6*1.5

1.5

1.6na

1.5

UTS ys

' Boilers

Liquid gas

Air receivers

Pressure vessels

Czechoslavakia

3.22.7

1.6

1.6

1.5

n

n

nn 1.8 n nVarious factors at designer's choice

Czechoslovakian rules are extensively detailed for all types of vessels withdifferent allowable stresses used for intemal pressure as compared with extemalpressure. For the design of boilers and pressure vessels, the allowable stressesare established by the least of:

*l.5 at temDerature.

Page 22: Process Equipment

24 SELECTION OF VESSEt, SPECITICATIONS. REPORTS, AND ATIOWABTE STRESSES

UTS

Intemal pressure----cylindersHeated wall nUnheated wall nCastings n

All wallsCastings

1.61.62.0

n 2.0n 2.5

Extemal pressure-cylinders without stiffening rings

1.6l.)2.0

2.02.5

1.01.01.25

1.351.7

F rance

The French rules for pressure vessel design establish the allowable shessesdepending upon the inspection and the compliance with the SNCT (SyndicatNational de la Chaudronnerie et de la Tuyauterie Industrielle) rules. The allow-able stresses are established by the least of:

SNCT w/insp.

SNCT w/insp.and analysis

Not SNCTw/insp.

Not SNCTw/o insp.

2.7

Gennany

The three types of pressure vessels recognized by the regulatory agencies inGermany are fixed pressure vessels, mobile pressure vessels, and boilers. Theallowable stresses are established according to a specific DIN (German IndustrialStandard) certificate or by testing. The allowable stresses are set by variousfactors of safety on the yield strength with a constant factor of safety on ruptureas follows:

UTS

v,5

1.0

1.0

1.0

1.0

1.6

1.6

1.6

1.6

1.6

1.6

1.5

1.9

2.4

ys

Steel (not cast)DIN 3

DIN2orlTested

nn

n

nn

n

I .:)

1.8Ll

1.51.51.5

2.I2 ALTOWABLE STRESS IN OTHER CODES OF THE WORID

ys RUTS L

Cast SteelDIN 3 nDIN2or 1 nTested n

Aluminum and seamless copperDIN 3 nDIN2or I nTested n

2.02.5l.)

l 5

1.51.5

nnn

nnn

Italy

The Italian rules for boilers and pressure vessels establish the allowable stressesby the least of the following:

UTS

J.f4.02.5

1.51.51.5

Boilers 2.7Pressure vessels n

UTS

1.6 1.01.5 1.0

1.6

1.5*1.6

Japan

The Japanese government does not have one group to develop their designcodes. Rather have several different rules for designing boilerJ and pressurevessels. Although they are published by different groups and generally writtenby the different groups, all codes are under the control of the Japanese govern-ment. The basis for setting allowable stresses is the least of:

rs

Boilers

Pressure vessels

Altemativepressure vessels 3

*1.5 used when YS/IS > 0.85.

'whcrcT: YS/TS < O.7.

1.6 1.67 av.l 25 min.

2/(1.6 - jI 1.5 av.I .25 min.

1.0

1.5

1.0

Page 23: Process Equipment

26 SETECTION OF VTSSEI, SPTCIFICATIONS, REPORTS, AND ATTOWABI.E STRESSES

Sweden

The Swedish rules for the design of boilers and pressure vessels set the allowablestresses using only the yield strength and the rupture strength as follows:

UTS ys C

Unilctl Kingdom

The British rules for the design of boilers and pressure vessels are collectivelycalled British Standards. The basis for settine the allowable stresses is the leastof:

UTS ys

1.51.5All

R

Boilers-BS 1113

Pressure vesselsBS 5500Carbon steelStainless steel

2.7

2.352.5*

1.5 I _.'

I _J

l.J1.51.5

l.

RTTTR.ENCES

Srrrrlcn, A. M., and J. R. Mase, "ASME Pressure-Vessel Code: Which Division to Choose?",('hrt\k\tl lit|ineering, January ll, 1982.

lnrthorlt oJ luhular Exchanger Manufacturers.Asroc., 6th ed., Tubular Exchanger Manu-lrrllrrrr As$oci0lbn, White Plains, N.Y., 1978.

rl,JJ [l lcnr|t(rrlrtrr.

REFERENCES

ANSUAPI Standard 650, Welded Steel Tanks for Oil Storage, 7th ed., American PetroleumInstitute, Washington, D.C., 1980.

1982 AnnuaL Book of ASTM Standards, Afieican Society for Testing and Materials, Philadel-phia, Pa., 1982.

DIN Standa (Deutsche Normen Dll,lr, Herausgegeben vom Deutschen Normeruusschu(D,VA), Berlin, Gemany.

27

Page 24: Process Equipment

- - 2f l+u)'Fxy

i,=#n(* .,&*)

r1 = -q.C-/afu*razn1" i 2 (l -p'J \ayz ,,'I

L. t" a_w

^J i 211*u; a*aY

Th6ori6s, €riter;o, ond bosic equorions.

29

CHAPTER 3STRENGTH THEORIES,

DESIGN CRITERIA, ANDDESIGN EQUATIONS

Page 25: Process Equipment

30 sTRINGTH THEORIES, DESIGN CRITERIA, AND DISIGN TQUATIONS

3.I STRENGTH THEORIES

ln the design of process vessels and pressure equipment, two basic modes offailure may be assumed: elastic failure based on the theory of elasticity andplastic failure based on the theory of plasticity. Except for thick-walled vessels,

elastic failure is usually assumed for the design of pressure vessels. It is consid-ered to occur when the elastic limit of the material is reached. Beyond this limit,excessive deformation or rupture is expected. These limits are usually measuredin terms of tensile strength, yield strength, and, to some degree, rupturestrength.

Of the many theories developed to predict elastic failure, the three mostcommonly used are the maximum principal stress theory, the maximum shear

stress theory, and the distortion energy theory. The maximum (principal) stress

theory considers failure to occur when any one of the three principal stresses has

reached a stress equal to the elastic limit as determined from a uniaxial tensionor compression test. The maximum shear stress theory (also called the Trescacriterion) considers failure to occur when the maximum shear stress equals theshear stress at the elastic limit as determined from a pure shear test. Themaximum shear stress is defined as one-halfthe algebraic difference between thelargest and smallest of the three principal stresses. The distortion energy theory(also called the maximum strain energy theory, the octahedral shear theory, and

the von Mises criterion) considers failure to have occurred when the distortionenergy accumulated in the pad under stress reaches the elastic limit as deter-mined by the distortion energy in a uniaxial tension or compression test.

Engineers have known for some time that the maximum shear stress theoryand the distortion energy theory predict yielding and fatigue failure in ductilematerials better than does the maximum stress theory.r However. the maximumstress theory is easier to apply, and with an adequate safety factor it givessatisfactory designs. But where a more exact analysis is desired, the maximumshear stress theory is used.

Two basic theories of strength are used in the ASME Boiler and hessureVessel Code. Section I,2 Section IV,3 the ASME Code, VI[-1, and Section III,Division 1, Subsections NC,4 ND,5 and NE6 use the maximum stress theory.Section III, Division l, Subsection NB7 and the optional part of NC, and theASME Code, VtrI-2, use the maximum shear stress theory.

In the two sections of the ASME/ANSI Code for Pressure Piping 83l that are

used primarily with the ASME Boiler and Pressure Vessel Code, both ANSI83 l. l6 and 83 1. 3e use the maximum stress theory. 83 1.3 is unique in that it usesthe maximum stress theory but permits allowable stresses to be established onthe same basis as the ASME Code, VIII-2, which requires use of the maximumshear stress theory. The other sections of 831 also use the maximum stresstheory. They require that in addition to the stresses caused by intemal and

cxternal pressures, tiose stresses caused by thermal expansion of the piping are

to he considered.

3.2 DESIGN CRITERIA 3I

3.2 DESIGN CRITERIA

The design criteria for both Sections I and IV basically call for determining theminimum wall thickness that will keep the basic circumferential stress below an

allowable stress level. Additional rules and charts are included for determiningthe minimum thickness of various components. However, in general, a detailedstress analysis is required only for special designs. Sections I and IV recognizethat local and secondary stresses may exist in some areas of pressure vessels;

design details, however, have been established to keep these stresses at a safe

level with a minimum of stress analysis investigation.The design criteria of the ASME Code, VI -1, and Section III, Division l,

Subsections NC except NC-3200, ND, and NE, are similar to those for SectionsI and IV except that the ASME Code, VI[-I, and Section III, Division l,Subsections NC, ND, and NE require cylindrical shell thickness calculationsbased on both the circumferential and the longitudinal directions. The minimumrequired thickness may be set by stresses in either direction. In addition, theASME Code, VIII-1, permits the combination of primary membrane stress andprimary bending stress to go as high as 1.5 S at temperatures where tensile and

yield strength control and 1.25 S at temperatures where creep and rupturecontrol, where S is the allowable tensile stress values.

The design criteria for the ASME Code, VIII-2, provide formulas and rulesfor thd?nore common configurations of shells and formed heads for temperatureswhen the allowable stress criteria do not exceed the yield strength and tensilestrength range. Requirements include detailed evaluations of actual stresses incomplex geometries and with unusual loadings, especially if a cyclic loadingcondition exists. These calculated stresses are assigned various categories and

subcategories that have different allowable stress values as multipliers of thebasic allowable stress intensity value. The various categories and subcategoriesare:

Primary stresses, including general primary membrane stress, local primarymembrane stress, and primary bending stress

Secondary stresses

Peak stresses

Primary stress is caused by loadings that are necessary to satisfy the laws ofequilibrium between applied forces and moments. Primary stesses are not

self-limiting .

Secondary stress is developed by self-constraint of the structure. Its basic

chamcteristic is that it is selfJimiting. That is, rotation and deformation ordeflection take place until the forces and moments are balanced even though

some pennanent geometric changes may have taken place.

Lastly, peak stress is the highest stress condition in a structure and is usually

Page 26: Process Equipment

32 STRTNGTH THEORIIS, DESIGN CRITERIA, AND DESIGN EQUATIONS

due to a stress concentration caused by an abrupt change in geometry. This stressis important in considering a fatigue failure because of cyclic load application.

In general, thermal stresses are considered only in the secondary and peakcategories. Thermal stresses that cause a distortion of the structure are catego-rized as secondary stresses; thermal stresses caused by suppression of thermalexpansion, but may not cause distortion, are categorized as peak stresses.

Potential failure modes and the various stress limits categories are related.Limits on primary stresses are set to prevent deformation and ductile burst. Theprimary plus secondary limits are set to prevent plastic deformation leading toincremental collapse and to validate using an elastic analysis to make a fatigueanalysis. Finally, peak stress limits are set to prevent fatigue failure due to cyclicloadings.

The basic stress iniensity limits for various categories relating to an analysisaccording to the ASME Code, VIII-2, and Section III, Division 1, SubsectionNB, and optional Part NC-3200 of Subsection NC are:

Stress Intensity CategoryAllowable

Value

FactorBased on

YieldStrength*

FactorBased onTensile

Strength*

General primary membrane(P,) ks,

Local primary membrane(P") UKS^

himary membrane plusprimary bending (PM + Pd liks.

Primary plus secondary(PM+PB+Q)

3s, -!c

s) +s"

s, +s,

25, S-1(

In the ASME Code, VIII-2, and Section III, Division 1, optional Part NC-3200 of Subsection NC, a factor of ft is applied to various loading combinationssomewhat related to whether or not the loading is sustained or transient. Thelaotors are k = 1.0 for sustained loads including dead loads and pressure;k - 1.2 for sustained load plus wind or earthquake loads; t = 1.25 for hydro-$tiltic tcsts; and k - 1.15 for pneumatic tests.

'I'hc dcsign criteria for Section III, Division l, Subsection NB, are verysinrillr lo thoso for the ASME Code, VIII-2, except there is less use of designlirrrrrrrlrrs, culvcs, tnd tables, and greater use of design by analysis in Section IIL'l'h(. cfllcgorics ol slrcsses and stress intensity limits are the same in both sec-liorrs.

+AiiurriflI lhrt I | .O. ,\,,, (lcsiSn strcss intensity valuc fbr Section III, Division l, SubsectionNll, n[(l thc |

't{ i',nrl pIr I {rl S hsr(.li()n NC, and thc ASMts Codc, VIII-2 (psi), S" = yicld strength

(plri). url ,\, ultirrxrtc k nsil(. slfrJrgth (psi)

3.4 STRESS-STMIN REIATIONSHIPS

3.3 DESIGN EQUATIONS

Once the allowable stresses are set, the basic design equations must be devefoped. The design of process equipment is based on the assumption that thematerial generally behaves elastically at the design pressure and design tem-perature. Accordingly, most of the equations are derived from the theory ofelasticity and shength of materials basis.

3.4 STRESS-STRAIN RETATIONSHIPS

The stress-strain relationship at any point within a homogeneous, isotropic, andlinearly elastic body that is subjected to a system of forces is obtained from thetheory of elasticity. Referring to Fig. 3.1, the stress-strain relationship is givenby

1.e,: ELo,-

p(oy + ozl)

t.er =

ELor- ploz 'r o^)J

Ie, : ;lo,- tt(o, I o)l (3.1)- I1- -

rs 2(1 + 1t),DGE

2(l + 1t)^lv = ---V- rn

2(1 + 1t).t/,- =

-

i--L

Or, in a different form.

(r+ tt)(1 -zp.)

(1,+p.)(1 -2tt)

[e,(l - pc) +

[e,(1 - p) +

p,(e, + e,)]

p.(e" + e")l

(l + p)(1 -Ii^,

: " ltl2(l + 1.t)

T,

- [€,(1 -LIL)

pr,)+p(e.+er)] (3.2)

Page 27: Process Equipment

34 STRENGTH THIORIES, DTSIGN CRITERIA, AND DESIGN EQUATIONS

' f1---> <-f3

t2

I@I t"lt4

(b)

II

,v

Figure 3.1 Slrcls rerulianr ot o point wirhin o homogeneous, isotropi<, ond lin€orly eldsri. body.

F.,r, = zG; tL)

Ev-Tn : ;:;---,----.._L\r t trL)

where eb ey e,: axial strain in the.r, y, and z-directions, respectively

oo o, oz = axial stress in the .r, y, and z-directions, respeptively

"y,!, yr,, y- = shearing strain in the -r, y, and z-directions, respectively

re, T

rz, rp : shearing stress in the.r, y, and z -directions, respectively

E = modulus of elasticity of material (psi)

G = shear modulus of material (psi)

1,c : poisson's ratio

In most pressure vessel applications, the values of o,, rr,, and r,, are relativelysmall compared with o, and or. Hence, they are normally ignored and the

3.5 STRAIN-DEFTECTION EQUATIONS

equations reduce to

35

Or, in a different form,

1.e,: E\ox - psr)

t.q= i\ar- Po')

€,: Elo' + stl

2(1 + tt)f"y = --E- r"t

o, = ---! ,1u" * *rsL-p-

o,:;\1e, + p'est- lL-

c,:0E

',=76+ iil*

(3.3)

(3.4)

3.5 STRAIN-DEFLECTION EQUATIONS

Figure 3.2 is cross section of a pressure vessel wall. It undergoes an extensionin the niddle surface of €o due to stretching plus extension due to bending. Theoriginal length lr at a distance z from the middle surface is given by

t,=adr-1\

The final length l2 after extension is

tz: dstt + .*r(r - 4)\ r./

whereas strain is given by

lr- lt,": l,

Page 28: Process Equipment

36 STRENGTH THEORIES, DESIGN CRITERIA, AND DESIGN TQUATIONS

Fisure 3.2 Cross s€ction of o sh€ll woll subie€ted to str€rchine ond bendins lodds'

Substituting the values of lr and lz into the above and deleting all small terms

results in

( t l\€.: €or _ ,\,:_ i) : e0,_ z. x\

where 1, is change in curvature. Similarly,

/ r l\€n : €ou -,\4- i) = es - z' xt

Substitution of the above two equations into Eq. 3.4 gives

Fo,: ,-:--Lr" + peo! - z(y" + trt'yt)

t-lt-tiq- ,--l€vt + l"r*- z(Xr+ PX')t- lL-

Nolr llrirl llr(' cx|)tcssirttt f, is related to the deflection by the expression

dzw / dx2x'=tt+kt"4'hffn

(3.5)

3.5 STRAIN.DEFTECTION EQUATIONS 37

However, because the quantity dw fdx is smal! compared with unity, the expres-

sion above becomes

d2w . d2wX': 77 a;to Xt = 7F

Hence, Eq. 3.5 may be written as

(3.6)

(3.7)

(3.8)

The shearing strain-displacement relationship can be obtained from Fig. 3 3.

The quantity 7," is shown in Fig. 3'34 and can be expressed as

"l'Y:"loq+a+P

where 7qry is the shearing stress due to in-place forces and d and B are due to

twisting moments. Also, from the figure,

. (d/ d\'ldv dud-srna -__6-: dy

(dD/?x)dx 0aIJ-srnP- d, =A

*=T+1^+ peo,-,(#. - *fu)lE I ldzw, drr\'lot: T7 *.leb

+ Pew - '\dy, - It dr') l

du 0af,t: Ioq, dy- a,

and

From Fig. 3.30, which represents the middle surface, the rotation is given by

-@w I Ai. The minus sign indicates counterclockwise rotation. As a result ofthis rotation, any point at a distance z from the middle surface will have a

deflection of

dw

dx

Page 29: Process Equipment

38 STRENGTH THEORIES, DESIGN CRITERIA, AND DESIGN EQUATIONS

z tD,

Figura 3.3 Sh€or dolormdliom of o unit cro$ .ection.

dteD = -Z--dy

Similarly,

-\,/./,?--zt,--'-,..'7 |t _----,- tu..-..

-

|_-,l-_

Hence Eq. 3.8 becomes

3.6 FORCE-STRESS EXPRESSIONS

And Eq. 3.4 becomes

^, :^'^ - )2-:----:-$y rvt -- dx b

39

(3.9)

3.6 FORCLSTRESSEXPRESSIONS

The force-stress relationship for the cross section shown in Fig' 3 4a can be

exDressed as

",=c("* -*#)

In the majority of cases, the quantity z/r is small with respect to unity and can

thus be dlsregarded. Also, substituting Eqs. 3.7 and 3.9 into 8q 3 10 gives

*,= f',,",(r - z\a,

N,= [n( - )a"n"=[,"(t-i)a"

u,=1,,,\t-z)a'

u.= [".'lt - z)a"

u,= J",'lr - i)a,

,, = -[ ,,'lt - 1)a"

u*= [,,",(t-4;,

(3. 10)

Page 30: Process Equipment

40 STRENGTH THEORITS, DESIGN CRITERIA, AND DESIGN EQUATIONS

,/

N.

N,

Et= r r(€0r+ /,€q,r-lJ'

Ft: .--------t (€0) + p€0r.)

l- lL'

1'u,Et2(l + 1t)

N,}

3.6 FORCE.STRESSEXPRESSIONS 4l

(3.1 r),.:&(#.#)u,=ffi\(*tu.

,*tu)

,. Eilt - tL) drwl2ll - lt2t ax dy

Example 3.1 Stresses are to be determined at the inside comer of an opening

in a cylindrical shell by applying strain gages at the location. The cylindricalshell is carbon steel with E : 29.9 x 106 psi and p : 0.3. The strain readings

from the three gages are €,: +360 x 10-6; €): +180 x l0 o and e' =-230 x 10-6. What are the stresses in the three principal directions at the

opening?

Solutian. Using the equations given under Eq. 3.2, the stresses are determined

AS

,oqo,: ;#1Q60X0.7) + 0.3(180 - 230)l : 13'630 psi( r.Jrw.+.,

,qq",: -*l(180)(0.7) + 0.3(360 - 230t1 = 9499 O.;' t r.JJ(u.+,

?qoo = "'' tr-?10rr0.7) + 0.3(360 + 180)l : 60 psi I(1.3x0.4)" --""'

Exanple 3.2. What are the stresses in the two principal directions of the

cylindrical shell with the o, = gt

Solution. Using the simplified equations given under Eq. 3.4, the stresses are

determined as

', =ffioso + 0.3 x 180) = 13,6oo psi

o, =ffi{rto + 0.3 x 360) : 9460 psi r

Page 31: Process Equipment

42 SIRTNOTH THEORI€S, DTSIGN CRITERIA, AND DESIGN EQUATIONS

Problems

3.1 Strain gages are attached to the surface of a tube subiected to internalpressure. The gages lie along the circumferential and l,ongitudinal axes.The tube is carbon steel with t = 29.9 x 106psi, 1.r,

: 0.3, and the stressat the surface in the circumferential direction is 17,500 psi. What are thestrain gage readings in the two directions?

Answer: e,: *498 x 10-6

€i: +117 x 10-6

3.2 In the tube of Problem 3.1, what is the strain in the z -direction? Usins thatanswer and the other answers in Problem 3.1, what are the calcrilatedstresses in the three directions?

Anst'er: a" = 17,500 psi

o" = 8,750 psi

o"=o

REFERENCES

7.

Criteria of the ASME Boiler and Pressure Vessel Code for Design by At],',ltsis in Sections IIIand VIII, Division 2, American Society of Mechanical Engineers, New york, 1969.ASME Boiler and Pressure Vessel Code, Section I, Power Boilers, ANSVASME BPV-I,American Society of Mechanical Engineers, New york, 1983.

ASME Boiler and Pressure Vessel Code, Sectionly, Heating BoiIeB, ANSVASME BPV-IV,American Society of Mechanical Enginers, New York, 1983.

ASME Boiler and Pressure Vessel Code, Section III, Division l, Subsection NC, Class 2Components, ANSUASME BPV-m-I-NC, American Society of Mechanical Engineers, NewYork, 1983.

ASME Boiler and Pressure Vessel Code, Section III, Division l, Subsection ND, Crllrr.iComponents, ANSL?ASME BPV-III-1-ND, American Society ofMechanical Engineers, NewYork. 1983.

ASMII Boiler and Pressure Vessel Code, Section III, Division l, Subsection NE, Class MC(i)tnpt,nt',ttr, ANSTASME BPV- I-l-NE, American Society ofMechanical Engineers, NewY,nk, 1983.

ASMIj lllrilcr and Pressure Vessel Code, Section III, Division 1, Subsecrion NB, CIaJJ 1( t'ntt\'tl' t.t, ANSI/ASME BPV- I-l-NB, American Society ofMechanical Engineers, NewY(n (. l()8lASMf i ( \nk. li,r I'rcssurc PipingB3l, Power Prping, ANSLIASME 83l.1, Amedcan Societyol Mrrhfiri(nl li[8inccrs, New York, 1980.

ASMf (irtfc lix Prcssure Piping B3l, Chemical plant and petroleum Rertnery pipin|,ANSI/AliMll ll I I L Amcr'can Soc'ety of Mechanical Engineers, New york, 19g0.

BIELIOGRAPHY 43

BIBTIOGRAPHY

Brownell, L. E., and E. H. Yoi{Irlg, Process Equipment Design, John Wiley, New york, 1959.

FattWI, J, H., Engineering Design, John Wiley, New York, l9&.Ha0ey, J. F., Theory and Design of Modern Pressure Vessels,2nd ed., Van Nostrand-Reinhold,

Princeton, N.J.

Seely, F. B. and J. O. Smith, Advanced Mecfuinics of Makriak,2nded., John Wiley, New york,1952.

Page 32: Process Equipment

CHAPTE R 4MATERIALS OF

CONSTRUCTION

Top: Metologroph of titanium wetd. Boltom: Tonrolum_ctdd veset (Courtesy of rhe Nooter Corp., Sr. l"ouis,

44

Page 33: Process Equipment

46

4.I MATERIAL SETECTION

MATERIALS OF CONSTRUCTION

The vast majoriry of vessels are constructed of ferrous and nonferrous alloys'

Ferrous alloys are defined as those having more than 50Vo iron They are used

in the eSME Code, VI[-l and 2, and include carbon and low-alloy steels'

stainless steels, cast iron, wrought iron, and quenched and tempered steels'

Nonfenous alloys include aluminum, copper, nickel, titanium, and zirconium

The ASTM designates all ferrous alloys by the letter A and all nonferrous alloys

by B. ASME uses the prefixes SA and SB, respectively ln most cases the ASME

unO eSfV specifications are identical. However, vessels built to the ASME

Code usually refer to the ASME specifications'Nonmetilic pressure vessels may also be constructed to the ASME Code'

Recently, ASME Section X was published to include fiberglass-reinforced plas-

tic (FRij vessels. Details of construction are given in Section 46' Concrete

vessels are also being considered by the ASME However, no specific rules are

available at this time.Selecting materials that are adequate for a given process is complicated and

depends on many factors such as corrosion, strength, and cost'

4.1.1 Corrosion

Corrosion,whichisdefinedasthedeteriorationofmetalsbychemicalaction'is probably the single most important consideration in selecting materials A

stigtrt ctrange in the chemical composition of a given -environment

can sig-

nifi'cantly cilange the corrosive behavior of a given metal This is illustrated in

epp""Oi* H, i,trich lists various environments and their effect on different

ferrous and nonferrous alloYs.

In a new chemical process, it is prudent to determine the factors that affect

the corrosion and then run tests on various materials in order to select the most

suitable one. Figure 4.1 shows an example of a heat exchanger.used in "city

water" service. The corroded tubesheet is made of carbon steel and the un-

corroded tubes are made of copper' Another example shown in Fig 4'2 is a

titanium lubesheet after exhibiling crevice corroslon'

fn nighty corrosive environments, every phase of the pressure. vessel fabri-

.ution pio""r, rnurt be evaluated for corrosion' Items such as buming' forming'

weldini, stress relieving, and polishing must be.considered Figure 4 3 illus-

trates a"Hastelloy C chu-te with corrosion in which marking Points were left on

rnu,"tlut Ou.ing h"ut treatment. Conosion at points of high stress along the break

lines can also 6e seen. In Figure 4.4, a Carpenter 20 tube shows knifeline attack

at a plug weld (shown by arrow) in a bayonet tube used in hydrofluoric acid

service.The cleanliness and finish of the inside surface of a pressure vessel before its

opcrltion ilrc vsry imPortant in preventing subsequent .c.onoslon in service'

Many uscrs tcquirc spccial clcaning proccdutcs ol'the insitlc surlace Prior to lts

insl;rllaliott.

Fisure 4.1 Cotroded corbon sleel lubesheet. (Courl$y of the Nooter Corp., St. touis, Mo.)

Frrruro 4.2 Corroded rirqnaum tubesheet. (Courlesy ol the Nooler CorP, Sr' touis, Mo )

Page 34: Process Equipment

Fisure 4.3 Hosrelloy C chure. (Courtesy o{ the Nooter Corp., Sr. rouk, Mo.)

48

Fisure 4.4 Crock in o Corpenter 20 lube weld. (Court6y of Nooier Corp., Sr. toui., Mo )

4.I MATERIAT SITECTION

4.1.2 Strenglh

The strength level of a material has a significant influence on its selection for a

given application. This is especially true at elevated temperatures where theyield and ultimate strength are relatively low and the creep and rupture behaviormay control the allowable stress values. In the ASME Code, VIII-l, the criteriafor allowable stress at elevated temperatures take into account both the creep and

rupture behavior as discussed in Section 2.4. In applying the ASME criteria forallowable stress as given there, the following procedures are used.

Specified Minimum Yield Stress

In obtaining the minimum yield shess of a given material, test data are plotted

at vadous temperatures as shown in Fig . 4 . 5 . A smooth trend curve is then drawn

though the averages of the data for individual test temperatures. The specified

minimum yield stress curve is obtained by applying to the yield trend curve the

ratio of the specified minimum value, as given in the material specification, to

the trend value of 80"F.

temperature,"F

Figure 4.5 Tensile ond yield 3irengrh.

49

o 200 400 600 800 1000 1200 1400 1600

Page 35: Process Equipment

!0 MATERIATS OI CONSTRUCTION

Sptcllled Mlnlnum 'l'ensile Siress

'fhe tensilc trend curve is determined by the same method as the yield trend curveincluding_ th-e,.ratio factor. The specified minimum tensile striss is arbitrarilytaken as I l07o of the tensile trend curve, as illustrated in Example 4. 1

Creep Rate

In order to establish the creep rate of lVo /lffi,O}} hours, data are plotted asshown in Fig. 4.6. Interpolation and extrapolation may be needed to establishthe creep rate for various temperature levels.

.0001

Figur€ ,{.6 Cre€p strengrh.

4.I MATTRIAI. SETECTION

Rupture Slrength

Test data are normally plotted as shown in Fig. 4.7. In some cases the data needto be extended to 100,000 hours and must be done with extreme care to extraD-olate accurately.

Example 4.1. A user is requesting code approval for a new material that hasa minimum specified tensile stress of 120 ksi and a minimum specified yieldstress of 60 ksi at room temperature. Tensile and yield values for various heatsand temperatures are shown in Fig. 4.5. Creep and rupture data are given in Figs.4.6 and 4.7, respectively. What are the allowable stress values at 300 and 1200'Fbased on criteria siven in Section 2.4?

1,000

Llle llrs.

Figur€ 4.7 Rupture strengrh.

5l

Page 36: Process Equipment

52

Solution

MATERIATS OF CONSTRUCTION

Allowable Stress at 300'F

l. From Fig. 4.5, average tensile stress = 130 ksi.Tensile stress reduced to minimum : l3O x 120/140: 111 ksi.Specified minimum tensile stress : 111 x 1.10 : 122 kst.Maximum stress to be used cannot exceed 120 ksi.Allowable stress based on tensile stress : 120/4 = 30 ksi.

2. From Fig. 4.5, average yield sffess : 60 ksi.Yield stress reduced to minimum : 60 x 60/75: 48 ksi.Allowable stress based on yield stress : 48 x 6 = 32 ksi.

3. From Figs. 4.6 and 4.7 it is apparent that creep and rupture are not a

consideration at 300'F.

4. Therefore, maximum allowable stress at 300"F = 30 ksi

Allowable Stess at 1200"F

1. From Fig. 4.5, average tensile saess : 112 ksi.Tensile stress reduced to minimum : lI2 x 120/1,4O: 96 ksi.Specified minimum tensile stress = 96 x 1.1 : 106 ksi, which is less

than maximum allowed of 120 ksi.Allowable stress based on tensile stress = 106/4 : 26.5 ksr.

2. From Fig. 4.5, average yield shess = 54 ksi.Yield stress reduced to minimum = 52 x 6O/7t: 42 ksi.Allowable stress based on yield stress = 42 x 6 = 28 ksi.

3. From Fig. 4.6, creep stress for 0.O1Vo rn 1000 hours = 15 ksi.Allowable stress based on creep = 15 ksi.

4. From Fig. 4.7. stress to cause rupture at 105 hours = 22 ksi.Allowable stress based on rupture = 0.67 x 22: 14.7 ksi.

5. Therefore, maximum allowable stress at 1200"F = 14.7 ksi. I

4. I .3 Moteriol Cost

llt'r'rrrrsc costs of materials vary significantly, the designer must evaluate mate-riirl (osl vcrsus other facton such as corrosion, expected life of equipment,Ivrrilirl'ility ol material, replacement cost, and code restrictions on fabricationrrrrl rr'1ririrs. n summary of the cost of some frequently used materials is givenrn l irlrlt ,l. | . With the large difference in cost, the designer should consider thelrx l(xs ltfior' 11r sclccting a given material.

4.2 NONFERROUS ATLOYS

TqblE 4.1 Approximote Cost ofMqteriqls Used in Pressure VesserConslruction

Cost inType Dollars/lb

0.30

0.7 5

0.90-2.501.50

t.'7 5

4.00

5.00

6.00

15.00

15.00

20.00

250.00

Carbon steel

Low-alloy steel

Stainless steel

AluminumCopper, bronze

IncoloyMonel

Inconel

Hastelloys

TitaniumZirconiumTantalum

'As of January 1983.

4.2 NONFERROUS ATLOYS

The 1983 ASME Section VIII Code, VI[-1, lists five nonfenous alloys for codeconstruction: aluminum, copper, nickel, titanium, and zirconium. These alloysare normally used in corrosive environment or elevated temperatures whereferrous alloys are unsuitable. Nonferrous alloys are nonmagnetic except forcommercially pure nickel which is slightly magnetic.

4.2.1 Aluminum Alloys

Aluminurn alloys have a unique combination of properties that make them usablein process equipment applications. They are nonmagnetic, light in weight, havegood formability, and have an excellent weight-strength ratio. Aluminum sur-faces exposed to the atmosphere form an invisible oxide skin that protects thernetal from further oxidation. This characteristic gives aluminum a high resis-lance lo corroslon.

Aluminum alloys have a systematic numbering system as shown in Table 4.2.'l he specification number also designates the various product forms. For exam-plc, SB 209 applies to plate products, and SB 210 applies to drawn seamless tubelxrtlucts. The first digit of the alloy designation number indicates its majorrllloying element as shown in Table 4.2.

All aluminum alloys are categorized by ASME specification number, alloy

Page 37: Process Equipment

54 MATERIATS OF CONSTRUCTION

Tqble 4.2 Aluminum Alloy Designotion

EXAMPLE+

designation, and temper designation as shown in Tables 4.2 and 4.3. Some ofthe terms in the tables are defined as follows:

Annealing.

Consists of heating the material to a given temperature and then slowlycooling it down. The purpose is to soften the material in order to remove coldworking stress.

Norm.alizing.

Consists of heating rnaterial to a temperature slightly higher than the an-

nealing temperatue and then cooling at a rate that is faster than annealing.

S o lution H eat Tr eatin g.

Heat heating at a temperature high enough for the alloys to be randomlydispersed.

Stahilizing.

A low temperature heating to stabilize the property of an alkry

,.ffi"ffi#*EffidF-Jfit<,6lLlfY.

"'ffi,#P.*,fffr4ffi..ffisffi*t' ffi.,,ffi*.ffi.ffi";^318H:" ,oPt-tcar td€

'' H&.,ffi'#^E lH,ffia'.nn5.

fFEATAa-E ILLOY.

5. tAtN ADV$J'AA IS fl,.l tT ls t€^I-lnElr a-E.

7, TLTRA HIgl S'FE €7H FFCENTTE!'' M)' USEDIN ffi.

C ST'TGFLITES(n^|?{ sElra-EssNEfr-TttaF4t5, A4ASa $aPElicEr€E €EF a |€,/17E(U{A'GF ltE

ffiffi6-nEDIE I TUTOFffi'T€S

DEGREE G C@,ITF|OL OFTE]FER OR TO IENTIFYA STECIAL s,ET G MECH-

NONIERROUS ATTOYS

Toble 4.3 Temper Clossificotion For Aluminum Alloys

Stain Hardening.

Modification of metal structure by cold working resulting in an increase instrength with a loss in ductility.

Thermal Treating.

Temperature treatment of an alloy to produce a stable temper.

4.2.2 Copper ond Copper Alloys

Most copper alloys are used because of their good corrosion resistance and

machinability. They are also homogeneous as compared with steel or aluminum

and thus not susceptible to heat treatment' Their strength, generally speaking,

may be altered only by cold working. The alioy designation system serves to

identify the type of material as shown in Table 4.4. Alloys 101-199 are normallya high grade copper with very few alloys added. Alloys 201-299 normally refer

b brass products that are mainly copper and zinc. Alloys 501-665 are bronze

products composed of copper and elements other than zinc. Other properties ofcopper alkrys are also sbown in the Table.

Jf

2- At'tt.€ALm3- nLUT TO.J HT TI]EN

"- #?,'ffif fi? ,HEN NATLTRALLYAGED TO sTAfuE COI'IDIT ION

5- ARTIFICIALLY AGED o/v-Y6- SLUT lc',l HT TIIEN

ART]FICIALLY AGED

a.ffiiig,rri;p:::ffi!*r9- SOLUT IO'I HT, ARTIFICIALLY

AoEO. T'/FN COLD IItrT<EDO- ARTIFICTALLY AGED TTEN

COLD V@KEO

Page 38: Process Equipment

56 MATERIALS OF CONSTRUCTION

Tqble 4.4 Copper AlloYs

Alloy Designation of CoPPers

l0l-19920tJ99301-399401-499501-599

601-64564s-665666-699701J30

Coppers

Copper-zinc alloys (brass)

Copper-zinc-lead alloys (leaded brass)

Copper-zinc-tin alloy (tin brass)

Copper-tin alloy (phosphor bronze)

Copper-aluminum alloys (aluminum bronze)

Copper-silicon (silicon brcnze)

Miscellaneous copper alloys

Copper-nickel alloys

Cold-Worked TemPer Designations

Approximate 9o ReductionbY Cold Working

Qua(er Hard

Half hard

Three-quarte$ hard

Hard

Extra hard

Spring

Extra spring

r 0.9

20.7

29.4

31 .l50.0

60.5

68.7

Most copper alloys are distinguishable by their color except for Cu-Ni alloys

that tend to lose their color as the amount of Ni is increased

4.2.3 Nickel ond High-Nickel Alloys

Nickel and high-nickel alloys have excellent corrosion and oxidation resistance

that makes thJm ideal for high temperature applications with corrosive environ-

ments. Products are normally called by their commercial names rather than their

ASME designation number as shown in Table 4 5'

4.2,4 Titonium ond Zirconium Alloys

Titanium and zirconium alloys are used in process equipment subjected to severe

environment. In the ASME Code, VIII-1, unalloyed titanium is listed for grades

I , 2, and 3, and alloyed titanium is listed for grade 7. Two zirconium grades also

given in the Code are unalloyed alloy 702 and alloyed alloy 705'

The modulus of elasticity for both titanium and zirconium is about half that

ol stccl. Also the coefficient of thermal expansion of both is about half that ofstccl. I'hc dcnsity o1'zirconium is slightly less than stcel' whereas the density of

lilrr|lirrrr is irlrottt 0.5ti lirttcs thltt ol stccl.

o

HFr".3;o

.t2 ax

9-B-zF

F

E

z

U'

B;=a. ,B t:

>doF<AE

\D \O \O oO\o \o- \o d @ o- a': a T 5 Tco of co cD rq ca IU) tan U) u) a a I

E E Eora ra diA A U) \J

EoS E g,.E$ 5dicc ca rq...j Ecco ea\)a a u1 v u) rh a

\o

\o \o \o

ta) tt) A I

vt(hu)l

\o \o \o

q

Y < flSd - -6=aa-.i,:,i,9JVCq9vY-ii

2222222222

ccg,,-56I ; r'i XEE ida 2e 2a2^::;. F23888A838:E;8t=e

z€ zcz44aa3z4

\or

I r IQCQ II I .J1 U) |

rr + a- C-+\oi + @ O-ir) + : <f r)

I aa a t4 av)

\o sf \o

lv)aa

IIi

a ao ! Q n Rv v> v 6 G 6

€ 'r,88

n^:i^v6 VoZ\J ZY

l= Izz z>v

Page 39: Process Equipment

al aoH5 g 6AA n | 3 |

F-

ra) a-v-' \o

l(ha-tY

; g nE H E

/\/txX XE AH O:';Qo;FQ;Fe36g.Sd)i dliH C:F JJ.o i6\3g5Eg6s€9lsd€

Yqrarartlu)all

I |:SX'i -iitr ocq | |ttt ca u) | |

El

nl)< i{><> x 5

C)

t

O

26n*i.i ,9, ,9+t-zzz

R=CJ

al

UO

II.

zo

Ut!z

5958

$na*$qfi qqra33383nltsa

$na$$qqqqqt3,38nA3nn3F^

s q s€$3$€$€$$$€ € qqAAEn'-n3333a3383 t83

$ $ 3 e 3 g ? q qq q

A A e n E 3 a lnl | 3

s$$nHfiH$$+qnAaeBSaaSSa

.J r.) c.r <l i\ ^r toiisiotidooozx

a^r'i=-=gg EEEEttgiss!ig$gqB622t2322222

EuEt sc ig ig I5 ic kc ic Ig Ig

q- *EEU

e&"€

s? a-aEP3-EE& (./t

O

g.rrrr{a

ln

zE)

o- q

=- *A

1!IU;i

i

Page 40: Process Equipment

MATERIATS OF CONSTRUCTION

4.3 FERROUS ALTOYS

Iron alloys with carbon content of less than 2qo arc known as steels and thosewith more than 27o are known as cast iron. Steels are further divided into those

with carbon content of more than 0.87o, called hypereutectoid steels, and those

with carbon content of less than 0.87o, known as hypoeutectoid steels. Moststeels used in pressure vessel applications have a carbon content of less than

0.47o. Steels with carbon content of over O.4Eo are very brittle and hard to weld.Cast iron used in pressure vessels dates back to the nineteenth century.

However, because cast iron is very brittle and because it cannot be rolled,drawn, or welded, its use in pressure vessels presently is limited to complicatedcomponents and configurations. The ASME Code, VIII-I, also imposes lim-itations on the pressure and temperature ranges and the repair methods.

Steel alloys can be produced with a wide variety of alloying elements. Someof the common elements and their effect on steel products are shown in Table4.6. The ASME Code, VIII-1, divides steel alloys into the following categories:

Carbon Steels.

These are widely used in pressure vessels. They have mainly silicon and

manganese as the main alloying elements and are limited in temperatureapplications to about 1000'F.

Low-Allny Steels.

These are essentially cbromium (up to l07o), Molybdenum, and nickel-alloy

Tqble 4.6 Effecl of Alloying Elements in Sfeel

AdvantagesElement Advantases Element

AluminumChromium

Restricts grain growth

Incrcases resistalca tocorrosion and oxidationIncreases hardenabilityAdds strength at hightemperature

Counteracts sulfurbrittlenessI ncrcases hardenability

l{ iscs grain-coarseningl('l|ll)crilturc( illrrlcrircls tcndencyt(,wirr(l lcnrpcr brittlenessIinllnrl(cs corrosionl( sislirtlec

Strengtheqs annealedsteelsToughens steels

Improves oxidationreslstanceIncreases hardenabilityStrengthens steel

Prevents formation ofaustenite in highchromium steels

Prevents localizeddepletion of chomiumin stainless steel duringlong heating

Increases hardenabilityRcsists tcmpcring

MirrUlocsc

Molylrk rrrrrrr

Titanium

Vanadium

4.4 HEAI TREATING OF STEETS 6I

steels. lhese elements enhance the steel for high temperature applications and

in hydrrigen service.

High-Alloy Steels.

These are commonly refened to as stainless steels. They have mainly chro-mium (over lOVo), nickel, and molybdendm alloys. The basically three types

of stainless steel used in process equipment are as follows:

M artensitic Stainless Steels.

This group includes type 410, which has a low chromium content of slightlyabove lTEo. They behave like steel, are magnetic, heat heatable, and difficultto fabricate.

Feffitic Stainless Steels.

This group includes types 405 and 430. They are magnetic but not heat

treatable.

Aust enitic Staink s s Ste e ls.

This group includes all 200 and 300 series and are chromium-nickel andchromium-nickel-manganese steels. They arc nonmagnetic and not heat

heatable.

4.4 HEAT TREATING OF STEELS

The lattice structure of steel varies from one form to another as the temperature

changes. This is illustrated in Fig. 4.8. Between room temperature and 1333"F,

the steel consists of what is known as "ferrite and pearlite." Ferrite is a solidsolution of a small amount of carbon dissolved in iron. Pearlite, which is shown

in Fig. 4.9, is a mixture of ferrite and iron carbide. The carbide is very hard and

britde.In Fig. 4.8 between lines A1 Qower critical ternperature) and A3 (upper critical

temperature) the carbide dissolves more readily into the lattice that is now called"ferrite and austenite." Austenite is a solid solution of carbon and iron that isdenser than ferrite.

Above line 43 the lattice is uniform in property, with the austenite the main

structure. The actual temperature for this austenite range is a function of the

carbon content of the steel as shown in Fig. 4.8.With this brief description, we can now discuss various heat treatments of

carbon steel.

Normalizing.

This consists of heating the steel to about 100"F above the upper critical lineAi and tben cooling in still air. The purpose is to homogenize the steel

structurc and oroduce a harder steel than the annealed condition

Page 41: Process Equipment

MATERIATS Of CONSTRUCTION62

'ri

=

PERCENT CARAON OF WEIGHT

Fisure 4.8 lron-iron corbide equilibrium didsrom'

ANNEALED

PEARLITE

NORI'ALIZEDPEARLITE

Figure 4.9 P€arlile 3tructure.

llrrr r'orrrisls ol lreating the steel to about 50'F above the upper critical line

,4, lrrrl tlrlrr ltttttittt cortling slowly. The purpose is to refine the grain and

rtrlttr'r srtllttr'ss

634.5 BRITTTE FMCTURE

Posweld Heat Treating-

It consists of heating to a temperature below the lower critical temperature-rJil- f- rft" purp;se of reducing the fabrication and welding stress and

softening the weld heat-affected zones'

Quenching.

The rate of cooling of steel after heat treating is very important in e-stablishing

ifr" ft.an"t. of st"eel Some steels such as SA-517 obtain most of their high

,t "ttgtft

Uy qt"*fting. The rate of cooling.depends on manY.factors such as

qu"nittlng -iAiu., tlmperature of quenching medium' and size and mass of

the part.

Tempering.

Ouenched steels are very brittle. In order to increase toughness' they are heat

;;;; il"* ;.;d then cooled to produce the desired propertv of high

strength and good toughness.

4.5 BRITTTE FRACTURE

Pressure vessel componenllconstructed of ferrous alloys occasionalllfail:ht-

i*tir;at"d,=A;".-"p:.-Iormalopqr3tingtdlFPeratureatalnressurewellilliiffi=0.;-;ftJG d*-i i"ir'* $"Jutt! o'"u'' ut to* !;'i-{'n"'1r iooffilrir;d uy incorporati4g.ufg1e fracture -coriiiderations

at the d€sgn

ffi ffirf .;Oiiticaiion requlreO vaiies from the simplest state-of-

il::* ;;d;dTi;,rt""t"iii.o.pri*tei mathematical analvses Both extremes

;; ;i;ii;,h;;i;isure uessel'designer, and their application ^depends

on the

amountofinformationavailableandtherequiredreliabiljtyolaglvencom-ponent.

Charpy V-Notch Test (Cv)

The Cv test is the simplest and most popular method of qualitatively determining

ffi'rrl."--i-Grl^cF*-TASTM- A-370_-and consistf of impact teslrn_g 9-n:sl:dJp.j"r_Tglllg: lljStaken from a spbcifib location of a product lorm. l he speclmen ls srucK wlln a

falling weighi(Fig.4.l}b) and the energy required to fracture it at various

tempJratures is recorded. Figure 4.11 shows two typical plots of the temperature

versus absorbed energy. The magnitude of measured energy, shape of energy

curve, and appearance of the cross section of tested specimens are all significant

in evaluating material toughness.

Page 42: Process Equipment

(a) srnolno specruel

ffil fn',n| | '-*nn

(c) pencert or sxeln rnlctuneAFTEB TESTII'IG.

Fig'rre ,1.10 Chorpy V-notch sp€c'men.

=sI

z

I

(b) resr ann*rormeu

cuRvi(A) CURVE(s)

64

Fisure 4.ll Cv En€rgy tronlilion €urye..

4.5 BRITTTE FRACTURE

The magnitude of energy level at a given temperature varies with differentsteels, as shown in ASTM 4-593. An energy level of 15 ft-lb is consideredadequate for 4-283 steel at room temperature. However, such a level is exceed-ingly low for .4-387 steels. Recognizing this fact is imperative in specifyingenergy requirements for various steels at different temperatures.

The slope of the energy curve in Fig. 4.11 gives the rate of change of steeltoughness with increasing temperature. At the bottom shelf of the curve, thesteel is very brittle as indicated by the cleavage appearance of the tested specimen. Failure is normally abrupt. At the upper shelf, material fails in shear and

- the cross section has a dull area. Failure bicurs after excessive yielding. [ow]--.r-o"ttgm;f"@Slt W,q sharp increase in toughness as the temperaiure increases,

as sho_wnin_Curve,4 qf Fig. 4 1 l. @-. as-sharu!_!J_ rfrrvx g-rn-\E:-.4.1t. This slight increase in toughness makes the

Cv test impractical to use in high strength steels.of dull and areas in the cross section of tested

nil ductility temperature.The nil ductility transition (NDT) temperature shown in Fig. 4.11 is of

significant importance when considering low strength steels. This temperature isbelow which the fracture appearance of steel changes from part shear to com-plete cleavage. Thus, this temperature is below which vessels with low strengthsteel must not operate without a detailed fracture evaluation.

The Cv tests give a good qualitative indication of fracture hends. TlpylQlot,however. eive anv coffelation between enersv and stress levels. Such informa-tion G-neeh wriirJ i-strisianaiviii is ftooila. roitrti.-iJ*n. other methodswere devised such as the drop weight test {DWT) established by the U.S. NavalResearch. Laboratory .

Drup We@ht Test (DWT)

The DWT procedure is given in ASTM E-208 and consists of welding a brittlebead on a test specimen. The bead is then notched and the specimen impactl$ted at various temperatures. The NDT temperature is obtained when thespecimen does not break upon impact.

In testing the specimens, deflection can be limited such that the stress atfailure does not exceed the yield value. Thus, a direct correlation is establishedbetween the NDT temperature and yield stress. Such information is used inconstructing the fracture analysis diagram (FAD).

Fracture Analysis Diagratn (FAD)

The FAD is one of the earliest applications of brittle fracture rules to fail-safedesigns. The results obtained from the curve are very conservative but require

The(Fig. 4.10c).

Page 43: Process Equipment

66 MATERIATS OF CONSTRUCTION

the minimum in engineering analysis. A simplified version of the diagram forlow strength steels is shown in Fig. 4.12 and indicates the types of tests requiredto construct the diagram.

Point A is obtained from the DWT and it establishes the location of the NDTtemperature with respect to yield stress. The crack arrest temperature (CAT)curve, developed by the Naval Research Laboratory is obtained by runningexplosive tests on sample plates at various temperatures and observing the crackpattem. From such tests the fracture tear elastic (FTE) point is determined at thetemperature at which the crack pattem changes from bulge and fracture to bulgeand partial fracture, as shown in Fig. 4.12. The fracture tear plastic (FTP) pointis obtained when the crack pattem changes from bulge and partial fracture tobulge and shear tears. The FTE point also locates the yield stress with respectto temperature, whereas the FTP point locates the ultimate stress.

Below point A in Fig. 4.12, fracture does not propagate regardless of thetemperatue as long as the stress is below 5-8 ksi. Between points A and I otherstress lines are drawn to correlate various stress levels. These lines are obtainedfrom the Roberson test, which consists of impact testing a specimen that is

TEMP+

" FLAT"FRACTIJRE

lft\ ItL) I"BuLGE"

&SHEARTEABS

tetL_________J

,BULGE'&

PARTIALFRACTURE

lKlMBULGE

&FRACTURE

0{DT+60"F) ( DT+120'F)

Figurc 4.12 Frocluro onolFis diogrom.

(NDT+r20'F)

-/

4.5 BRITTIT FRACTURE 67

stressed to a certain level and heated from one side to create a temperaturegradient as shown in Fig. 4.13.

Figure 4.14 shows the complete fracture analysis diagram. The range of flowsizes at various stress levels has been obtained from experiments as well as

experience. The experiments consisted of using large spheres of good impactmaterial and replacing portions of them with a notched brittle material. Thespheres were then pressurized to a given stress level at the NDT temperature ofthe brittle material. The size of the notch was varied with different stress levelsto obtain the range in the figure.

mpAcT

ERiPFigure 4.13 Diosrom of specimen urd in Roberrson crock-drrBr bsr.

YIELDsrnEss

lslzT

ll

= riloT (NI'I+3o'F) (NDT+60'F)TEMe-.-

Fisuro 4.14 Generdliz€d frocture onolysis d,osrom.

Page 44: Process Equipment

MATERIATS OF CONSTRUCTION

ln using Fig. 4-14, the following limitations must be considered:

1. It applies only to low carbon steels.

2. It is valid for thicknesses of less than 2 in. Larger thicknesses requirespecial evaluation and it has been proposed that the FTE temperature forthicknesses over 6 in. should be taken as NDT + 120"F rather thanNDT + 60'F. The FfP temperature should be NDT * 210"F instead ofNDT + 120'F. This indicates that for thick sections, Fig. 4.14 is on the

unconservative side and the safe operating temperature should be greater

than those indicated by the figure.

Example 4.2. A low-carbon steel material with NDT temperature of 15"F is

used in a pressure vessel. What is the rninimum safe operating temperature forsuch material?

Solution. Because no stress level is given, the minimum stress is assumed atyield. Entering Fig. 4.14 at yield stress, the CAT curve is intersected at the FTEpoint. Moving vertically, a temperature of NDT + 60"F is obtained. Thus, theminimum safe opemting temperature is 75'F.

If stress concentrations are assumed in the vessel and the stress level is beyondyield at some areas, then a conservative design is at the FTP point. In this case,

the safe operating temperature is NDT + 120'F, or 135'F. I

Example 4.3. A low-carbon steel vessel with an NDT temperature of -20oFis to have a start-up temperature of 0'F and a stress level of one-half yield. Isthe start-up iemperature safe?

Solution. From the CAT curve in Fig. 4. 14 the minimum safe temperature is

at NDT + 30" or 1ffF for a stress of one-half yield. Thus, start-up temperatureis on the unsafe side because it is less than 10'F. If start-up temperature iscritical, the shess will have to be decreased or a better impact material se-

lected. I4.5.1 ASME Pressure Vessel Criterio

The ASME Code, VIII, uses a different approach for preventing brittle fracturein pressure vessels with carbon steel construction. Division 1 prohibits the use

of some carbon steels below -20'F and requires impact testing of all others thatare subjected to temperatures below -20"F, with some minor exceptions. Di-vision 2 uses a more refined approach that takes into account the effect ofmaterial type, thickness, and temperature. Figure 4.15 is a simplified version ofthe code approach. It exempts some tough materials of a given thickness fromimpact testing when the service temperature is above a specific value given inthe filure.

4,5 BRITTLE FRACTURE

or11+22+3THICKNESS

GRoUP A: Nonnallzed SA-442 over 1,0 ln.orinrl ized 5A-516 And sA-662

GRoUP 8: SA-442 over 1.0 In. I'lhen l{ot Nonnallzed5A-516 Up To 1,5 In. Thick

GRoUP C: SA-442 Up To 1.0 In, Thlck

GRoUP D: All Carbon And Loll Alloy Steels Not Listed Above.

Figure,l.l5 lmpdci test exemption curvos for some corbon sreels. (Co'rrte.y of the Americon Society ofM€€honicol Ensineers.)

The above approach, although different from the FAD concept, is a practicaltool for preventing brittle fracture without requiring elaborate analysis; it isbased on test data.

The FAD and ASME criteria are applicable to low-carbon steels where theeffect of temperature is prominent. Toughness of higher strength steels or mate-rials such as stainless steels, aluminum, or titanium is independent of tem-perature. Thus, a different approach based on the mathematical theory of frac-ture toughness is used in establishing adequate toughness.

Example 4.4. A 3.O-in.-thick pressure vessel is made of SA-533 Gr. B mate-rial with an NDT temperature of 0'F. The design temperature is 50"F and thedesign membrane sffess is three-fourths of yield. What are the code fracturerequirements of this vessel if it is constructed in accordance with (a) Division Iof Section VIII, (b) Division 2 of Section VIIL

69

60

50

,4O":l 30

Cl 20

El 10

El o4l-l -1oulFt -20-30_40

-50-60

Page 45: Process Equipment

MATTRIALS Of CONSTRUCTION

Solulian. (a) Because the temperature is over -20"F, Division I does notrequire any analysis.

(b) From curveD ofFig. 4.15, the minimum temperature that exempts impactrequirements for a 3.0-in.thick vessel is 120'F. Thus a Cy test is manda-tory. I

4.5.2 Theory of Brittle Frocture

Basically the brittle fracture theory assumes that stress at the vicinity of a crack(Fig. 4. 16) due to a load applied perpendicular to the direction of crack is givenby the following expressions:

".: #(*":)('.: #(*":)('

. 0 30\-stn-stn-l'... . -... ,, I- -/,a30\-i srn; srn , ," -/

K, 1.0 0 3a\T4= ./^ | Sln; cos; cos r,vzTIT\ z z z/

where a,, o], 7ry = stress components at a point (ksi)

r, 0 = polar coordinates from tip of crack

Kt : fracine toughness factor (ksiV-in)

The fracture toughness factor K1 is a function of applied load as well as the

Figure 4.16 Elostic srres, distribulion neor rhe tip of

tft

4.5 BRITTTE TRACTURE

configuration of the body and crack. Thus K1 can be expressed by

&=oF (4.l)

where F : crack shape factor.

Unstable crack propagation occurs when the value of K1 reaches a criticalvalue K1c, which is a function of the properties of the material. Temperaturevariation could have a drastic effect on the value of K1c. as is the case with lowstrength carbon steels.

Some published K/c values are given in Table 4.7. Experimental deter-mination of the Krc factors is described in ASMT E-399 and is rather costly toestablish.

Values for the crack shape factor F are normally obtained from the theory ofelasticity. Because of the complexity of such analysis, only a few cases aresuited for practical use. Some of them are shown in Table 4.8.

Materials in general lose their toughness as the yield strength increases. Onemeasure of toughness is the ratio K16 f or. Ratios larger than I .5 indicate toughmaterials, whereas lower ratios indicate more brittle materials. A study ofK16/o,and Eq. 4.1 reveals that the defect factor F has to be very small when o" is highand K1q is low. In other words, very small defects in high strength materials canlead to catastrophic failures.

Fracture theory is one the most accurate methods presently available forevaluating maximum tolerable defect size. The main drawback is the difficulttask of obtaining I</c factors for different materials. Economics might dictate asimplified approach like FAD or the ASME criteria with a small permissibledefect size rather than a fracture theory approach that might allow a largertolerable defect.

Relatiaiship Between K1g and Cy

Determination of K1c values is tedious and expensive especially for low strength

Toble 4.7 Some Approximofe K7a Volues

JK/c (ksi\-inJ

Material - 300"F -200'F - 100"F

7l

A302-Gr. B

,A.5l7-Gr. F

A203 Gr. A norm.

A203 Gr. A Q and TA.533 Gr. B

HV-80

25

34

38

35

55

34

44

50

83

40 78

48

7'7

46

Page 46: Process Equipment

Tqble 4.8 Shope Foclors for Common Configurolions

case l: Flovl in a sheet of

Case 2:

Clse 3:

inf

l"

I n terna l ci rcul ar flow in

toItllll

Internal clrcular flow in a

F=zVT

inlte vrldth.

a sheet of finite wi dth

r l1'2F=Fr.L# tan @wl

thick pl ate.

F=V ra

( Ref. 2, p. 49 )

( Ref. 2, P

3, P. 39 )

o s0 )

( Ref.where "a" is radlus'of crack

73

Tqble 4.8 Shope Foctors for Comrnon Configurolions (Coniinued)

and oy ls yleld

Case 4: Internal elliptic flow jn a thlck plate

3t . If .a2E-'g_ E_

nor axi s and "

notcn.

axl sl,ihere

La se 5

u2a' is

: Singlo

the ni

e edge

II

6 E- ( Rer'

is and "2c" is the maior

F=CVir.a

c=1i1'iF+o227+ roa(i)'-zasz(if

+4272/ \4t+l\r /

( XET 328 )

case 6: Elliptlcal surface flow.

F=

where "2c" is cra

materlal stress,

ck length' "a" is crack depth, o lsstress. ( Ref.

actual

31 5 )

- o.ztzo2f or2

Page 47: Process Equipment

74 MATERIALS OF CONSTRUCTION

steels. Various methods relating the,K/c factor to the relatively inexpensive Cytest have been suggested. One empirical method proposed by Rolfer and Barsomconsisted of preparing two equations for correlation purposes. One equationrelates the Cy and K1s values at the transition temperature region, whereas theother equation is applicable at the upper shelf region. Thus, for the hansitionregion,6

Krc:155Cvtl2

whereas for the upper shelf range,

(4.2)

(4.3)

where Cv is in ft-lb, o" in ksi, and K1g in ksivG. Equations 4.2 and 4.3 are formedium strength steels such as 4.517 Gr. F and 4302 Gr. B.

4.5.3 Hydroslotic Testing

Hydrostatic testing of a pressure vessel is the best available method for deter-mining maximum tolerable defect size. Thus, if a thick pressure vessel ishydrotested at a pressure that is 50% greater than the design pressure, the criticalK1 is given by Eq. 4.1 as

K1g = oF

Assuming an intemal defect represented by case 3 of Table 4.8, the maximumK16 immediately after hydrotesting is

/ I;\Krc: t.5 r.(r\/;J

Maximum defect size r at the design pressure is given by

: "

(,

or

- - t t<^

Hence, a crack that is discovered after hydrotesting can grow 2.25 times itsoriginal size before causing failure. This fact illustrates the importance ofhydro-testing and is based on a hydrostatic temperature that is the same as the lowestoperating temperature of the vessel.

f&Y:4ofQ-o.r)\ov./ \sr /

"',('fu) -l1f/

4.5 BRITTTE FRACTURE

4.5.4 Foctors lnfluencing Britlle Froclure

Many factors such as torch cutting, arc strikes, and cold forming affect the britdefracture behavior of metals and should be considered in fabricating pressurevessels. Torch cutting or beveling of the plate edges may lead to hard and brittleareas. In cases where this condition is underdesirable the plate should be heatedto minimize this effect. Grinding the edges eliminates the hard surfaces.

Arc strikes can create failure by brittle fracture especially if the strike is madeover a repaired area. It is desirable to grind and repair all arc strikes beforehydrotesting, especially at low temperatures.

Cold forming of thick plates may lead to fracture in areas with stress raisersor plate scratches. All stress raisers should be ground off to minimize theireffect. Hot-forming substantially improves the situation because it increases theNDT temperature and thus prevents brittle fracture.

Example 4.5, A titanium pipe (ASTM 8265 Gr. 5) with a 2.375-in. outerdiameter and a 0.154-in. wall thickness has an actual stress of 30 ksi. a vieldstress of 120 ksi, and K1q : 40 ksiVin at a given temperature. The pipecontains a flow of depth 0.05 in. and length 0.25 in., which is similar to case6 of Table 4.8. What is the maximum internal pressure the pipe can hold?

Solutian. From a conventional strength of material analysis, the pressurerequired to yield the pipe is given by Fig. 5.4 as

75

Using fracture toughness approach, maximum stress is

KrcF

From case 6 in Table 4.8,

1.12\4;Xo.o5)

^ a\Rl - Rl) 120(1.88'z - 1.034':)' Rl - Ri r.88r - r.034,

= 0.359

Hence, o : 40/0.359 - 111.4 ksi

^ tll.4(t.88)2- t.0341maxr: ll8' r l034': : 14Jl(sl

'l'hcrclirre liacture toughness criteria control the design. I

Page 48: Process Equipment

NONMETATTIC VESSEIS

Hydrogen ,orliol pretlu?c, P.r. i

Fisure 4.17 (Courtesy of the Americon Pelroleum lBrirute.)

4.7 iIONMETALLIC VESSETS

Rules for fiberglass-reinforced plastic (FRP) pressure vessels are covered in

Section X of the ASME pressure vessel code. Construction of FPR vessels is

divided into four classes: the contact molding, bag molding, centrifugal casting,

77

76 MATERIAIS OF CONSTRUCTION

Examnle 4'6. An A302-B material with a yield stress of 50 ksi is to be used

irl ".!*"* "".r"1. The Cv value is 15 ftlb and an examination of the percent

#"i^il;; .rott ...,i* of tested specimens indicate a temperature in the

transition range. Ultrasomc examination of the plarc uncovered an elliptical

il;;;;d. fit" surface that is 0.375 in long and 0 25 in deep How safe is

the vessel if the operating stress is I yield?

Solution. From Eq 4'2' K1g = 15(15)0 5 = t9 ksiVin-

From Table 4.8, case 4,

\/;ajzrF = ;ts+l;ts,,oI25/orus" - "-"

Hence, from Eq' 4'1, o-: 19/0'46: 41 ksi Actual stress : 'l

x So = r:i.fl*fit"rt it l_es's,rtan the critical brittle stress Therefore' operation of the vessel

is safe unless the defect grows in size l

4.6 HYDROGENEMBRITTLEMENT

Essentially, the two different methods by which hydrogen can embrittle steels

are:

l. Hydrogen decarburization' In this case hydrogen penetrates the steel

and combines with the carbides in the structure (Fig' 4 8) to form meth-

ane gas. This gas accumulates in the space of the original carbide and

;;il;t ;p p;";t" that leads to cracking' This process normally acceler-

ates with an increase rn temperature ind in operating -pressure'

One

method of minimizing hydrogen attack is by using Cr-Mo steels' Here

the carbides are in solution wiih ttre cr or Mo and do not readily combine

*ittt th" hyd.og"n. The type of steel to be used in a giv€n combination

of te-perutu."hd p,"ttot" it normally determined by the Nelson chart

in Fig. 4.17.

2. Hydrogen attock. Researchers have observed that hydrogen attacks-'

"Jatuin"r"gions of a pressure vessel at temperatures below 200'F when

they have-high hardniss zones in the range o1200 Brinelland higher' The

exact mechanism is not known exactly, but it is believed that the hydro-

een is attracted to hard regions with higher stressed zones. Accordingly,

;;;;;;;q-t" soft h;-affected zones with a Brinell hardness below

200 to avoid hydrogen attacks at low temperatures'

1C;-Yr Mo Stccl

Page 49: Process Equipment

MATERIATS OF CONSTRUCTION

and fi lament-winding Processes.In the contact-mol,cling process reinforcements and resins are placed in a cast

mold and cured at room temperature. Vessels constructed by this process are

limited to a design pressure of 150 psi.

In the bag-molding process a pressurized bag is used to compress Prerolled

fiberglass "!hnd".t

and heads preforms against an outer heated mold The

uessels conjtructed by this process are also limited to 150 psi pressure'

In the centrifugal casting process, the cylindrical sections are formed from

chopped fiberglasi strands and a resin system in a mandrel, which is spun to

oroduce a suitible laminate and heated to cure the resin system Pressure vessels

constructed by this method are also limited to 150 psi design pressure'

In the filamenrwinding process, filaments of glass and resin are wound in a

systematic manner to form various components. The ASME code limits the

pressure range to 1500 psi for filament-wound vessels with cut filaments and to

i000 psi for filament-wound vessels with uncut filaments'

FRi' vessels normally operate at low temperatres. The ASME Code, Section

X, limits the temperature iange between a minimum of -65oF and a maximum

of 150'F. Also, because the modulus of elasticity is about 1 x 103 ksi, special

care must be exercised in designing various components Because of this and

because different fabrication processes produce different strength vessels, the

ASME Code states that in order for a given vessel to be adequate, a prototype

must be cycled 100,000 times between zero and design pressure and then burst

at a Dressure not less than six times the design pressure'

REFERENCES

Pellini, W. S., "Principles of Fracture Safe Design-Part l" ln Pressure Vessels and Piping:

Design and A'',,lysis, Vol. l, American Society of Mechanical Engineers' New York' 1972

Tetelman. A. S., and A. J. McEvily, Jr' Fracture of Structural Materidlt, John Wiley '

New

York, 1967.

Rolfe. S. T., and J. M Ba$om F/(r cture anal Fatig e Control in Structures' Prentice-Hall'

Englewood Cliffs, N.J., 1977.

Riccardella, P. C., and T. R. Mager, "Farigue Crack Growth in hessunzed Water Reactor

Vessels" in Pressare ye ssels and Piping: Disigtl and Analysis, Vol l, American Society of

Mechanical Engineers, New York, 1972.

Wessel, E. T., andT. R Magel, "Fracture Mechanics Technology as Applied toThick-Walled

ttu"t"- pa".*," Vessels" in Pressure vessels and PipitlS: DesiSn and Analysis' vol l'American Society of Mechanical Engineers' New York, 1972

Roberts, R., and C Newton, "lnterpretive Repoft on Small-Scale-Test Conelations with f''DaA," Welling Rcs\rch Council' Bulletin 265, New York' | 981'

BIBTIOGRAPHY

BIBLIOGRAPHY

Aluminum Standards aM Data, Alrmin'um Association, Washington, D.C., 19'19.

Alner, S. H.,Introduction to Phlsical Metallurgy, McGraw-Hill, New York, 1964.

Nichols, R. W -, Pressule Vessel Engineering TechnologJ, Applied Science Publisherc, England,t91l .

Thielsch, H., Defects and Failures in Pressure Vessels akd PipinS, R. E. Krieger, New York,1965.

Page 50: Process Equipment

PART2ANALYSIS OF

COMPONENTS

8l

Page 51: Process Equipment

CHAPTER 5STRESS IN CYLINDRICAL

SHELLS

Atr'0|t|h,t|.otcy|lndr|co|lh!|hinochomicolP|on|'(cour|g,yofE.|.dUPontdaNomoursondco.)

83

Page 52: Process Equipment

11

where p = g€ssure

Z = length of cylinder

o, = hoop stress

r = radius

I = thickness

The stain ee is defined as

and from Fig. 5.2,

PL.2r:ZoeLt

final length - original lengthoriginal length

2t(rIw)-2rr€0=

---;-z1fr

3TR!IS IN CYTINDRICAI gHErrS

(s.1)

(s.2)

5.I STRESS DUE TO INTERNAL PRESSURE

Thc classic equation for determining stress in a thin cylindrical shell subjectedto pressur€-is obtained from Fig. 5.1. Summation of forces perpendicular toplane ABCD gives

Prot= T

w

Flgor.5.l Fr€c-body diogrom ol d rylindricol $ell lubi.ctod to intarnol prerlure.

3,I STRI3E DUE TO INTTRNAT PRESSURE

Figur€ 5,2

Also,

where

the.radj4 deflection of a cylindncal shell subjected to internal pressure isobtained by subsdrudng rhe quantity e6: osf E in6 Eq. 5.i. ilnce for thincvllnoers

85

dwar (s.3)

(s.4)

E = modulus of elasticity

Equations 5.1 and 5.4 give accurate results when r/r > 10. As r// decreases,however, a more accurate expression is needed because the stress distributionthrough the thickness is not uniform. Recourse is then made to the,.thick shell,,theory' first developed by Lame. The derived equations are based on the forcesand stresses shown in Fig. 5.3. The theory assumes that all shearing stresses arezero due to symmetry and thal a plane section that is normal to thjongitudinalaxls

-betore pressure is applied remains plane after pressurization. In other

words, e1 is constant at any cross section.

_. A relationship between oi and_o1 can be obtained by taking a free_body

diagram of ring dr as shown in Fig. 5.30. Summing ior"", ii the verticaldirection and neglecting higher-order tdrms, we then h-ave

ae- o,

A second relationship is obtained from Eqs. 3.2, which is written as

= do,dr

\. o,II(l + rr)(1 - 2*rl+(t - 1t) + p,(e, + e)l

(5.5)

Page 53: Process Equipment

86

(l + p)(1

E

[er(l-p)+pr(e,+e)] (s.6)

(1 +pXl- .r.^ [€r(l - ;r) + g.(e, + e)l

Substituting Eqs. 5.2 and 5.3 into the first two expressionssubstituting the result into Eq. 5.5 results in

dzw ldw w ---'-t -r - --- - -- = var rar r-

A solution of this equation is

of Eq. 5.6

(s.7)

whcre A and B are constants of integration and are determined by first substi-tuting Eq. 5.7 into the first one of Eq. 5.6 and then applying the boundaryconditkrns

o,: -Pi at r = ri

rnd

o!

la'Fisuro 5.3 Cro5s i€.rion of

tb)o tfiick cylindricol :hell.

and

.B

o, = _p,

ljxorrulon 5.7 then becomes With or known, Eq. 5.8 for the deflection of a cylinder can be expressed as

5.I STRESS DUE TO INTERNAT PRISSURE 87

w = -t .€1 . *n--t=Alr'(t - t, - ztt\(Er? - p,r|) + r?r1{o + D(n - p")l (5.8)

Once w is obtained, the values of o6 and d; are determined from Eqs. 5.2, and5.3, and 5.6 and expressed for thick cylinders as

_ _ pr? - p,r? + (pt - p")(r7r3/r2)aa =

----- 4:i- (5.9)

4rZ - nrl + (n - n)blrl/rz),-" - ,l

where o; = radial stress

od : hoop stress

p, = intemal pressure

p, : extemal pressure

4 : inside radius

r, = outside radius

r = radius at any point

The distribution given by Eq. 5.9 of the shesses through the thickness of acylinder due to iniernal and extemal pressues is shown in Figs. 5.4 and 5.5,respectively.

A comparison between Eqs. 5.1 and 5.9 is shown in Fig. 5.6. The figureillustrates the adequacy of Eq. 5. I for r,/4 ratios of less than or equal to 1.1 (or,conversely, rt/t > lO).

The longitudinal stress in a thick cylinder is obtained by substituting Eqs. 5.2,5.3, and 5.8 into tle last expression of Eqs. 5.6 to give

oI= EeI+2p(\? - !"31r;- ri

This equation indicates that o1 is constant throughout a cross section because €r

is constant and r does not appear in the second term. Thus, from Fig. 5.7 theexpression ot can be obtained ftom statics as

(5.10)4r? - P"r'z.

,2_.?

Page 54: Process Equipment

6=tr,..t!id- )- f;-Ji \ J' I

"'=-++r(#)

Ar Inne. surr.ce +=t+)=-t

.Ai Ourer surraco +="#

ft=oFigurc 5.4 Slrca! dishibdion in o rfiick cytirder du. to inrornol prcrlur€.

,,=#e#)

At fnnersurtace "r=ffift=o

aroorersurfaca "r-#ifl9=_r.oP"-

Figuro 5,5 Str€ls dithibt ion in o thick cylin&r due l,o enornol pr.3sur€.

88

Fi9ur6 5.6 Comporison ot tornulor for hoop sire33 in o cylindricol 5hcll.

Page 55: Process Equipment

90 STRESS tN CYr"tNDRtCAt SHtrrs

l(Ptri - P,,r!,)lt - zr.t) + (h - t',,)rlrl,(l + rt)

-

Lr\r; - ri)(5. 1 1)

The deflection pattem for external and intemal pressures is shown in Fig. 5.8.

Example 5.1. The inside radius of a hydraulic cylinder is 12.0 in. What is therequired thickness if P : 7500 psi and a6 = 20,000 psi?

Solulinn. From membrane Eq. 5.1

Pr 7500 x 12t=-: oo 20,000

= 4.50 in.

lnternal Pressur€

*=!"il+##tdl

Max.!t At Inner Surlace

w.=E:tfl2:lll'E(ro"-r;")

*=-& . t 'tr'(r - zr) * r,"(r *,., )Ie.r (r;- r,')

Max.q At Inner Surrace w,=-B:dJiJ2:t)EGTil

External Pressure

Figure 5.8 Rodiol deflftrion du€ lo inlernol ond exrernol prelsore.

ot _rl+ r?

P rl- r!

5.I STRESS DUE TO INTTRNAI PRESSURT

From Lame's equation (see Fig. 5.4)

: 5.80 in.

Hence, the error of using Eq. 5.1 in this case is 22Eo. I

Example 5.2. A cylinder has an inside radius of 72.0 in. and an internal

pressure of 50 psi . What is the required thickness if the allowable stress is 1 5 ,000psi, 1.r

: 0.3, and E = 30 x 10o Psi?

Solution. From membrane Eq. 5.1,

50x72 : 0.24 rn.

9l

15,000

From Eq. 5.4,

50 x 722 : 0.0360 in.30x106x0.24

Using the thick shell theory, we obtain the required thickness from Fig. 5.4 as

'): O.24 in.

and from Fig. 5.8,

(5q?2f | 2-0.3 \' : 30 x rgu \tf* - rV1

= 0.0305 in.

Examples 5.1 and 5.2 indicate that Eq. 5.1

sreater than 10. I

loe + p, = /l "\ / --------= -

is adequate when the ratio rlft is

Page 56: Process Equipment

3TRI3S IN CYIINDRICAI SHETIS

Problcms

5,1 A cylinder with an inside diameter of 24 in. is subjected to an intemalpressure of 10,000 psi. Using an allowable stress of 25,000 psi, determinethe required thickness.

Answer: t:6.33 in.

5.2 A cylinder has an inside diameter of 12 in. and an outside diameter of 18

in. Determine the maximum intemal pressure that can be applied if themaxirnum allowable stress is 20.000 psi.

Answer: p1 = 7690 psi

5.3 A cylinder is subjected to an external pressure of 5000 psi and an internalpressure of 2000 psi. If 11 = 15 in. and rz = 19 in., what is the maximumcircumferential, longitudinal, and radial stresses? At what location do theyoccur?

Answer: o6: -17,900 psi at inner surface

o, = -5000 psi at outside surface

at = -9960 psi uniform tkough thickness

5.2 DISCONTINUITY ANALYSIS

All the previous equations were based on the assumption that the cylinder is freeto deform under pressure. In practical applications, the cylinder is attached toend closures that reshain its deformation. Other items such as stiffenirg ringsand internal bulkheads affect the cylinder deformation and introduce localstesses. These local shesses can be evaluated by a dicontinuity-type analysisusing the general bending theory of thin cylindrical shells. The theory assumesthat the loads are symmetric around the circumference and that the thickness ofthe shell is small compared with its radius. It is also assumed that the in-planeshearing forces and moments are zero. The problem then reduces to that ofsolving the forces shown in Fig. 5.9. The relationship between these forces canbe obtained from statics. Hence, from Fig. 5.9,

>4:0

ff*,ar=o

5.2 OISCONTINUITYANAIYSIS

l{o dx

(b)

Figore 5.9

which indicates that N, must be a constant.

Let

N,:0

Also,

>4=0

93

dx

+ 4!!.|i ax

dox dx-?t

d?'+at=rdxr

Similarly,

2M,=o

(s.12)

Page 57: Process Equipment

94

or

3TRE5S IN CYIINDRICAT SHETIS

(s.l3)

(5.14)

*-a.=oax

Deleting Q, from F4s. 5.12 and 5.13 gives

N, d2M,

- + ---:--l : rr ta-

This equation has two unknowns, N6 and M,' Both unknowns can be expressed

in t".-, of,h" O"flection w. The relationship between M' and w is given by Eq'

3.1I as

D, Et'= rro=E (s'15)

Because the rate of change of deflection in the a-direction is zero due to

symmetry, the above two equations reduce to

".= -r(**)(s. 16)

Mo=

and

Me = FM, (s.17)

'l'hc cxprcssion for No is derived from the axial and hoop strains' In refening to

liil, 5.9, thc uxitl strain is given by

",: -r(r,tt. - *t")

duax

-'(#..?)

",: _*(#)

5.2 DISCONTINUITYANAIYSIS

and the hoop strain as

wee= -i

Substituting expressions 5.18a and 5.18b into Eq. 3.11 gives

95

Substituting Eqs. 5.16 and 5.19 into Eq. 5.14 yields

Also,

y,=.Et ;1r,r p,e6)=ot' - lt-

EtNs:7 ,\es+ Pe)r-p-

u4*r(*\:-,r' \dx+ /

du /w\=

: lLl- |dx \r/

(5.18b)

(5.19)

(s.20)

Defining

".ilno: Lt -Jlt

- lL-)4r2D r2t2

the differential equation becomes

(5.21)

)(5.l8a)

where p is a function of .r.

ffi*oon*=-+

Page 58: Process Equipment

96 tTRlSt tN CYUNDRTCAT SHlrtg

5.2.1 Long Cyllndorr

One of the most practical applications of Bq. 5.21 is for long cylinders subjectedio end shears and moments as shown in Fig. 5.10. The force and deformationdistribution at any point r along the cylinder due to O0 and M0 can be obtainedfrom Eq. 5.21 with P = 0. Hence,

aw;i+4p.w:o

A solution of this equation can be expressed as

' '"- = ::lg l -:1. **!.gz;it -

p*t + - y-tc-'-e$ €L-L. 9r-t* -ff)- _J-.gD

By observation we can conclude that the deffection due to @6 and Me approacheszero as .r aplnoaches infinity. Thus the constants C1 and C2 must be set to zeroand the solution becomes

The constants C: and Ct can be evaluated from the boundary conditions

(s.22)

M..=o=

Mo= -'e;1.="

;i = e-tu(q cos B, a Ca sin

Figur.5.l0

5,2 DISCONTINUIIY ANAIYSIS

and

Hence,

a.l._,= n"= -,(#)1."

.'.'*-"".--",^ _ -lct=;;7i(Qo + BmsliLP tl

;

'Ms\ a=,L*--- ?E:p" - '"" l

Equation 5.22 then becomes

w = ]6rl?tvtobin Bx - cos F.r) - O cos Fx].

By defining

{* = e-e(cos Br + sin Br)

!* = e-&(cos Br - sin pr)

Cs = s-$t "o"

PDs = e-tu

"in Pthe deflection and its derivatives can be expressed as

, :;fu<oro"* + escp)

#= *1roU""ctu+ S.AP)

t:=$aor"os+zeoD,,)

# = jour,De'- enBB,)

Values of Ap,, BB,, CB,, ar]d Dg, are given in Table 5.1.

Using the terminology of Eqs . 5 .23 and 5 .24 , the expressions for M,are represented by

i7

(s.23)

(s.24)

arfi Q,

Page 59: Process Equipment

98 sTRtss tN CYUNDRtCAt SHEttS

Tqblr 5.f Vqfurr of functiqng Ap* Bp- Cp. Dp,

Cp" DB,Bu,B,

00.05

0.10

0.15

0.20

0.30

0.40

0.50

0.55

0.60

0.80

l_00

1.20

1.40

1.60

1.80

2.00

2.50

3.00

3.5

4.05.06.0't.o

1.0000

0.99760.9907

0.9'19'7

0.9651

0.926'7

0.8784

0.8231

0.79340.76280.6354

0.5083

0.3899

0.2849

0.1959

0.12340.0667

-0.0166-0.0423-0.0389-0.0258-0.0045

0.0017

0.0013

1.0000

o.9025

0.8100

0.7224

0.6398

0.4888

0.3564

o.24150.1903

0.1431

-0.0093-0.1108-0. 1716

-0.201l-o.2077-0.1985-0.r794-0.1149-0.0563-o.0177

0.0019

0.0084

0.0031

0.0001

1.0000

0.9500

0.9003

0.8510

0.80240.707'7

0.61740.5323

o.49190.4530

0.3131

0.1988

0.1091

0.0419

-0.0059-0.0376-0.0563-0.0658-0.0493-0.0283-0.0120

0.0019

0.00240.0007

0.0000

0.0475

0.0903

0.1286

o.1627

0.2189

0.2610

0.2908

0.3016

0.3099

o.3223

0.3096

0.2807

0.24300.2018

0.1610

0.1231

0.0491

0.0070

-0.0106-0.0139-0.0065-0.0007

0.0006

M"=(5.25)

Q,=QBMnDy-QoB*)

The relationship between M,, M" Q, N, w, and d for various boundary condi-tions is shown in Table 5.2.

Exarnple 5.3. A long cylindrical shell is subjected to end moment M0. Plot thevalue of M, from F, : 0 to p, : 4.0. Also, determine the distance .r at whichthc moment is abort 7Vo of the original applied moment M0.

Solution. From Eq. 5.25, M,: MoAs.The values of Ak are obtained from Table 5. 1 and a plot of M, is shown in

_r(+\\ax- / =

fi<zou,ea + 2eoDB,)

5,2 DISCONTINUITYANATYSIS 99

Toble 5.2 Vqrious Disconlinuity Funclions

e

t4^

Ne

qo

- ilo,F;tlo---F

-2 oB2.t

0

Qq

2 B3A

2Bz,D

0

26. r. Qo

Qo

0

zB2.o.to

E.t.Ao

46 3. 0, A0

0

0

28. D. eo

0

282 .D.e o

0

Ne

Qx

-llo 8o",F.o ""

t4o C^E;r'- b"

zlioB2.r.Br,

-26. tito , DBx

0o C-

28'D

-0oiPo ^p,

q9 . D-B FX

28. r. Qo. CBx

Q6. Bgx

Ao(2Cax-8Bx)

z8do ( ABx - cBr)

zB2.o,t4lrr -cr,

!1. ao ( 2ce " -8."

4B3D,aJ B6x- DBx)

? ttu'-tu''

eo {ABr( - 2CBx)

?$ D'ed DB, -aB")

:.t.00(c^ -8" )F-3- p'

tB2. D. oo ( 2DBr+B B)(

'clockwise moments and lotation arcpositive at point 0. Me = tir|..

positive at point 0. Outward forces and deflections arc

Fig. 5.11. From Table 5.1are about 2.00.

or

the values of Bx at which M, is equal to 7Vo of Mp

Bx = 2.00

and

.r: 1.56\G

The significance of the quantity 1.56Vr . l is apparent from Fig. 5. I 1. It

2

e

(l)

shows

Page 60: Process Equipment

r00 3TR!35 lN CYllNORlCAL Sl{llts

that 0 momcnt epplicd at thc cnd dissipatewery rapidly and reduces as much as

94% ofthe original momcnt atr = l.56Vrt. This indicates that any other forceapplied ot that distance x can be analyzed without regard to the applied momentMo' IExample 5.4. A long cylinder is subjected to end shear ps. Plot the value ofM, as a function of C0 from Fx : 0 to Fx = 4.0 and derive the location of themaximum value of M,.

Solutinn, From Eq. 5.25,

,'=*o^Referring to Table 5. 1 for values of D p,, a plot of M,/ (Qo/B) can be constructedas shown in Fis. 5.11.

q'ry

Figura 5.1I

and

(l) I

5.2 DISCONTINUITYANATYSIS 't0l

To find the maximum moment M,, the above equation can be differentiatedwith respect to r and equated to zero. Hence,

*, = 3.e-& sinA

ff = o = ftr-Ou* sin Bx * Be-tu cos Bx)

and maximum moment is given by

, _ o.34Qo

PrEtlw\==:- "lexr lr-lz r-F-\ r/

pr=,E' ,(Y* ur,\r - rr'\r /

and

Solving for e, and w gives

I

Example 5.5. Determine the expression for the deflection of a long cylinderwith end closures due to intemal pressure p.

Solutinn. For intemal pressrre p, the axial force it 7'1, = pr/Z and the hoopforce is Ne = pr. Also from Eqs. 3.11 and 5.18,

Pr (l - 2tt)''Et2

'#('- t)

Page 61: Process Equipment

t02 STNESS IN CYTINDRICAT SHELTS

trlxomple 5.6. A still'cning ring is pllced anrund u cylinder at a distance

rcmoved from the ends us shown in Fig. 5. 12. The cylinder has a radius of 50.0in., a thickness of 0.25 in., and is subjected to an intemal pressure of 100 psi.

Assuming E : 30 x 106 psi and & = 0.3, find

(a) The discontinuity stress in the shell with the ring assumed to haveinfinite rigidity .

(b) The discontinuity stress in the shell and ring if the ring has a thicknessof 0.375 in. and a depth of 4.0 in.

Solution.

(a) A free-body diagram of the shell-to-ring junction is shown in Fig. 5.13.Because the ring is assumed to have infinite rigidity, the deflection due topressure must be brought back to zero by a force pq. Also, because the slope atthe shell-to-ring junction is zero (due to symmetry), a moment M0 must beapplied at the junction to reduce the slope created by force Qs to zero . From Fig .

5. 13,

deflection due to P - deflection due to Qe * deflection due to Mo = g

The deflection due to P is obtained from Eq. I in Example 5.5, whereas thedeflections due to M0 and Qs are obtained from Eq. 5.24. Hence

tl(r-E\ -4 +!!=:oE.r \' 21 2B3D zB'D

4" x 3/8" ri ng

tigure 5.12 Me = 96.4 in.-lb/in.

5.2 DISCONTINUITYANATYSIS-+rrtr" I

oo {odo

r03

Figuro 5.13 Sign conv6ntion oi poini 0, clockwiss 0 ond i4" ore + , outword w dnd Q. oro -

From Eq. 5.15,

D = 0.00143 E

and from Eq. 5.20,

B=03636

Hence the deflection compatibility equation becomes

Mo- 2'75OQo= -321'39

The second compatibility equation gives

(1)

rotation due to O0 - rotation due to Me = 0

Qo-ZBUo:g e)

Solving Eqs. I and 2 gives

Mo : 321'4 in.Jb/in'

The maximum longitudinal stress is given by

.=N.ry= 40,900 psi

The maximum hoop moment is given by Eq. 5.17 as

Page 62: Process Equipment

-, Etw"r

But because w = 0, N6 is equal to zero and the maximum hooP stress is

*:T*,",

O) The shell deformations are expressed as follows:Due to R

, - p,-'- -1-',

", - ='#l'- i)

{

L'=o *-*-- I

?Y'oo'

l0.l

Tho hoop force Nc is glvcn by Eq. 5.19 as

Due to Mo,

tTRttt tN cruNDRrcat sHttls

Mn

':t9o-Mo

@

The ring deformations are expressed as follows:Due to p,

pr(r + d/2\n=- dE

0=0

Solving Eqs. 3 and 4 yields

!.2 DISCONTINUITY AI,IATYSIE

Due to 00,

Due to Mo,

The deflection comPatibilitY is

2Qor(r + 2)

'= - bdE

0=0

w=0d=0

t0t

(3)

and

(4)

Mo = 152'0 in-lb/in.

Oo : 110.6 lb/in.

wp - wQo* ,*]"' - ,o + *roof^"

,i( - t) - #. #=,*#!".'3e#2

Mo - 4.0@o: -296'8

Sirnilarly,

f0, + ilao- 9al"t. = lflp + ilMo - 0oJn*

2BMs-20=g

Page 63: Process Equipment

pr , 2QorO,: -- r ---:---

aDa

= 1250 + 7370

= 8620 psi

Maximum longitudinal stress in cylinder is

Pr . 6MnO'= - - ---A-zt I-

_ 100x50 x6x t5?2 x 0.25 (0.25).

: 24,600 psi

t06

lloop stress in ring is

Hoop force at discontinuity is

where

and hoop stress at discontinuitv is

STRESS tN CYUNDRTCAT. SHfttS

w=lt,p-wgo*wyo

=P"(,-E\- Q, * uoE \' 21 2B3D 2B2D

_ M7,500E

.. E (0.25)(447 ,sOO / E)

'", = -- 50

= 2238 lb/in.

No . 6Meoe=----1----r-T T-

2238 , 6(0.3 x rsz)0.25 0.252

= 13,300 psi

5.2 DISCONTINUITYANATYsIS

whereas away tiom discontinuity

Proe:::20'000Psi

Problams

5.4 A long cylindrical shell is welded at one end to a rigid bulkhead such thatthe deflection and rotation due to applied pressure are zero. If r = 36 in.,I = 0.5 in., p : 240 psi. lt: 0.3, and E = 29 x 10" psi, what is themaximum lonsitudinal stress?

. Pr 3PrAnswet: a= n'T -:E-zt tv3\t _ p2)

: 40,015 psi

The shell in Problem 5.4 is welded to a thin bulkhead such that only the

deflection is zero due to applied pressure. What is the maximumdiscontinuity stress?

. Pr 0.966PrAnsweri o= z *;'Fyt - u31

= 18,740 psi

5.2.2 Short Cylinders

It was shown in Eq. 1 of Example 5.3 that the applied edge forces in a long

cylinder dissipate to a small value within a distance of l.56Vrr. This basic

behavior enables the designer to discard the interaction between applied loads

when they are far apart. As the cylinder gets shorter, the assumption of long

cylinders does not apply and constants C1 and C2 in Eq. 5.8 must be considered.

Consequently, Eqs. 5.23 and 5.24 have to be modified to include the effect ofall four constants. Equation 5.8 may be rewritten in a different form as

w = Ar sin Bx sinh Bx * 42 sin Pt cosh Bx

*A3 cos Bx sinh pt + A4 cos Br cosh B-r 6.26)

and a solution obtained for various boundary conditions.The most ftequent application of this solution is in the case of edge forces and

deformations as shown in Table 5.3. Many practical problems can be solved

with the aid of Table 5.3 by itself or in conjunction with Table 5.2

t07

f,.f,

Page 64: Process Equipment

o!

=I0

o

o

c

3

(t

-9.oqF

=

t ----TI ,rlt_,Y

"--l

108

5,Tlris -:-

dld,-------, --

Jr ulu v:{vdle | ++F:E $16 T

-i=._, : d<'Fi €1. s

'=-

's":ss)sdl6 dl6 dl6 dl6 -:-| + + | u'16ys:gvrdl6 sl6 dl6 dl6 ;s| + | | dl6:ss)9;S+

dlu dlu d'lu dlu s,, L--;-,!t,:

-l-F.ils ' P '"'",o,l$ l-l$ dl.q R d

r-li- r"-rS r--=-'1 | .-=-t>-r-rS+s I s 6le --i -dlu if | + -Hlu-+9lri>-s-s "i rJlr.r 51s I

dl.: s | | ."T..t l-. tTlri :g r---'J,v ' v,

=;+ dt6, E ssls slS-E- h t

:s,-----..-- dl6UIU :9r $16

5ddld +

t>.:s,1,+<'< (a,

S .--- .ir ,:--:- --r d|U } - ":"f- f-"i-clo *dl6<ilr-, * r f, -i-.ir .. s tilrir s ",- dlu +>' s '-i- dl6 +riltiril6 * + f,i -i- ..i.. >- dld

;' )J L-J (JlU €>,' _ ,u ru,

s >" --.: dlu -dlddlu F f SEc:i R $l* i€lcq

".A.E.E66aak k,al ,5

l+rid.d.&&d.d{de.eAP)'eAAes.d.&6.{&ds.iiifriEEEE5r!666altltllllllllllll5ss>":lss:s

ca ac,

aaca cc- + |

.= .E aa cq

,,99ail I = a€€€€.'€'da6daaltlillllllll.: .l ,i .1 ,1 rt

1.2 otscot{TtNutTY ANALYS|S t09

Example 5.7. Derive Np for the case of applied bending moment M6 at edger = 0 for a short cylinder of length l.

Solution: The four boundary conditions are:At.r:0

_,(*\ =,"\ax-,/

atx: I

_,(*\:o\ax'/

From Eq. 5.26, the second derivative is given by

jj : Z|tte, cos Bx cosh Bx * 42 cos p"r sinh Bx - A3 sin pr cosh pr

-,(*\ = o\dx' /

-,(*\: o\ax- /

- Aa sin Bx sinh pr)

whereas the third derivative is expressed as

,1J u,# = Z!3lAr(cos px sinh pr - sin pt cosh Bx)

+ A2(cos Bx cosh Bx -sin pr sinh pr)

- A(sin pr sinh pr + cos pt cosh pr)

. - .A+(sin pr cosh Bx * cos F-r sinh pv)l

Substituting Eq. I into the first boundary condition gives

. _M^q, :

2D B,

Substituting Eq. 2 into the second boundary condition gives

Az: Atand from the third and fourth boundary conditions the relationships

(l)

(2)

Page 65: Process Equipment

il0

and

3TRT33 IN CYIINDRICAI 9HEITS

Mo lsin Pl cos Pl + sinhB/coshB/= Dtr \--GF7t:;tnT--

N, : Et*r

Ft= 1(Ar sin ft sinh ft * Az sin Fx cosh Fr

A3

are obtained.From Eq. 5.19,

Using the values of A1, A2, A3, Aa obtained above and the terminology of Table

5.3, Eq. 3 reduces to

c, t'r f C"N, = "' ;i*; | -sin pr sinh p1 + ::1sin Bx cosh Bx + cos Pv sinh Fx)r U)15'| Lt

C,- frcos Fx cosh Pr I

or

n, = ZrMoF'( -v, * !v, - !v,\ r\ ct Lt ,/

Example 5.8. Determine the maximum shess at point A of the thin cylinderin Fig. 5.lzla. I*t p' = 9.3.

Solution. A free-body diagram of junction a is shown in Fig. 5.140. The

deflection at point A in the thick cylinder due to P is obtained from Table 5.3

by letting Br equal to Bl. Hence,

-r lgtu _ Qu. - Qu\*o: ifrEV-,"' - c,u c,"u)

For B' = 0.7421, Dt = 0.01145 E, znd Bx = Bl' theobtained:

+ A3 cos Br sinh Bx + A+ cos Fr cosh Fr) (3)

following terms are

-M" / sin2 61 + sinh'? B/e^ = zaB, \.l"[tB, -]t"t}

I.2 DISCONTINUITY ANAI.YSIS

or from Tables 5.2 and 5.3 with r : 0,

"r I

l_* ,,t-

w: toolrn

The deflection compatibility equation at point A is

ltl

(

(b)

Figure 5.1,1

Cr = O.2028 Cz = 1.1164

Ct = 1.5444 Cr : 0.5481

C5 = 0.4568 Ce = 0.6596

U=o.272r yl=0.4006

Vq = 1.4984 V: 0 8707

%=0.5986 V=0.949s

Thus the expression for wo due to P is given by

=6,

Page 66: Process Equipment

tt2 STRESS IN CYI.INDRICAT SHEII.S

and with B2 : 1.0495 nd D2 = 0.00145 E, the equation becomes

144'O2P - 288'S2Qo + 436'59M0 = 2983OQo - 313 'O7Mo

or

5 '2O6Mo - 4'M7Qo: -P

The rotation at point A alue to P is obtained ftom Table 5.3 as

^ p //- r' a. \A = _l:!U +

=u4 +;Vl"P 2q1Dt\ct ' L1 Lt /

or

t, =*n';t'

The rotation compatibility equation at point A is

t')=o = t'

Hence,

429.33P , Mo lrct\ - Qo (cs *co\-{-

-l

-

| -E - zp,o,\c, )' zB?o'\cr' cr,/

or

(1)

-Mo , Qo= -9244

v6,

a1a aa P

T + 896.45M0 + 436.5980 = -657.r3Mo + 3l3.wQo

which reduces to

l2'58M0 + Qo = -3J '48 P

Solvlng Eqs. I and 2 yields

Mo = -0.27 P

0o = -0.08 P

5.2 DISCONTINUITY ANALYSIS

Hence, maximum axial stess is

I t3

" =ry =6Q-'?77:\ = 2s.e P psi0.252

Thb circumferential bending moment is given by

Mo = drI" = 0.08 P

The circumferential force N6 is given by Eq. 5.19 as

-- Etwwe= _T

= 4 {wo^ - wroyr 'to

Et2l-o.og P -o.27 P\R \ zBiDz 2giDz /

= lezt.tu + 84.53) = 2.53 Pu' -'

No.6MoOO : --:' -r ----;--t

_ 2.53 P ., 6(0.08_P)

0.25 0.25'

= 17.80 P

Probbms

5.6 Find the discontinuity stess in the figure shown due to an inlemal pressureof 375 psi. I*t E : 29 x lff psi and p = 9.3.

Probbm 5.6

(2)

Page 67: Process Equipment

I l4 STRESS IN CYTINDRICAT SHEtts

5.3 BUCKTING OT CYLINDRICAL SHELLS

Most cylindrical shells are subjected to various compressive forces such as dead

weight, wind loads, earthquakis, and vacuum. The behavior of cylindrical shells

undlr ih"se compressive iorces is different from those under intemal pressure'

In most instancei, the difference is due to the buckling phenomena that render

cylindrical shells weaker in compression than in tension'

Sturm3 used the system of fbrces in Fig. 5.15 to establish the buckling

characteristics of cylindrical shells subjected to extemal comp-ressive forces'

From the figure he derived a relationship between strains and deflections Using

this relatioiship and Eq. 3. 1 l, he obtained a system of equations .that relates

forces and moments to deflections. These equations together with the equi-

librium equations determined from Fig. 5.15 result in the four basic differential

equations for the buckling of cylindrical shells'

5.3. I Uniform Pressure Applied to Sides Only

For this case, the hoop force is

Ne=-Pr+f(x'0)

where/(x, g) is a function of .x and 0, which expresses the variation ofN0 from

tt" an".uge uutue. Wtten the deflection w of the shell is very small,/(x, d) is also

u.ry ,-u- . Similarly, the axial and shear stresses are expressed by

N,:0+g(ir'0)Ne':O+h(x'0)N'p=0+i(x'0)

Substituting these expressions into the four basic differential equations for the

buckling oi cylindrical shells, and using boundary conditions for simply sup-

oorted J.rds. tire solution for the elastic buckling of a simply supported cylindri-

cal shell due to uniform pressure applied to sides only is given by

c.: rB(!\ 6.27a)

where P., = buckling Pressure

E : modulus of elasticitY

/ = thickness

D" = outside diameter

K=KtI "'(?)

5,3 BUCKIING Of CYI.INDRICAL SHELTS 5

rvr6" + aSoe

r"re +affoo

re+affae

*$oervp" +$ae

..2n. - :=:;---------;1r"'z[N2,\2 - prti - lt - l]3r \t - lt-)

- a * l.+ trlNz[l + (i - t)(z- tt)]-AA

.,2L2 : --n=d-r1

where N : number of lobes as defined in Fig. 5.16

n'r' , ,

N2 L2

N2L2 ,

E-r-: poisson's ratio

l}]

r.r"=+ So'a @o"

lrx + Sox

Fisuro 5.15

Page 68: Process Equipment

I l6 STRISS IN CYLINDRICAT SHETLS

/nlfi"T$d\J/,1,

Cdgor Sitnph Suppod€dSymm.rd.ol Ahour C

Eds6 rirdSymn€rri.ol Aboul

c

Figur. 5.16

F=N2-r*l-t-----Ld- Aa rlt - 1tzlt)ta

{N'?[l + (^ -r)(2- p)]- 1]

(l P,r\ I'{(t - $}tctt - pl + (1 + ri\ + a + 1 + p}t\ Ltl )

1 = moment of inertia : 412

A plot of the ( value in Eq. 5.27a based on the first two terms of expression Fis shown in Fig. 5.17.

5.3.2 Uniform Pressure Applied to Sides ond Ends

The values of No, N,e, and N6 are the same as those for pressure applied to sides

only. The value of N, is given bY

*^=+rge.ol

Substituting those expressions into the four basic differential equations for the

5.3 EUCKUNG OF CYUNDR|CA| SHttrS

Fisure 5.r7 corop,e c..n"""" * -*o.il'Ji'i; r,.",,,.".",,r.,.nry, edses 3impry supporred;

buckling of cylindrical shells, and using boundary conditions for simply sup-ported ends, the solution for the elastic buckling of a simply supported cylindri-cal shell due to uniform pressure applied to sides and ends is given by

Pn = ln, for side pressure only) E *1;r"u.tr r\t | \u, tLL t

"= *(;l (s.27b)

where ": ",.

&(Dj)

^:: ^tF ll7rl2L\F

A4 : A?;---------;;--' -F + (n'r'/2Lt)

A plot of the K value in Eq. 5.27b using the first two terms of expression Fis shown in Fig. 5.18.

tt7

0r4 0.6 I 2 4610 20 40 60 100 m0

Page 69: Process Equipment

r l8 STRESS IN CYLINDRICAT SHEtts

ttl4610 r00 200

vatues of IFisure 5.lS Collopse coefficienls of round cylinders wirh pr$3ur€s on sides ond ends, edges 3implv

supporred; p, : 0.3.1

5.3.3 Pressure on Ends OnlY

For this case,

Ne=0+f(x'0)N" = -t' + g(x' 0)

No'=O+ h(x' 0)

N'o = 0 +i(x' 0)

and the four differential equations are solved for the value of P", For small values

of tfr, the critical compressive longitudinal stress or can be expressed as

ttr20 ,10 6006 I

r l-r0*

o,:n': o.6oE(t)'t\r/

t- : q.or

(5.28)

f,xample 5.9. A cylindrical shell with r : 30 in is simply supported at the

cntl.. il L : l0 ft and t : A315 in., find the critical buckling pressure for a

runilirlrr applictl pressure to sides and ends. Let E : 29 x 10" psi'

Solttlirtlt

2: root

5.4 THERMAT STRESS

From Fig. 5.18, K - 16 and from Eq. 5.28,

I l9

IP". : ( r6)(2e,ooo,r*,(q#)

P". = ll3 psi

5.4 THERMAL STRESS

If a cylinder is subjected to a uniform change in temperature and is allowed todeform freely, no thermal stress is produced. Any restraint that prevents freedeformation produces thermal stress. The amount of restraint affects the stress

level. Figure 5.19 illustrates bar restrained in one and then in two directions. InFig. 5.19a the bar is fixed in the.r-direction only and is subjected to an increase

in temperature. To determine thermal stress, the restraint is first removed and the

bar allowed to deform due to change in temperature. A force F is then appliedto produce the same but opposite deformation. The thermal stress in the bar can

be calculated from the compatibility equation

&:5o

where 6r : deformation due to temperature

6r : deformation due to force F

Substituting the values of $ and E7 in the compatibility equation gives

o = -q LTE for a uniaxial case (5.29a)

where o = stress (positive values indicate tension)

d : coefficient of thermal expansion

AI : change of temperature (an increase is taken as positive)

E = modulus of elasticity

If the same bar is restrained in two directions as shown in Fig. 5.19, the(lcli)nnations due to 4 and 4, are calculated in the same manner as the uniaxialtlolirrmation. The two compatibility equations then become

Page 70: Process Equipment

t20 sTRESs IN CYTINDRICAT SHEttS

il----------'1--1\ ti\____J.i'l*-'-l L-,,

(")

A comparison between Eqs. 5 -29a nd 5.29b indicates that a higher stress

level is obtained when the number of restraints are increased Hence, for a bar

with r.r. - 0.3. a stress increase of 437o results when the number of restraints

incrcasus lirrrn one to two. Another interesting feature of Eqs' 5 '29a and 5 29b

is tlrrl thc thormal stress is independent of thickness and length'

lirlualion 5.29b oan also be obtained from the theory of elasticity Hence, ifc rv AT is substituted into the first two expressions ofEq (3'3), the fo owing

tcsttlls:

+&rH.lN\F\Nl--|l.,l

]--t i{ li-'fI L,.6t o.llE

T----l

L

d = coeff. ol .rp.hsjon (b)dr- ch.nse 1n tenp. (positlve Hhen tenp. lncre.s.s)

T = Polssot's rrtlo Figur.5.r9

&-6r'+/'6"r=0&+p8r,-6"r=0

where g, = proisson's ratio

6i", = deformation due to force 46p, : deformation due to force F,

Solving the above two simultaneous equations gives

l---lrlll-I rl+llt

o;- -

TI

_JL-l*1,*'

a LTE1- tL

for a biaxial case (5.29b)

'r t N

5.4 THERMAT STRESS l2l

from which the expression

Ut : o' : --tl LTE' t- p

is obtained.In a triaxial case, the thermal stress can be determined easily from the theory

of elasticity. Substituting e: a LT in the first three expressions of Eq. 3.1results in

(5.29c)

Example 5.10. An intemal stainless steel rod is welded to the inside of acarbon steel vessel as shown in Fig. 5.20. If the coefficient of thermal expansionis9.5 x 10 6 in./in.'F for the rod and 6.7 x 10-6 in.iin."F for the vessel, whatis the stress in weldA due to a temperature increase of400'F? Use E = 28 x 106

psr.

Solution. Weld A is essentially subjected to a uniaxial stress. Hence,

max 0: E La AT

= (28 x 109(9.s - 6.7)(10 9(400): 31,400 psi I

-laLT = "

(o"- Lro)

_,|a LT = -; (tr, - p,rr,)

-a ATEo,: ct = ", = | _ Zl" for a triaxial case

Fisure 5.20

Page 71: Process Equipment

122 STRESS IN CYLINDRICAT SHELLS

l.)xumple5.ll.Anintcrnu|stuinlcsstrayiswcltlctllrrthcinsitlctr|.acarbtlnstccl vcssel as shown in l'ig 5 2la. ll'the coeflicicnt ol'thermal exprnsion is

g.5 x l0 6 in./in."F for the tray and 6.7 x l0 r' in./in.'F fbr the vessel, what

is the stress in the weld due to temperatunj increase of 400"F? Use E : 28 x 106

psi and pr : 0.3.

Solution. A conservative answer can be obtained by assuming the tray attach-

ment to be rigid. Because the weld is subjected to both hoop and axial stresses'

it can be treited as a biaxial condition Hence, from Eq' 5 29b

-(28 x 106)(9.5 - 6.7X10-1(400)o=@: _44.800 psi

If a more accurate result is desired, then a discontinuity-type analysis can be

performed. In referring nFig.5.2lb, and due to symmetry, the equations ofcompatibility and equilibrium can be written as

(a) ft=6r(b) 0r=0(c) 0z=0(d) )F=0

From the above four equations, the four unknowns 4, Fz, Ft' and Mo can be

obtained.Equation (a) can be written as

ollMo

fn 'l/-fr\_-/ .*F3,h--Fz

I i,o

@l(b)

Fisure 5.21

: deflection of shell due to temperature -l 4 - Mo

F,r F, M(a,,)(AD(r) +'#tt - p): (a,,)(An(r) - rrn- tifi {t)

Equations (b), (c), and (d) can be written as

Ft Mo

-I Mo-n2PrD - BD:

u

Ii+F +4:0From Eq. 2, \:2FMoFrom Eq. 3, n: 2BMoFrom Eq. 4, 4: -4FMo

and Eq. 1 becomes

^l#. #] = 1a", - a,,)(Af(r) (5)

5,4 THERMAL STRESS

dellection of tray due to temperature + Fl

Assuming the thickness of the cylinder is I = 0.1875 in. and using other givenvalues, the value of { from Eq. 5 is

E - -618 lb/in. or o: 618 psi compression in weld

The value of618 psi is significantly lower than the conservative value of44,800psi obtained from Eq. 5.29b because of the ffexibility of the cylinder. If thethickness of the cylinder is r : 3.0 in., then Eq. (5) gives

n = Zl,20O lb/in. or o:21,2O0 psi compression in weld

This value indicates that as the cylinder gets thicker, the stress approaches thatof Eq. 5.29b. In fact, if the cylinder is taken as infinitely rigid, then Eq. (1)becomes

(a,,XAO(r) - p.) : (a-XA?.)(r)

and the equation yields 4 : -44,800 lbiin. or o = 44,800 psi compression inthe weld, which is the same as that obtained from Eq. 5.29b. I

(2)

(3)

(4)

* H<t

Page 72: Process Equipment

t24

5.4.1 Uniform Chonge in Temperolure

STRESS IN CYIINDRICAI. SHELTS

A unitbrm change of temPerature in a component usually results in a thermal

stress both at and adjacent to the component. The magnitude of the stress is a

function of many factors such as geometry, degree of restriction and temperature

variation. The stress can normally be determined from a free-body diagram ofthe various components. The following examples illustrates this point

Example 5.12. A pipe at 10'F is partly filled with liquid at 40"F and gas at

250"F as shown in Fig. 5.22a. What is the maximum thermal stress if a =6.5 x 10 6in./in.'F, E = 30 x 106psi, and p = 0.3?

Solution. A solution can be obtained by taking a free-body diagram at the

gas-liquid boundary as shown in Fig. 5.22b. Compatibility at the interface

requires that the deflection in (a) equals the deflection in (D). Hence' from Eq.\)L

H" M^ HN Mo(axA7i)(r) - ffi* ffi= t")tAl'ttn * rp'o* ,Bo

from which

Hn = @)(Lr1- AAX/)@)(D)

: (6.s x 10-6)(240 - 30)(6X1.4843f(5366)

= 144 lb./in.

,=$

lri| fieas lt

I "--{';"'' --14t" "o' ,--. { ' li| ( 2 )Liquid lli-li

(b)

Figwe 5.22

Hence,

Ne = 827 lblin.

5.4 THTRMAI. STRESS

Also

N.: 2565 lb/in. at interface

t25

M0 can be obtained tiom the second compatibility equation whereby the skrpcin F\g. 5.22a at the interface is equal to the slope in (b). Or

Mo __!, _Mo, Hs

BD 296: pD- 2B'D

and Mo : 0.The circumferential force in the pipe due to I1o is obtained from Eqs. 5. 19 and

5.24:

t't':4' H: c"r 2BtD "w

Maximum value of Cp. is obtained from Table 5.1 as 1.0. Hence,

M": O

and

t\6<Max o: o.rrr- = 20.500 psi

The maximum bending moment due to I{0 was derived in Example 5.4 as

"":Y "Stress due to bending moment at Bx = r/4 is

6M 6 (o'34H0\ = l2,ooo psio':v:vx p /

Deflection due to flq zt Bx = n/4 is obtained from Eqs. 5.23 and 5.24 as

o.322Ho

2B"D

B'=x

Page 73: Process Equipment

t26

end circumfcrcntial $trcss is

sTxEss lN cYllNDRlcAt SHELl"S

827 ^oo= #+ 0.3 x 12.000 : 10,200Psi

Thus maxrmum stress occurs al rnterface with magnitude of 20,500 psi. I

Example 5.13. Determine the bending stress in a cylinder fixed at one edge

(Fig. 5.23a) due to a uniform rise in temperature of 200"F.

c = 6.5 x 10-6 in./in..F

E:30xl06psip=o'3

Solution. Radial deflection of cylinder if ends are free is

w : (a)(Afl(r): 0.039 in.

From Fig. 5.23a the rotation at the end is zero because the cylinder is fixed.

Hence

M" O^

BD zB,D

Qo = 2PMo

/1\-lMo

Hs

Fisur€ 5.23

(b) {! * aB'*:EJ$tlx- fl,)(5.30b)

5.4 THERAAAT STRESS 127

ln the second compatibility equation the deflection due to temperature plusmoment plus shear is equal to zero. Or

o.$s + #_#:oand

Mo: (0.039)Qp2D)

: (0.039)(2X0.46941 (42.e30)

= 738 in.-lb/in.

6Mo = :+ = 70,800 psi I

5.4.2 Grsdient in Axiol Direction

The stress in a cylinder due to a thermal gradient f, in the axial direption can beobtained by first subdividing the cylinder into infinitesimal rings of length dr.Hence, the radial thermal expansion due to 4 in each ring is given by (c)(4)(r).This expansion can be eliminated by applying an external force { such that

deflection due to P, = deflection due to I

Hence

and

E= ",r,

p, = Etan

r

-Prae: -l : -taT.Because the cylinder does not have any applied loads on it, the extemal forceP, used to reduce the deflection to zero must be eliminated by applying an equaland opposite force in the cylinder. Hence, Eq. 5.21 becomes

(5.30a)

Page 74: Process Equipment

Itt STRTSS rN CYIINDRICAL SHEttS

Thc total strcss in thc cylindcr is dctcrmincd from Eqs. 5.30a and 5.30b.

Example 5.14. A vessel that operates at 800oF is supported by an insulatedskirt. The thermal distribution in the skirt is shown in Fig.5.24a.Ifthe top andbottom of the skirt are assumed fixed with respect to rotation, what is themaximum stress due to temperature gradient? d = 7 x 10-o in./in.'F, p =0.3,8= 30 x 106psi.

Solutian, The equation for linear temperature gradient is

T,:4+4 iT*

The temperature change can be expressed as

{a)

Tx rv=(EJ, )x=-sx

A'lr t

t\t\

J_/

(dFhut. 5.21

Tb= 2odF

t-aodF

r n-T=rx

and the circumferential stress due to ring action obtained from Eq. 5.30a is

5.4 THIR 'tAt STRISS

E4uation 5.30b gives

and w reduces to

From Eq. 5.19

(l)

e").

",=+:*(T) (2)

.="u$(Lf),*",which upon substituting into the differential equation gives

t,=# and cr=9

w=rq.

129

,,= -u"(T),

onfu * o.o* =";;(*),

A particular solution takes the form

Adding Eqs. I and 2 results in

oe= 0

which means that for a linear distribution the thermal stress along the skirt iszeto.

The slope due to axial gradient is given by

- dw lT" - T,\u = --:- = ral -----=; Idx\r/

Page 75: Process Equipment

rt0 3TRr93 lN CYI'INDRlCAt gHEtts

Bccausc thc cnds arc fixcd against rotation, a momcnt mu$t be applied at the ends

to reduce 0 to zero. From Eq. 5 24

lr, - r^ -Mo'"\ , )= B,

u,= -oolff)<n- n

Since B = 0.2142, D = 2.74'1 x 106 '

Mo = 742 in'-lblin'

and

o = ,1450 psi

5.4.3 Grodient in Rodiol Direciion

Thermal stress in a cylinder due to a temperature gradierrt in-the radial direction

can be obtaned from ttre theory of elasticity' Hence, Eq' 3 can be written as

,,=!f",- tL(oo+ c)f + ar

*: jl", - P(at + o)f + uT

u=|b,- p(a,+ os)l+ ar

where aT is the suain due to temPerature change' If the temperature is sym-

^"iii" *i,tt respect to 0, all shearing stresses are zero and the radial and hoop

$truins can be exPressed as

I

dww',=6 "=i

(5.31)

6 32)

(5.33)

or

I de9\e,: ee + r\a, )

(5.34)

I.4 THIRMAT 3TRI33

Substituting Eqs. 5.31 and 5.32 into 5.34 gives

/ do.\ p do,o,: {rs* r\*)- t_*to,trdr-oo)

. (r-- J",' . ^,(#)(s.35)

In Section 5. I it was shown that the equilibrium of an element in a cylinder (Fig'

5.3) can be expressed by the equation

",- ''='(*\

Solving Eqs. 5.35 and 5.36 for a gives

dlt d , .f -E ,, , ..,-(41\,kl;ftt,'",t|: T.;;"tr * rt,\i) (s'37)

Solving the above differential equation and applying the boundary conditions

|lr

(5.36)

o. l = 0

i="4l=0

gives

Ea-l + P(r'z - r? ['" rra, - [' rrar\o. = -:-------'-- _--' | - tt' r' \16 - ri J., J,, /

Frorn Eq. 5.36

E<x r + u' (rl! :j ['. r,a, - [' rra, - rr\ (s.38)oa= t - ttz I \rj- r? J,, ""' J,," /

and from Eq. 5.31 for a cylinder umestrained in the:-direction,

Ea / 2 r,-, -\ot = _-_l_-;__ ,l trar_ tl- L- p\ri-rih, /

From these equations, some cases can be derived.

Page 76: Process Equipment

t32 STRTSS IN CYTINDRICAL SHTLLS

Cav L Llnear'l'hcnnul l)islrihulion

[,irr thin vcssels, a stcady-state condition produces linear thermal dishibutionthrough the thickness that can be expressed as

r - r'L-J

where d : inside wall temperature relative to outside wall temperature.

Substituting f into Eqs. 5.38 gives

EaT, f (r2 - r\zrt + r.)rt-:

-l

' r'(l - 1t\ | 6(ri'r r")

EeT f (r2 + r?)(2rt + r")nr-r-\t - pl L otrr r ro,

LAIi I zrt+ ro r"-rl' (l - pll3(r1 + r,) r"- r,l

6(ri - r")

2\r3 - rl) - 3r"(r'z - r!)l^

| \J.J')o\r, - ro) I

2(r3-rl)-3r"(r2-r!)

Figure 5.25 is a typical plot of o,, ae, and cz. The plot indicates that o, isrelatively small compared with o6 and o,. For all practical purposes, o6 and o.are equal.

The maximum values of op and ol occur at the inner and outer surfaces. From8c.5.39.

"/ffi

And for thin wall cylinders. Eq. 5.43 reduces to

5.4 THERMAI STRESS

-EaT,f 2r,, + r, lov= o,- l, . .l| - pLJtr. -f ritlEaT f r"+ 2rt1ue=u,=. l-l| - p LJtro -f riJ l

For thin wall vessels, Eq. 5.40 reduces to

- EaTtCfe = C, = ,r,l _!\r tL)

EaTce: o,: ^-Ltt - lL)

t33

for inside surface

(s.40)

for outside surface

for inside surface

for outside surface

(5.41)

(s.42)

for inside surface

(s.43)

for outside surface

Case 2. Logarithmic Thermal Distribution

In thick vessels, a steady-state thermal condition gives rise to a logarithmictemperature distribution that can be expressed as

t: "/lu l"')

\ln r" - ln r,/

and upon substitution of this expression in Eqs. 5.38 results in

Again disregarding or as being small compared with o6 and o", Eqs. 5.42have a maximum value of

'(;)l#cr.l'-'^? - *('. #)'(;)]

u?T:,, r1, - 2Lnk-,t'i,,n/tr)l- p,ntro/nL r ri-r; \/,/l

ErxT f, 2rl ,lr"\f

-t

r - --------- lnt -ll- pJ tntro/ rJ L 16 - ri \r, / l

2(l

z(r

2(r

z(rEaT I. 2,1 . /a\l

- t"t t"lJ,)L' ;:'l' 'n\-/l

Page 77: Process Equipment

t34 STRESS tN CYUNDRTCAL SHfl"t"S

I')tt'li lirr insidc surlacetft: (r: - ,zt<l _ tl

EqToe: o, = Z\l _ lD lor outslde sunace

which are the same as those for the linear case.

Case 3. Complex Thermal Distribution

ln many instances such as transient and upset conditions the temperature distri-bution through the wall of a vessel cannot be represented by a mathematical

expression. In this case a graphical solution can be obtained from the thermal

stress. From Eq. 5.38

- - eq lt-rr,lf.'t'z[,.rrar-!f ,ror-r]oe: l- *l-rz, - r, 1, r- J,, IFor a cylinder where the thickness is small compared to the radius, the firstexpression in the brackets can be expressed as

I r trilrt2 p --,- : 2r Ji: Trdr-----';-'------- | IrAr :

r; - ri J,, ntr; - ril= mean value of the temperature (5.44)

distribution through the wall

'l'he second expression can be expressed as

I trc-, 2n fiTrdr-l rror: ---': ,r' J,, 27Tr -

: one half the mean value of the temperaturedistribution from the axis of the vessel to r

However, because the temperature distribution from the axis tocxpression 5.45 for all practical purposes can be neglected. Hence,

cxoressed as

/5 45\

| 15 Z€rO,

oo can be

(5.46)Ea .^oo: --\1n - I)I- IL

4n : mean value of temperature distribution through the wall

f : bmDerature at desired location

wncrc

Fisure 5.26

5.4 THERMAI. STRTSS

From Eq. 5.38 it can be seen that cr, can also be expressed by Eq. 5.46.

Example 5.15, A thin cylindrical vessel is heated by ajacket from the outsidesuch that the temperature distribution is as shown in Fig. 5.26.1f E : 27 x 106psi, a : 9.5 x 10-b in./in.'F, and p, : 0.28, determine (a) maximum thermalstress using Eq. 5.40 and (b) maximum thermal stress using Eq. 5.41.

Solution. (a) 4: 400 - 700 = -300'F. Hence at inside surface

-(27 x t01(9.5 x tO-ox-300)/2(lJ) - t0\- (t - 0.28) \3(13 - tO)i

= 55,800 psi

and at outside surface

t35

u = -- ,1 _ 92s1 \ :tr: _ rot

= -51,000 psi

(b) For inside surface

(-27 x 109(9.5 x l0 6)(-300)

'': 2(r - or2s)

: 53,400 psi

and for outside surface a = -53,400 psi. I

Example 5.16. A pressure vessel operating at 300'F is subjected to a shortexcursion temperature of 600'F. At a given time, the temperature distribution in

(27 x 106)(9.5 x 10 6)(-300) lt3 + 2 x 10

(l-028, \3(13-lo)

Page 78: Process Equipment

It6 3TR!!t tN CYUNORICAI sHEtLs

thc wall is shown ln Fic..3.27 . Find thc msximum thcrmal stress at that instance.

Lct rr = 0.3, E = 3dx 106 psi, and a = 6.0 x 10-6 in./in."F

Solutlon. This problem can be visualized as a biaxial case where the inner

surfacs heats quickly while the rest of the wall remains at 300'F' Using Eq.

5.29b results in

(6 x l0-6x600 - 300x30 x 106)o:ffi= -77,100 psi

which is extremely high and is based on very limiting assumptions. A more

realistic approach is that based on Eq. 5.46. The mean temperature is obtained

from Fie. 5.27 and tabulated as follows:

Locations as

Ratios of ThicknessTemperature

T Area

00.1

0.20.30.40.50.60.7

0.80.91.0

And I' = 356"F.From Eq. 5.46, at inner surface,

600

460

400

370

340

320

310

305

300

300

300

53.043.0

38.5

35.5

33.0

31.530.8JU.J

30.030.0

>355.6

_ - (30 x 106)(6.0 x 10-6)/?56 - 600)

= -62.700 psi

ond Bt outcr surface

., _ (30 x 196x6:0_x 10-6)(356 _ 3oo)" l-0.3= 14,2100 psi

NOMIIiICTATURI

It is of interest to note that the high sness occurs at the surface only. Thus atone-tenth of the thickness inside the surface, the stress is

_ _ (30 x 10ux9I_!o-1res6 _ 460)t= r-o!3 \JJu 'uu''

= -26,700 psi

The high stress at the inner surface indicates that local yielding will occur. I

NOMENCTATURE

Fl3l'l = -----=:-" l2(1 - tt2)

D, = outside diameter of cylinder

E = modulus of elasticity

K = constant

L : length of cylinder

M, = axial bending moment

t37

tisur' 5.27

Page 79: Process Equipment

rtt

Mp ' hoop bcnding momcnt

p = pressure

P", = buckling pressure

P/ = internal pressure

Po = extemal pressure

O, = shearing force

r : radius of cylinder

4 : inside radius

ro = outside radius

, = thickness of cylinder

T = temperature

AT = iemperature change

p = deflection

c = coefficient of thermal expansion

B

6

€t

€t

e0

0

lL

o

Ot

or

Oe

= deflection due !o temperature change

= longitudinal strain

: radial strain

= hoop strain

= rotauon

= proisson's ratio

: stress

= longitudinal stess

= radial shess

: hoop sftess

ETRI'I IN CYTINDRICAT SHTTT!

REFERENCES

l. Murphy, G., A 'anced Mechanics of Materials,

ll4-t2t.McGEw-Hill, New York, 1946, pp.

IIIIIOORAPHY

2. American Society of Mechanical Engineers Boiler ond Prcssure vessel Code, Sdct/.rn yrrl-Rules for Constructiotr of Pressure Vessels, Division 1, ANSI/ASME BVP-VI -l,NewYork,1980 Edition.

3. Strum, R. G., "A Study of lhe Collapsing Pressue of Thin-Walled Cylinde$," University ofIllinois Bulletin, Vol. XXXIX, No. 12, 1941.

BIBI-IOGRAPHY

The Amedcan Society of Mechanical Engineers, Ptessure Vessel and PipinS DesiSn-ColkctedPapers 197-1959, New York, 1960.

Baker, E. H., L. Kovalevsky, F. L. Rich, Stn ctarulAnalysis ofShells, Mccraw-Hill, New York,1912.

Flugge, W., Stesses in Shells, Springer-Verlag, New York, 1960.

Gibron, J. E., Linear Elasrtc Theory oJ Thin SherrJ, Pergamon hess, New York, 1965.

Hefey,I. F -, Theory and Design of Moder PresJrt? y?JtetJ, Van Nostrand-Reinhold, Princ€ton,N.J., 1974.

Timosheoko, S., S. woitrowskey-Krieger, frreory of Plates 4r1d Shelrs, Mccraw-Hitl, New York,1959.

t39

Page 80: Process Equipment

Con|co|hrodconsistingof|woeccgn|liccones.(co',rtesyoftheNool€rcorPorgtion,sr.LoUi!,Mlo.)

r40t4l

CHAPTER 6ANALYSIS OF FORMED

HEADS AND TRANSITIONsEcTtoNs

Page 81: Process Equipment

142 ANAI.YSIS OT TORMTD HEADS ANO TRANSITION SICTIONS

6,I HEMISPHERICALHEADS

The required thickness of hemispherical heads is determined from a free-bodydiagram as shown in Fig. 6.1. Hence

Pm2 = Zmo

', Pri-2t

where a= membrane stress

P : pressure

r = radius

t = thickness

This equation which assumes uniform stress distribution through the thick-ness, is adequate for relatively thin heads. As the thickness increases withrespect to the radius, this assumption becomes invalid. Hence, a more accurate

formulation is needed, which is obtained from the "thick head" equations.

From symmetry, it can be demonstrated that at any point in a hemihead

subjected to uniform pressure,

From Eqs. 3.1,

(6.1)

(t6.2)I.

e, = E\ot - zlto,)

FisiJr€ 6.1

6.I HEMISPHERICATHIADS

1...eo: ELt

t - lL)1o4, - pa,)

t43

(6.3)

(6.6)

The strain displacement relationship is the same as that derived from cylindri-cal shells:

and

dw

Hence, expressions 6.2 and 6.3 become

(t - QfrQo6) - vfiWS - o, * 21t'o6 -- o (6.4)

Figure 6.2 shows an inflnitesimal segment of a spherical head Summation offorces in the radial direction gives

(6.s)

w'f

,",= -l(fi)<,'"t

i12

5r-

Solving Eqs. 6.4 and 6.5, we obtain

ld\l' , 'r

rl; ll+ +(rro,) | : 0\dr / Lr- qr I

Its solution is expressed as

The boundary conditions are given by

o,= -n al r: ri

and

a,: -n at r:ro

Solving the boundary conditions forA and B and substituting into Eqs. 6.5 and

6.6, we obtain

Page 82: Process Equipment

l.l{ Al'lAtYlll Ol lOR illD H!AD3 AND TnANSl?lON SICTIONS

r?P' / rl\ r3P / 't\06: oo= -:ll + -l - -;l=lt +:+lr; - ri \ zr'/ r; - /i \ 2r./

Equation 6.7a can be simplified for the following cases:

Case 1. Internal Pressure Only

max o.= _e atr=ri

max oo = or: | :?.'?r* ')r,]n at r = riLzlr; - ri)l

Case 2, Exlernal Pressure Only

maxot= -P. at r:r3 rlkrnrxa6= ot= - ZE:;, atr=ri

(6.7a\

(6.7b)

[6.-dor \\ ' ' d. /

Figure 6.2

",:f+('-*)-*('-*

(6.7c)

6.I HIMISPHERICATI{TAD3

Jo/f I

fisurs 6,3

A comparison between Eqs. 6.1 and 6.7 is shown in Fig. 6.3.

Example 6.1. A hemispherical head with r = 15.0 in is subjected to an

internal pressure of 4000 psi. If the allowable stress is 23,000 psi, find the

required thickness from Eqs. 6.1 and 6.7.

Soltttion. From Eq. 6.1,

,:+- (4000x1s)

2(23,000)

= 1.30 in.

From Eq. 6.7,

rln l. ,11o.: _-i_-1 | I _r : " Iri,- riL zril

Page 83: Process Equipment

ANAIYSIS OT TORMED HTADS AND TRANSITION STCTIONS

= 16.31

t : 1.31 in.

6.1.1 Vorious Looding Conditions

Occasionally, hemispherical heads are subjected to a variety of loadings such as

wind forces, snow and dead loads, and agitator and equipment reactions. The

membrane stresses induced by such loads usually are obtained from "thin shell"

membrane theory that assumes that the loads are carried by membrane action

rather than bending moments.When referring to Fig. 6.4a, the middle surface of a shell is taken as a surface

of revolution. This is generated by the rotation of a plane curve about an axis

in its plane. This generating curve is called a meridian. An arbitrary point on the

middle surface of the shell is specified by the particular meridian on which it isfound and by giving the value of a second coordinate that varies along the

meridian and is constant on a circle around the shell's axis. Because these circles

are parallel to one another, they are called the "paralled circles."The definition of r, n, 12, and @ are shown in Fig. 6 4a. The radius 11 is

mcasuretl from point 0, which is the center of curvature of the meridian; 12 is

mcasurctl fiom the z-axis and is normal to the meridian. The parallel circle isdolincd by r.

lirrrrr lrig. 6.4a,

r = 12 sin $ds = r, d.6

lrigruc (r.4/r is a free-body diagram of a section of a surface of revolution.

Srrrrrrrrirrg lirrces parallel to the tangent at the meridian and simplifying by

th.lctirg lt:rrns of higher order, we obtain

-!, gN,pt - r,(q# -r,Npcos d + 16',) = gt4l, \ do /

I

2(15t(4000) + 2(23.000X l5 )3

2(23,000) - 4000

6.I I{EMISPHERICAIHEADS 147

f :re SrN0

cls:f1 d0

dr - ds .Cos P

r'r6e+ ffi dQ

N@+tl do

Noo + *F de

++ do

Figure 6.4

Summation of forces in the direction of parallel circles gives

,i a:*Ut=n\12rt

For the majority of pressure vessel applications, the loads are symmetric with

respect to the axis of revolution. Hence, all derivatives with respect to 0 in

expression 6.8 and 6.9 can be deleted. Shearing stresses due to torsion are small

comDared with other stresses. Thus expression 6.9 can be deleted completely'

Tire last equation of equilibrium is obtained by summing the forces in Fig'

6.4b perpendicular to the middle surface:

j6<,N*l -,,(#* rlNep cos 6 * r,',) :0 (6.9)

(6.8)(6.10)

Page 84: Process Equipment

I4g ANAI.YSIS OT TORMTD HTADS AND TRANSITION SICTIONS

Substituting oxprcssi()n 6. l0 into 6.tl givcs

I fr 1No: . -,,, , I I r, r2(P, cos {- Pasin Q)s\nQdQ + Cl (6.11)12 sln- @ LJ I

The right-hand side of Eq. 6.11 is equal to the sum of all the N6 forces arounda circle of angle d. Therefore we can solve Nd at any given location { bysumming all forces in the {-direction. Once N6 is obtained, Nd can be deter-mined from expression 6. 10.

For a spherical shell, 11 = 12 = r. Hence, expressions 6.10 and 6.11 can besimplified as follows:

N5 I N6= P,r

" t. I (6 12)No : ^,-, .l ltP, cos @ - P6 sin @) sln $ d$ + C Isln - @ LJ I

The displacement for various loading conditions is derived from Fig . 6 . 5 . Thetotal change in length AB is

u:4ra6 - w d6taQ

The strain is therefore

1/do w\ea=-l-;--l\ \aQ rr./(6.13)

)(-

i-d0

Fisurs 6.5

'fhc change in r,, is given by

Ar' = Dcos A -:=srn @

and the strain is expressed as

,r=!1ucos@-wsin@)

6,I HEMISPHERICAT HEADS I49

(6.14)

Substituting ro = 12 sin { and Eqs. 3.3 into expressions 6.13 and 6.14 gives

(6.15). h.__lt:ucotO- EtlNe f"Na)

Equations 6.15 can be solved for the deflections once N, and Nc are estab-

lished from Eqs. 6. 12. Table 6.1 shows the solution of Eqs. 6. 12 and 6. 15 forvarious loading conditions.

Example 6.2. Determine the forces in a spherical shell due to snow load.

Solutian. From Fig. 6.6,

P, -- -P" cos2 Q

P:P,cosdsind

From Eq. 6.12

rlN^ = +-l f(-p, "os' S - P" sin2@ cos @) sin A dQ + Cl' sln- q)LJ I

-p"rf r I=,.'i' ;l l(cos' d + sin'z d) sin 6 cos 0 dO + C Ism- qlJ I-a-P", lt. ",1 ^l:rtt}Lts'n-@l+c.l

.- -P.r 4rC/vr :

-

- -

2 sin 0

As 4 approaches zero, the second expression of Nd approaches infinity unless

C is set to zero.

Page 85: Process Equipment

;.t'

!l

.trrr

r^r

<f ! ,9,/+ --,{

- ..l+

= +k!

| | -lc

le

-i,+

.f;|*

+

\j/

l5lr50

I

!l !la oo-l dl

eo

o.

+

!lrl

r-;-1-l'1

-l+

'.t ..lN*il

!te.tr

f---l

+

NI

+

@e

!'6

o

.tq.

c

o

oo

o!

oI{t

IIoo

-o

Page 86: Process Equipment

152 ANAI.YSI! OI TO|.MTD H!ADs AND TRANSITION SICTIONS

Thus, for C = 0

From Eq. 6.12,

-P.;

rle: -r.r cos' q + \

Yr= -P.r(cos2 Q - L)

= -4cosz|

6, L2 DiscontinuitY AnolYsis

'l'hc rnctnbrane analysis discussed in the previous section fails to Sive adequate

rcrult$ whon the loais are localized or when the hemispherical section is attached

to lnothcr shell that acts differently under certain loads' In these cases the

hcnding moments must be considered in the analysis' In Figure 6'7 it is seen that

lix u givcn krading condition, the membrane and the bending moments can be

con$id;rcd us shoin. Proceeding as before where both the free-body forces and

Figor€ 6.6

6.1 HtMllpHlRlcAt l'llAol ltl

the comDatibility equations are taken into consideration, a complicated numb€r

"i.i*oii-*ut Oifierential equations result' The solution of these equations is

imoracticat. however, withouisome simplifications. By assuming symmetric P.

forces only, the differential equations for a spherical shell reduce to

#r.#*rQ- o(cotz O+ tD= -#and

(6.16)

(6.17)

#**Affi-o<""eQ- rt)=Eto

EilBRAI{E FORCES

8 EIIDI NG FORCES

Fig'.rre 6.7

Page 87: Process Equipment

lla Af{Al,Ygl ot fotMrD HIADI AND TRANIITION SlCrlONS

whcrc 0 is thc anglc of rotation and is given by

By a rigorous analysis Gibsont has shown that in Eqs. 6' 16 and 6.17 only the

higher-order terms are significant in most usual pressure vessel applications.

Accordingly, the equations reduce to

^ a ldwr raQ

d2 o _ -Qrzdo' D

(e: ",,dE'

Eliminating 0 from Eqs. 6.19 and 6.20 gives

(6.18)

(6.1e)

(6.20)

(6.2r)

where

ffi++*o=o

/ ,\2,\a=3(l-r1l;/

Nr- -Qcot0

N" = --9-do

M^:2(+\- r \dQ/

Mo = pMo (6.23)

(6.22)

The solution of Eq. 6.21 can be expressed as

g: g^o(c1cos A0 + c, sin,\@ + e-^o(ct cos,\d + c4 sin ld)

Once the value of O is determined for a given loading and boundary condi-tbns, the other quantities can be obtained from

6.t HEITATSPHERICAI HIADI ll!

0 = slope

| /d'zo\EVG)

w : radial deflection

r ..,I F;lt\ e - luYA)

The solution of Eq. 6.23 for various common loading conditions is given inTable 6.2.

Example 6.3, Calculate the head discontinuity forces of the head-to-shelljunction shown in Fig. 6.8a. Let p : 3gg psi and /, = 0.3.

Solutian. From Fig. 6.8b and Table 6.1 the deflection in the head due topressure rs

_ (300x50)'?rl _o?lE(0.50) '-

_ 1,050,000

E

P126o :

=(l - ,r) sin

Tqble 6.2 Approximote Force qnd Deflection funcfions for Sphericol Segments

I,//-r-\Hoftflff)--xo'<l"L/

a

lO

lr

6

-f e-rYsln4ocos ( rr+"/+)no

2re-r1sln{o(cosr.r)tio

Vi*e-rYst nqrotocos { ry+nllltto

L-rYsi n0osi n (ry ) Ho

to f""-rt"t no" [zr"t no"o"rvtT(-rF*""o"""t rv*r+l]J

1; t-z'F^2u-tt" rnro"i n (r.r+r/a)l

?I "-rtrtn(rr)ru

z16.f. "-^t"o,

( rr*nrl)no

-?1 e-11cotosi n ( ry)ro

y6-"- r'r" i n1r1*nll lto

,ao lzre- ry I-,6- rs tiocos{ ry+r/a)-+ucos0sinrYl,l

ro /-1r,3 "-rt.o"rr\rT \-- /

Page 88: Process Equipment

It6 AltlAtYlll Of iotlillo HIAD! At'lD ltAilllTloN slcTloN3

Figirr€ 6.8

8nd

- O.3)(lqoJ

12.038

6,:Wl^ouo=-2f4

From Table 6.2,

8Ho+Mo=-995.17 (1)

6.r HlMrsPHtRtcat HtADs lt7

6,"=s#6

,rr: -3#ro

Similarly, the deflection in the shell due to pressure is obtained from Eq. I ofExamnle 5.5 as

tt\_;,,='#('

and from Table 6.2.

B=

= 0.1818

E/ | n\3D=-ij:j_=0.0916Era\t - u.J-)

:ffi,,-0.,r,_ 637,500

E

u,":,--#4r"

eo" = aEEm

6rr=yM,

0,"=gfMo

total deflection of head = total deflection of shell

r.r+4pq * Tr" * Y*" = q# _ ryH" * Yr,

OT

Page 89: Process Equipment

I58 ANAI.YSIS OI FORMED HTADS AND TRANSITION SICTIONS

Sirnilurly,

rotation of head : rotation of shell

-579.65.. 2t9.tt .. 165.15.. 60.05..._-t uo - E *o: - -E-nrt --iwo

rlo = -0 818 Mo

and from Eq. 1,

Mo : 179'4 lb-in'/in

and

Ilo = - 146.8 lb/in.

From Table 6.2, N0 at discontinuity is

)A2 prN.: 2tH" +':::-M^ + -2

: z(r2.o3s)(-146." * ?g?qg@-' !9PNe= -3534 + 1040 + 7500

No = 5006 lb/in'

and

y^=A=7500 lb/in.

Mo : 179.4 lb-in'lin.

and

Me : 53 '8 lb/in' I6.1,3 Thermol Sfress

'l'hc dcrivation of thermal stress in a spherical segment due to radial distributionol ternpcrature can be derived similarly to cylindrical shells (see Section 5.4.3).Thc meridional and circumferential stresses in a sphere are the same due to

6.I HEMISPHIRICAIHEADS

symrnetry, expressed as

ZEa lr'-r| r,.^,, f -,,\O,:-l-ltr-Ar-ltr-Arltt - p)r'\r; - ri ,, ,, /

159

(6.24a)

Eu l2r3+rl r"-,, f,^,, ,-\06: ao: ^l .. I Tr.dr + | Tr.dr - r.Tl \6.24b)tt- p)r- \r;-ri J,, J\ /

Example 6.4. Determine the circumferential thermal stress on the inside sur-face of a hemispherical head subjected to an inside temperature of 600'F andvarying linearly to a temperature of 400"F at the outside surface. Let 11 :30in.,12 : 40 in.,E : 30 x 106psi, o : 7.0 x 10-6in./in.'F, and g, : 6.3.

Solution. The temperature distribution across the thickness can be expressedAS

r=6oo_ Lg_rs

or

T=1200-2Or

The first integral in Eq. 24b gives

f; r,,a, = J* trzoor, - zor3tdr

= 6.O50.000

The second integral is zero because the limits of integration at the inner surfaceare both ri. Hence Eq. 6.24b gives

(30 x 106)(7 x l0 6)

(1 - 0.3X30t

[2(3ot + (30t.. ^-^ ^^^. ^^ .ltffi ro'o5o'ooo) - (3ofll2oo - 2o(rnj

= -32,800 psi I6.1.4 Buckling Strength

The buckling equations developed by Von Karman and Tsien2 are the basis ofthe design equations developed by ASME. Von Karman's equations, which aresubstantiated by tests, give a more accurate prediction of buckling strength of

Page 90: Process Equipment

160 ANAI.YSIS OT FORMTD HTADS ANO TRANSITION SICTIONS

splrcricul sccli(nls tlurl thosc dcvclopcd carlicr by l.luggc, Timoshenko, andothers. Von Karrnan antl 'l'sicn took the out-ot-roundness imperfections intoconsideration. 'l'hey also used the energy equations as a basis for derivation.Refering to Fig. 6.9, it can be shown that the strain energy due to the extensionof the sphere is given by

u,: Er'(!\o f fYJ^- r)'sin d/d (6.2s)' \r/ Jo \cos a /

Similarly, the strain energy due to bending is expressed as

,, _ -_,/,\ T (p -., ,fcos0 d0 ,\') , /sin 0 .\,1 .,U7: Lr"l-l; I srn Ql--- _ -ll+l --tlld6

6.26)\r/ tz Jo lcos @d@ / \srn A / |

The potential energy of the external pressure p is given by

-rBU1: Prit I P sin'?dcan 0 - tan O) cos Q dg (6.27)JO

The total energy of the system is the sum of Eqs. 6.25, 6.26, and 6.27 . Hence

U=Ut+U2+Ur (6.28)

Equation 6.28 can be simplified by assuming B to be small. By neglecting termsof higher order and expanding the sine and cosine functions in a power series,liq. 6.28 becomes

U E(t/rt rp ,^,-:-# | (0. - 6'\6d6Tr" 4 Jo

.ry rUffi-'l . G- 'flaoo+PrQz@-Q)dQ (6.29)

'l'hc solution of Eq. 6.29 is obtained by the Raleigh-Ritz method by finding ancxprcssion of the deflection that satisfies the boundary condition

0:0 at 4:0s:B at Q=B

6.I HTMISPHERICAI.HEADS t6l

(6.30)

(6.32)

Such an expression can be written as

o:alr-c,1"-4)lL \ p'/lwhere 0 is the slope and is related to the deflection by

a: , fu @ - o) dO (6.31)JO

From Eqs. 6.30 and 6.31 the value of C, can be determined to be

^46wt -;F

Substituting Eq. 6.30 into 6.29, the energy expression becomes

It / 14\ / Ci Ci\ Et, ^,^, pBo_-: l+186lCl _ ir-al - "" B2ct _,_L cin' \bur/ \ 7-i) - l8tP-ci-pc'This expression can be minimized by taking its derivative with respect to Cr andequating the derivative to zero. This gives

or 4 /a\f-. ..ls\t/r /.^6, _^\trlr),]a =

ros \;/L'zr - 63\i)F - lot7 * 'o)'p-l (6'33)

where

Pro:'

and D is obtained from Eq. 6.32.

Figure 6.9

Page 91: Process Equipment

I62 ANAI,YSIS Of fORMTD HEADS AND TRANSITION SICTIONS

A plot ol l!. 6..|.1 is shown in lrig. 6. l(). 'l'hc nrinirnum value ol ljq. 6.33crn bc lirund by taking thc derivittivc with respect to B and equating the result(o zero:

or 4/D\l + (3/280)t6/r),Et 5\r/l + t24/3st(6/tP

(6.34)

which is shown as a dashed line in Fig. 6.10. This figure illushates the effectof 6/t on the buckling shength of spherical sections. The minimum value ofbuckling strength is obtained from the figure as

!=o.z+ at 9:9.35tt t

The value of 0-24 can be reduced if the strain energy due to membrane stressbefore buckling is considered. Therefore, if Eq. 6.25 is modified to include thisstrain energy and if the revised expression is substituted into Eq. 6.29, the

1.2

1.1

t.o

o9

o.8

o.7

o.6

o.5

o.4

o.3

o.2

o.1

.o

64.rc%

Fisure 6.10

('REt

\l--\

\t, '#;*t, I 20,l

.15

,r)

5\,7

I (\

Eltve op,i

6.2 ETTIPSOIDAL HTADS

dil'lerentiation results in an expression whose minimum value is

fi = o.rtt

Experimental values have shown that the minimum value obtained is of the orderof

r63

Dxample 6.5. What is the required thickness of a hemispherical head subjec-ted to an external pressure of 15 psi? Let r : 96 in., E : 27 x l0o psi, andfactor of safety (FS) = 10.

Solution. From Eq. 6.35, with o", : (FS)o and o: Pr/Zt

ff: o.tzs

(,t)'"''(;) : ' '*

,ro: 2

Ne: +Prz=j;-

(6.35)

(6.36)

= 0.45 in.

6.2 EttIPSOIDAt HTADS

The governing equations for the design of ellipsoidal and torispherical heads areobtained from expressions 6. l0 and 6. I l. For internal pressure, P. : P, P6 : O,

and the two equations give4

I

(15X96)110)

0.25(27 x 106)

14 18

We can write Eqs. 6.36 in terms of the major and minor radii a and b. Using

Page 92: Process Equipment

l6tl ANAl,Ytlt Ol lOt,UlD HtADt AND TRANSII|ON SICTIONS

fisure 6.ll Ellipsoi&l heod.

the notations of Fig. 6.11, we then obtain

a2b2(az sin2 Q I b2 cosz E1zlz

n2''

1a2 5i1z Q r b2 cos2 qlrlz

Expressions 6.36 then become

^, -Po' I^6- 2 @rJfI? AT brrxf, O,7t

,, _ Po' b' - (a2 - b2) sin2 E2b2 (a2 sin2 6 i b2 cos2 q1r/z

The radial deflection rll and meridional deflection ll due to intemal Dressureare given by

(6.37)

GIu'-,l;t

Pa'nD^2

n W'(Fcosv)

ulc'- l] and

6.2 rruPsotDAt HEADS

where

ffi''r)"G= \/l + [(a/ br2 - 1] cos2 7

At any given point on the ellipse given by.re and y6, the angle { can be obtainedIrom

"i"Q=ffiA plot of Eq. 6.37 in Fig. 6. 12 shows that for ellipsoidal heads with a/, rarios

over 1.4, the hoop stress at d = 90'is in compression. The curves indicate thatthis compressive force increases as the head gets shallower. Design of headsbased on these high compressive membrane forces iends to give ulha-conservative answers. This is because discontinuity forces tend to lower themaximum compressive sFess which results in more realistic desims. The ASMECode uses such an approach in the design of elliptic and torisfherical heads.

Example 6.6. A2; I ellipsoidal head is subjected to an intemal pressure of100 psi. If a = 48 in. and r = 0.5 in., detemine the hoop and meridional stressat6=9A'.

Sol.ntion. With d : 90', Eq. 6.37 becomes

nr=t

= ryEq = 24oo lb/in.

%=r# = 48oo psi

,j

,1'"(i.{|,(tl -, - *-y, - *,(t)

I

Page 93: Process Equipment

166 ANATYSIS OF TORMED HEADS AND TRANSITION STCTIONS

elozlq

Similarly,

h/.Fis'rr€ 6.12

No=+(2br-ar)zo-/lno.|r4Rl

= -ffitz x 24, _ 482)

: -4800 lb/in.

- 4Rfno' = -(rf = -9600 psi I

and

6.3 TORISPHTRICAI. HEADS 167

6.3 TORISPHERICALHEADS

In formulating the discontinuity equations for torispherical heads at the cylinderjunction, two assumptions must be made. First, the ratio a// must be over 30.Second, all deflections dissipate rapidly away from the junction. With these twoassumptions (known as Geckeler's approximations), the discontinuity analysisof a torispherical head near a cylinder junction is similar to that for a cylindricalshell. Hence, the governing equations are (see Section 5.2.1)

-! + 4Baw : O (6.38)

where

B=

Equation 6.38 is similar to Eq. 5.21 for cylindrical shells except that in Eq.6.38 the quantity p is a function of 12 that is variable along the meridian. Thisrequires numerical integration of all moment, force, deflection, and slope ex-pressions at angles less than @ : 9g'.

If a discontinuity force is applied at the edge as shown in Fig. 6. 13, Eq. 6.3gyields the following values.3

.:#rru,n,-FoB^Md.

u, : 7, : z1,f;c ^oo

- FoBp,Mo)

n = Gr"^n, + zBoDe,Mi (6 3e)

*r=ffi<-oupo+ Ap"Mo)

Me = t&10

Fisuro 6.13

Page 94: Process Equipment

I6E ANATYIIT OI IORMTD HTADS AND TRANSITION STCTIONS

whcrc AA = ., rr'(cos ps + sin Bs)

Be, = e &(cos Bs - sin Bs)

Cs = s-8" t.,t PDp" = a-Fs rin B"

.Rt - u\rh= \l--a-p = poisson's ratio

6.4 CONICAL HEADS

The sfress distribution in a conical head can be obtained from Eqs.6.11. From Fig. 6.14 with d constant,

r=ssind/t=o

12= stard

Redefining N4 as N, and p4 as p", Eq. 6.10 becomes

and Eq. 6.l1 becomes

Na : p,s tan d

rv" = + I ,0,- o,tan d)r dr

6. l0 and

(6.40)

Fisure 6.1,{ 2 cos c!

6.4 CON|CAT HEADS t69

The forces and deflections obtained from Eq. 6.40 due to some typical loadingconditions are shown in Table 6.3.

Exampfe 6.7. A conical shell with d : 45" and base diamerer of g ft issubjected to an intemal pressure P Find the expressions for N6 and N".

Solutinn. For intemal pressure, N" : 0 and lr'e = p. Therefore, from Eq.6.40,

Ne : Ps tan 6r

p-

cos a

P .2N"=;*d,;+c

s=0 N"=0

(1)

Also

at

Hence

and

c= 0

Ps tan a'

PrlV":;-: ,zcosa

6,4,1 Unbolonced Forces ot Cone-to-Cylinder Junction

Thejunction of cones-to-cylinders must always be considered as part of the conedesign because of the large stresses that occur there. By referring to Fig. 6.15,the force 1{, at point 0 was found in Example 6.7 to be

I

PR

Page 95: Process Equipment

6.4 CONICAT HEADS t7l

(b)

Figure 6.15

Sumrnation of vertical forces at point 0 gives

2zrRV = PnR2

or

V =PR2

Since V is the resultant of components N" and A, it follows that 11 is an inwardforce with magnitude

.. PR t^n d,= 2

I

I

od

d -o\nP

d o I at4(J NI

. 6t .t. Etro , Fr olsrA AI AI

^ r--:---r:+! ilN

!

'IR

itlloE - Ol

v; -l t 3l6

oldIE N I

- - ;lo ;l .l olpo ol olN olq 'l't *" a,

""1-

a f' drN

-3"i

| -o r:JI ld d -

I (/lla o - ot-oN | .1.^ u ltldd old alN o olN(JI I E OIFc tF Qtia . lo) ilo N le Ull

of | 6 | . , tP

^" ? | ".liz@@Fo

+

t

d.

o

o

oI

o

olt

oooop

-o

(irlt

oF

170

Page 96: Process Equipment

172 ANALYSI3 O' TORM!O HIAOS AND TRANSITION SCCTIONS

This tbrce H must bc resisted by ring action at the junction The required area

of the ring is given by

PR2 tairr a' (6.41)

where A : required ring area

P : intemal pressure

R = radius at base of cone

o' = one-half the apex angle

o : allowable compressive stress of ring

Example 6.8. What is the required area of the compression ring at the cone-

to-cylinder junction in Example 6.7? Let P : 20 psi and the allowable stress inthe ring 10,000 psi.

Solution. From Eq. 6.41,

20x48'?x1.002 x 10,000

= 2.3O in2 .

6.4.2 Discontinuity AnolYsis

The derivation of the discontinuity expressions for conical shells is similar to that

for cylinders. The resulting moment and force equations for conical shells are

expressed in the more complicated Bessel function terms. However, approxi-

mate solutions for various edge loading conditions can be expressed in simple

form as shown in Table 6.4. In this table,

.HR(f

2o

I

^tIJ='-,' srn 4)

-

o==

ts

+

Nl@l x xNll-l

ttN->l *'l * e-NI

=I

9cl .-l € =.._:- 61 ,-

ol 4. ol @IE

' lo -l!o,lNN l@tl.{

=

i-:-r

I .\r

l-->+

qI

F^ x Fl+

o

o

.olt @l to .l 0,

I NIS'tN !l IN--> N | -_>

=cg6:

=11.o *.

173

Page 97: Process Equipment

t74 ANAIYSIS Of fORMEO HEADS AND TRANSITION STCTIONS

I

Figure 6.16

ExamDle 6.9. Calcuiate the maximum longitudinal and circumferential

*"r... i" the cylinder shown in Fig 6' 16 due to intemal pressure P

Solution. From Fig' 6.16

f+F:H (1)

where from Section 6.4.1,

Pr tan a'

'l'he deflection compatibility between the cylinder and cone is given by

dclloction of cylinder at junction due to M and /

: deflection of cone at junction due to M and F (2)

Sirrrilutly,

r()trti()n ol cylinder at junction due to M and/

= rotation of cone at junction due to M and F (3)

llsirrl f rrlrlcs 5.2and6.4 and solving Eqs 1,2, and3 result in the following

6.4 CONICAT HEAD5 t/5

exprcssrons:

where

f:HuF:H(1 -U)

/r\M: HIiIVZ\p/

H: Pr lan d'2

cos2 o'(3 * cos2 c')i + cos'zc'(6 + cos2 a')

_.uvz=o*"o"2"';

The maximum longitudinal stress due to M and pressure is expressed as

* : ?(t t - 4 sss v,,,4 "" "')

whereasthemaximumcircumferentialstressduetoMandpressureisgivenby

6.4.3 Cones under Exlernol Pressure

The solution of the buckling of a conical section subjected to external hydrostatic

oressure is normally obtained by energy methods The resultant equation is very

ffi;;#ili; the iterativi prociis needed for lhe solution s Experimental

,"."-"ft "o-paring

the buckling equations of conical and cylindrrcal shells has

.iro*oiftut tfti, U*lling of a conicai shell is similar to the buckling of cylindrical

r-n"fi.-*ift "

length eq-ual to the slant length of the cone and a radius equal to

,h" un"aog" radiris of curvature of the cone Research has also shown that the

qr""tiiy O - Dr/Dr) has a significant influence on the buckling of a cone'

Page 98: Process Equipment

176 ANAI.YSIS OF fORMtD HTADS AND TRANSITION SICTIONS

Accortlingly, thc buckling oquitti(n ol a cono citrl bc cxpresscd as

*,:"('-';)

where p is the modified buckling equation of a cylindrical

f(l - DtlD) is a function of Drf Dz.

A simplified equation for the buckling of a cylindrical shell" is

p 2.42E (t /2r)25=6_EfnlL/r,-o.4sen84

shell and

(6.42)

For most applications, the second quantity in the bracketed denominator is small

compared with the first one and can thus be neglected' Based on this, the

buckling equation of a cone (Fig. 6.17). may be wrinen as

4, _ 2.6(cos a')25(r)15./, _ 4\E tl1,Dt-rDtl21'5rU or/

!V"'

Fisure 6.17,. : T (' * noq)

= 24 3't5 in.

6,4 CONTCAT HEADS 177

'Ihc magnitude ofthe tunctionl(l - Dtf D) canbe deternrined thetlrctically

Based on this plus the "scatter" band of experimental data, a value of l 0 was

used for the function at Dr/D2 of 1.0 (cylinder). The function changes linearly

to a value of 0.8 for DtfDz of zero (full cone). Thus the buckling equation

becomes

p

ti

The second bracketed expression can be approximated by the quantity

2

r+ND,

Using a factor of safety (FS), the allowable external pressure on a cone is given

by

P, - 2.6(t"/D2)25

E (FS)(Le/Dz)

P. = allowable external pressure

E : modulus of elasticity

t"=tcosd7"=11/2)(t + Dt/D2)

Dl : diameter at small end of cone

D2 : diameter at large end of cone

(6.43)

Example 6.10, Design the cone shown in Fig. 6.18 for an extemal pressure

of 15 osi. Let FS = 4.0 and E = 30 x 166 psi.

Solutinn. a' = 30.96" and cos a' : 0.858.

Page 99: Process Equipment

I70 ANATYSIS OT FORMED HEAOS ANO TRANSITION SICTIONS

From Eq. 6.43,

,": o,(wo-1a,ly'

=,,(u?,#i:,'*i"l': 0.20 in.

I : """""""': : U.zJ ln.cos a'

and

I

NOMENCTATURE

a : major radius of ellipse

b : minor radius of ellipse

lt:Et3/12(l-ttz)/)r : diameter at small end of cone

D r =60"

Fisur€ 6.1S

NOMENCI.ATURE

/)z = diameter at large end of cone

C : modulus of elasticity

L = axial length of cylinder

L":(h/2)(1 +Dt/D2)

/ = axial length of cone

l' : slanted length of cone

M = bending moment in hoop direction

M = bending moment in meridional direction

N, = axial force in cone

N = force in hoop direction

N = force in meridional direction

P : pressure

P" = allowable extemal pressure

4 = intemal pressure

P, : external pressure

P, = radial pressure

P" = axial pressure in cone

P = meridional pressure

Q : shearing force in head

r : radius

rr = radius of curvature as deflned in Fig. 6.4

12 = radius of curvature measured from axis of symmetry

4 = inside radius

r, : outside radius

s = distance along the slanted length of cone, measured from apex

? = temperature

t : thickness

t" = tcos a'v = axial deformation

w : radial deformation

179

Page 100: Process Equipment

I8O ANATYSIS OT IORMED HEADS ANO TRANSITION STCTIONS

* coellicient ol thcfl)lal oxpansion

= one-half the apex angle of a cone

a

a

e=w for cylinders

for cones

7 =7r/2-Q6 = deflection measured perpendicular to axis of symmetry

A : rotation

^ =\yto=-6i/Fp = poisson's ratio

o = stress

o- = critical buckling stress

o, : radial stress

.r, = longitudinal stess in cone

od = hoop stress

od : meridional sfess

S = angle as defined in Fig. 6.4

R,EFERENCES

Gibson, L E., Linear Elastic Theory of Thin SherrJ, Pergamon Press, New York, 1965.

von Kaman, T. and Hsue-Shen Tsien, "The Buckling of Spherical Shells by ExtemalP.essue" in Ptessure Vessel and Piping Detign: Collected Papers 197-1959, AfieicanSociety of Mechanical Engineers, New York, 1960.

Coates. W. M., '"The Stale of Shess in Full Heads of Pressure Vessels" in PressureVessel anlPiping Design: Collected Papers 1927-1959, American Society of Mechanical Engineers,New York. 1960

Baker, E. H. et al., Srell Arnlysis Manual, NASA CR-912, National Aelonautics and SpaceAdminisb"ation. Washingto!, D.C., 1968.

Jawad, M. H., "Design of Conical Shells Under Extemal Loads," Jounal of Pressure VesselTechnology, Vol. lO2, 1979.

R^etz, R. Y., An Experimental Investigarton of the Strength of Small-Scale Conical ReducerSections Between Cylindrical Shells under Extenal Hydrostatic Pressure, V. S. Department ofthe Navy, David Taylor Model Basin, Report 1187, February 1959.

t.

BIBTIOGRAPHY I8I

BIELIOGRAPHY

Bilfington, D. P., Thin Shell Conctete Structures, Mcclaw-Hill, New York, 1965.

Flugge, W,, Stresses in Shells, Springer-Verlag. New York, 1967.

Timoshenko, S., and S. Woinowsky-Kieger, Theory of Plates and Shells, McGraw-Hill, NewYo*, 1959.

Page 101: Process Equipment

I

CHAPTE R7STRESS IN FLAT PLATES

V'nnn^ flot plote3. (Court$y of lhe Nooier CorPorotion, Sr' Louis, Mo )

t83

Page 102: Process Equipment

l8.l 3TR!SS lN fLAT ptATrS

7.1 INTRODUCTION

lli:4gl * very common in grgcesl .quiq-"nt.Qiqrgql

such areas as nozzle covers, bulk heads, ani tuUesilOets, Ttrereasru\,rr .ucas .ts rozztc covers, DulK neads, and tubesheets, -whereas rcefanCularglles.are used as segnrylq! trays, baffles, and in rectangulir'p."rGffi;i;.This chapter presenB-6rieTdescription of the theoretical iackground of circularand rggjqggkUllates.

The theory of symmetric bending of laterally loaded plates is generally basedon the following assumptions:

l. Thickness of plates is significantly smaller than the least lateral dimen-sion of the plate.

2. Loads are applied perpendicular to the middle surface of the plate.3. No forces are imposed in the middle surface.4. Lines perpendicular to the middle surface before deformatron remain

perpendicular to the deformed middle surface.5. These lines are inexlensible.6. These lines remain straight lines.

These assumptions form the basis for developing the bending theory of platesand apply to plales where buckiing is not a consideration.

7.2 CIRCULAR PLATES

The relationship between the radius of curvature and the deflection of a circularplate is obtained from Eq. 3.6 as

1 d,2w

;= 77or in terms of the terminology of Fig. 7.1,

! =d2w : -dQrn dx,2 dr (7 .t)

'fhc second radius of curvature is also obtained from Fig. 7.1. Line,4g is them(lius of curvature r, of all points at a distance r forming a cone:

sind-at=I

Using the sign convention that clockwise angles and moments are positive and

7.2 CIRCUI.AR PI.ATES t85

downward deflections are positive, the relationship becomes

6 1dwfr f rdr

The moment-curvature relationship is based on Eq. 3.11 and is given by

Substituting Eqs. 7.1 and 7.2 into this expression gives

M,: -D(+ * L+\\4r- r dr./

= D(!+ * *9\\/ dr r/

(7.2)

(7 .3a)

(7.3b)

Sinilarly,

M,: -D(!+ * p+\\r ar dr/

= -o(9 *

Fisure 7.1

1 1\- -r p-l

dd\p-, Iar/

(7.4)

Page 103: Process Equipment

t86 STRESS tN r[AT ptAnS

For a unilorrnly bodcd platc, thc tbrces acting on an clement are shown inFig. 1.2u. Taking moments uboul a-n gives

(M,r d0) - (". - ff*)<, + dr) d0 + z(u, a,.t) - " *(i)

/ )n \ /,{.\-lO + 7 drl\r + dr) dol+l = o

\ 4r / \z/(7 .s)

Ttle qvant\ty Mt dr d@/2 is the component of M, perpendicular to axis d to a as

shown in Fig. 7.2b.Disregarding higher-order terms, Eq. 7.5 can be reduced to

M,+#r-M,'rQr:0

(b)

tiswe 7.2

(1 .6)

(Mr1!!r

(o+5F dr)

7.2 CIRCUTAR PTATES

Substituting Eqs. 7.3 and 7.4 into 7.6 gives

d1w I d2w 1dw O_--=:drr r dr2 12 dr D

or

dlrdld,/,)\1 O-:-|_-|r-||:=drlr dr\ dr / I D

Similarly, substituting Eqs. 7.3 and 7.4 into Eq. 7.6 gives

d20,ldo o -oa*-;ar-7: D

187

Equations 7 .7 and 7 -t are the basis differential equations for the bending ofcircular plates due to symmetric loading. Equation 7.7 can also be written interm of the local load as

(7.7)

(7.8)

(7.e)

Once w is determined from Eqs. 7.7, then the moments are obtained from Eqs.7 .3 arrd 7.4. The shearing force is determined from Eq. 7.6, and is exDressedas

o: D(+.!+ - \+\\ dr- r ar- r'ar/ (7.10)

Example 7.1. Derive the moment expression for a uniformly loaded, simplysupported circular plate of radius a. For g, : 0.3, plot the moment diagram anddetermine the maximum deflection. rotation. and stress values.

Solution. From Fig. 7 .3, the sheat Q at any radius r is givenby 2mQ : nnz Por

l,lii,rr1= -g

I d [,d l! d (,a\.ll = cr drl drlr dr\ dr/l) D

Pr

Page 104: Process Equipment

188 STRlSl lN rtAT PLATIS

Fisure 7.3

Therefore, from Eq. 7.7,

dltdldw\l Prd,l;E( d, ) ): b

Integrating both sides gives

dl dw\ Prl ^d,\' d,)

:5 - '"A second integration gives the expression for the slope that is given by

^ dw Pr3 Crr Cz-drl6D2r

and the third integration gives the deflection w as

Pr4 C,rzw:_L+++C2lnr+,C,64D4-

(1)

At the center of the plate, r = 0 and the slope is zero due to symmetry. Hence,liom liq. l, f,2: Q.

At r : a, moment M, = 0 and Eg. 7.3 gives

Cr: Paz /3 + u\-8D\l+,,/

At r a, thc deflection is zero and Eq. 2 gives

,,=#(T#-')

7,2 CIRCUI.AR PI.ATES

Hence, the deflection as expressed by Eq. 2 becomes

Pra r2 13 + p\ Pa2 Paa /6 + Zu \r4':_ t_!_t _llsD 4\l+prl8D 64D\t+p 'lor

o '15+u '\w: -)-(az - ,tll'; :, * .a2 - r2lUD'- \l+p Iand

^ dw Pr(, 3+p,.\- dr l6D\' l+p')

The maximum deflection occurs in the middle where r = 0. Hence

Paa /5 + p,\ Pa4 15 + u\ 12(l - 42tnj*, =_t | = _t ____________:_ | ,

64D\t + pl 64 \r + p/ Et3

andwithp=0.30

"'-"" - o'696!aq,

Et3

The maximum rotation occurs at the edge where r = d. Hence,

^ -Pat -3^, (l - rr)d'- = 8r,(r + p) : tP"' -i

and with /.r = 0.30

s^^= -t.os EtY

The moment expression is obtained by substituting Eq. 3 into Eqs. 7.3 and7 .4. Hence

,,=*rt + 1t)(a2 - 12)

u, = ftbt{z + p.) - r2(1 + 3p.)l

t89

(3)

(4)

(s)

(6)

Page 105: Process Equipment

r90 tliltt rN trAT PtATtt

A plot of Eqs. 5 and 6 for g. = 0.3 is shown in Fig. 7.4. The plot indicat€s thatthe maximum moment occurs in the center and is given by

M*=3#

6M l.24Pa2T- I-

Example 7,2. Derive the moment expression for a uniformly loaded circularplate of radius a that is fixed at the edge. For trr, = 0.3 plot the moment diagamand determine the maximum deflection and stress values.

Solution. From Example I,

Pr4 Ctz ^ ,.:64D- -T-- Lz lll / -f L:

2n

{{'o

00

I'h

Figoro 7.4 Momeni diltriburion for simply suppord plolo.

I

(l)

lt.

and

7.2 CIRCUTAR PTATIS t9l

(2)

At the center of the plate r = 0 and the slope is zero due to symmetry. Hence,from Eq. (2), C, = 0.

At r = a, the slope is zero and from Eq. 2,

-Pa2Cr=

Also at r = a, the deflection is zero and from Eq. l,

Ct:6

Hence, Eq. 1 becomes

pra pa2r2 paa

64D 32D 64D

= L1^z - 'z1zuD'"The maximum value of deflection occurs at / = 0.

- Pr3 C,r C,H=-+-+i-l6D2r

u,: f,bT + p) - r2(3 + tL)l

u, = llt tt + tLt - 121t + 3p))

8D

(3)

Paa Pa4 l2(l - tr-z)w=-'64D&

and for P = 0.3,

r,v.*=0.171r9)\Lt" /

The moment expression is obtained by substituting Eq. 3 into Eqs. 7.3 and7.4. Hence,

(4)

and

(s)

Page 106: Process Equipment

tt2 $iltt tlit llaT ptATtt

l.flgure 7.5 ,nom€nt didrihtion tor f,or ft(€d plote.

A plot of Eqs. 4 and 5 for p = 0.3 is shown in Fig. 7.5. The plot indicates tlntthe maximum moment occurs at the edge and is given by

-PazM,*"=

6M -0.7 SPazo*,=v_---v-

Problems

7.1 Determine the maximum deflection, slope, and bending moment for asimply supported plate subjected to edge moment Me.

16tlffi

and

T

.,.

7.3

7.3 RTCTANOUTAR PrAlt3 t9g

^ azMnAnsweri mo( lr = # at centerzD\t + l.L)

^ aM"max 0 = -_ft

at edgeu\r 'f p)

max M, = Mo throughout plate

m^x M, = Mo throughout plate

A ctcular plate is fixed at the edge and is at an ambient temperature of70T. What is the maximum stess if the top surface is heated to alemperature of l70T and the bottom surface is cooled to a temperature of-30T?kta = 9 x 10-6 in./in. T,r:0.5in.,a:60in.,8:30 xlffpsi,p=9.3.

. aLTEanswer. o =n _ 1.,

= 38,600 psi

Determine the maximum moment in the circular plate shown in Fig. 7.6if a = 4 ir., b = 2 in., p : 0.3, and P : 100 psi.

Answerz M' : 384.6 in.-lb/in.

Fieur. 7.6

7.3 RECTANGULAR PTATES

In developing the differential equation for circular plaies, the shearing shess wasignore.d because the load was symmetric with respect to 0. In rectangular platesunder uniform loads, the shearing stress interacts with the normal shesses in the.r- and y-directions and thus cannot be ignored. This results in a more compli-cated differential e4uation than that for circular plates. In addition, the solutionof th€ differential equation of rectangular plates is more elaborate and involvesthe use of Fourier series. Because of this, only the case of a simply supported

Page 107: Process Equipment

Ifi lnl$ il ftAT ftATtt

rrctangulsr plate loadcd throughout its surface is discussed here. Nonsymmetricloadings and boundary conditions other than simply supponed result in quitecomplicated solutions that are beyond the scope of this book. The examplesgiven in this section are intended to give the reader a concept of the generalbehavior of rectangular plates and the difference between them and circularplates.

If an infinitesimal section is removed from a rectangular plate, the forcesacting on it will occur as shown in Fig. 7.7. Summation of forces in the z-axissrves

q(x, y)dx dy - Q, dy + Qt dx +

This equation can be reduced to

(a. ft,,)*=0

(a.. ff *)', -

q(x,yt+#.#=, (7 .1,r)

Summing mornents around the "r-axis and deleting all quantities of higher ordergives

m, *$$o'

Figwe 7.7

7.3 RKTANOUTAR PIAT!3 19!

W-+-Q'y=o (7.12)

(7 .t3\

(7.t4)

(7.15)

(7.16)

(7.18a)

(7.18b)

(7.18c)

dQ" =

d,g _ atu,dy dy- dxdy

Similarly, summing moments around the y-axis and deleting all quantities ofhigher order gives

#.ry-e"=odo, d2M, azM,,ar-: d* - atfr

Substituting Eqs. 7 .13 andT .15 into7.1l and using M"t = -MofromEq.3.1lgives

, d,M, 2d2M* a2M,q\x, y,-r -;z - -;i + ir, = u

The differential equation relating deflections and applied loads is obtained bysubstituting Eq. 3.11 into 7.16 and obtaining

daw 2daw 1aw ak. v\

-

-l-

-

-t

-

: :-:---:--:-:-ax4 dx2dy2 dy4 D

(7 .17)

which is the differential equation of the bending of a rectangular plate subjectedto lateral loads.

For any grven loading and boundary conditions, the deflection p can beobtained frorn Eq. 7.17. Tlie bending.moments can then be determined ftorn Eq.3.1I as

".: _,(#. _?)

^: -'(#.,#)

u* = o !-'Y^' dxdy

Page 108: Process Equipment

Itc filttt tt{ il.tT tta?tl

and tho shcarfng forccs Q, and p, arc determined from Eqs .7 ,12,7 .14, and3.lla8

n.- -,*(#.?)

"= -,&(#.?)

Example 7.3. Detennine the maximum moment in a simply suppofied rectan-gular plate of length a and width D if the applied load is expressed as

q = qssinTF*T)

I*t a = 6O in., b : 25 h., eo = 3psi, and p = 0.3.

Sohttian, Assume y to be of the form

w=C txl rrY\rr;\rr 7/This expression satisfies the boundary conditions of w = O and M : 0 at all fouredges. Substituting this expression into Eq. 7.17 gives

r-= 4o" Dr4(1/ az + l/b\2

and the deflection expression becomes

w : DFn# +Ilbry't # ('* ?)Substituting this expression into Eqs. 7.18, gives

,,= aOffilnG,. *) sinr sin|

u = Qo /.]|l ..,- -t \ ^'- Tx -,- n!'""

: }(FaI7FfV-j - F) sln - srn ,M,:dffi"*Y"o"|

Thc maximum value of M, and M, occur when .r = a/2 and y = b/2. A

(7. l9a)

(7.19b)

7.4 CIRCUIAR PIATIS ON IIASTIC IOUNDATION I97

comparison of the denominator in parentheses in the expressions for M, and M,indicates that M) will always give a larger value of M for the given values of aand b. Accordingly, the maximum value ofM is given by

M*=atrffitm@.*)M^."==,?'o,==fq!*a\

1r2(1/ffi2 + | /25\2\602' 252f

= 145.1 in.lb/in.

The maximum value of M,o occurs when.r = 0 and y = 0 or r. Hence, themaximum valae of M, is given by

M,r3.0(0.7)

12(1/602 + r/25r,6q25)= 40.2 in.lb/in. I

7.4 CIRCUIAR PLATES ON ETASTIC FOUNDATION

Many tubesheets of heat exchangers are designed as plates on elastic foundationas discussed in Chapter 14. The solution of the differential equation of a plateon elastic foundation involves Bessel functions. The four Bessel functions usedin this section are

- t -l)ix4iZ@) = 6sr1r1 = >. *, -?"7'[(2])ll''- (x/2\o (x/2\8 (x/2\t2=t-E--+o. 61, -"'

S. (-1\jx4j'Ll\xt = Det\x) = 47W* ,X

_ (x/2)2 , (x/2)6 (r/2)'o- --l?---L- -f?-- "'23ft) = _ ? *"r(,) =

t+ _ 1lr, * r^i . a<.t]

z1i = ar.,k) =z+ .1lr, * ,"5.t,<,t]

Page 109: Process Equipment

r9r ltiltt ll{ fLaT ptATll

whcrc

" = /lY - 99/rY * 4(?1r\" - . . . .

" - \z) 31'z \2) 51'? \2),, _ 4{z\ (x\ _ d(4) /.rY _r d(6) /r\u + . . . .h:-';-\1) --+r\1) -?tr\r/ - "

I I l*.......*lQ\n)= t*t*1-z "

"t = 0.577216

The limits of the Z functions as 'r --> 0 and as x :+ co are given in Table 7' 1'

The table also shows the limits for the first derivatives of Zt tltroryh Zq.

The relations between the various derivatives of the Z functions are as fol-lows:

Toble 7.1 Limits of Zfunctions

FunctionLimit as

.r ---+ 0Limit as

Z{x)

z2@)

h6)

h(x)

&(x)dx

il.(x)dx

&'(x)

1.0

_x2--7-

0.5

2t^+

-x'-:7lo

-xzx, yx-Itr=

2

nx

dx

E+(x)dx

f cos K

-f sin K

r, sin rl,

-z cos ry'

1fu(cosr-sinr)

;!(cosr+sinr)

ft@osi,- sinrli

1fu(cosg+sin0.1xI =:eXD""'=' !2tx - !2

xnv86

,t, = j- +i'v26

7.4 C|RCUIAR PtAftS ON ltAgTrC TOUNDATTON t99

d2z,k) | EtG)Zzlx) - - ---jax- x a.x

dzz2\x) 1 fl,2@)-----:--;-=-zt\x)-- ,ax- x ax

d'zA(x) lfi,l?)----=-- = L4\x) - - -'--:-dx' x dx

d2z4@) | dZlx)-----:--t-=-23\r)-- ,ax- x ax

The force exerted by an elastic foundation on a ciruclar plate due to deflectionof the foundation is expressed as

P=Kow

where p = foundation load

w = deflection of foundation

Ko = stiffness of foundation

: modulus of elasticity of foundatior/depth of foundation.

The differential equation of a circular plate on an elastic foundation can beobtained by modifying Eq. 7 .7 as

i,lli,(,#)l=ryThe solution of this equation is expressed as

(7.19)

w = Cfl(ar) 'f C2Z2@r) * C3Z3(ar) i CaZa@r)

where ": ^{EJD21 - Za : Bessel functions

Ct - Qa : constants of integration

Example 7.4. Detemfne the maximum deflection in a circular plate on anelastic foundation subjected to a concentrated load F in the center of the plate.

Solution. From Table 7.1 it is seen that as r approaches infinity, Z and Zz alsoapproach infinity. Therefore, Ct and C2 must be set to zero. Thus

w:CtZt(ar)iCaZa(ar\

Page 110: Process Equipment

100 tTmll rt{ tuT ptaTtt

and

0 = + = Ct a Zi@r) + Ca a Zi@r)-dr

As r atrrproaches zero, 0 must be zero due to symmetry. But from Table 7. l, Ziapproaches infinity as r approaches zero. Hence, Ca must be set to zero. Thus

w = CzZz(ar)

dw* = CtaZS@r)

d2w ^.f I Ijj=c*'lzo{or)--zi@nld3w ^"f I I7j - Aa'zlozi@r\ -:zKar)]

Substituting these derivatives into Eq. 7.10 and equating this to F' gives

^F4azD

' =

'fi6t'<*>

and

and

F8rr2D

NOMENCI-ATURE

Et3;:;:----------;:tz\t - p-)'

= modulus of elasticity

= stiffness of foundation= modulus of elasticity of foundation/depth of foundation

= radial moment in circular plates

E

Kq

M,

UEUOORAPHY 201

Mt = tangential moment in circular plates

M, = moment in .r-direction of rectangular plates

My = moment in y-direction of rectangular plates

M,r = shearing moment

P = applied pressure

O = Shearing force

applied load

r = radius

T = temperature

t = thickness

w = deflection

21 to Za = Bessel functions

a = */EJDpoisson's ratio

REFERENCE

l. Tiomoohenko, S., and S. Woircwsky-l<liege\ Theory of phtes and Shelts, McGmw-Hill,New Yort, 1959.

BIBTIOGRAPHY

Hetenyr,M., Beams on Etastic Foandation, University of Michigan Pr€ss. Atrn Arbor, Michigan,1964.

McFarland, D, E., Smith, B, L,, aDd Bernhan, W. D., Analyris of plates, Spaftan Books, NewYork, 1972.

Szilard, R., Theory and Awlysis of Prorer, hedice-Hall, Englewood Cliffs, {.J., 1974.

Page 111: Process Equipment

PART3DESIGN OF

COMPONENTS

203

Page 112: Process Equipment

CHAPTER 8DESIGN OF

CYLINDRICAL SHELLS

2052tJ4

a,' ,'l,rrrr-n rower used by o ferlilizer monufocturer' (Courtesv of lhe Nooter CorPorolion' St tot,,is' Mo )

X

Page 113: Process Equipment

206 DlgloN or cyuNDRrcAr. sHEr.rs

Cylindricul vcsscls ure very liequently used in the petrochemical industry. Theya.re easy to fabricate and install and economical to maintain. The requiredthickness is generally controlled by intemal pressure, although in some instancesapplied loads and extemal pressure have control. Other factors such as thermalstress and discontinuity forces may also influence the required thickness.

8.I ASME DESIGN EQUATIONS

A simplified equation was developed by the ASME Code, Vltr-l, for deter-mining the required thickness of a cylinder subjected to intemal pressure. It isa simplification of Eq. 5.3 and gives accurate results over a wide range of r2/r1.This equation is expressed as

(8.1)PR

where t: required thickness

P = inlemal pressure

R = inside radius

S = allowable stress

E : joint efficiency factor

sE - 0.6P

A comparison of Eqs. 8.1 and 5.9 is shown in Fig. 5.6. It indicates the widerange of applicability of Eq. 8.1. The ASME Code, Vltr-l, has, however,limited the use of Eq. 8.1 to t less than or equal toR/2 and pressure less or equalto 0.0385 S. Various forms of Eq. 8.1 are shown in Appendix I together withan altemate equation that expresses the thickness in terms of Re rather than R.

The factor E in Eq. 8.1 is an efficiency factor and its magnitude depends onthe extent of radio$aphy performed at the various seams of the cylinder. Appen-dix J illushates the effect of radiography of various seams on the values of E as

established by the ASME Code, VI[-l.In Section VIII, Division 2, of the ASME Code, the equation for required

thickness is based on the stress at an average radius. Hence,

^ P(R + t/2)t

PR

s - 0.5P(8.2)

8.I ASMI DESIGN EOUATIONS 207

As the pressure increases above 0.4 S, Division 2 uses plastic analysis (seeSection 15.l) to obtain

r =ftn/R+r\\Ri (8.3)

Example 8.1. A pressure vessel with an inside diameter of 50.0 in. is subjec-ted to an intemal pressure of 100 psi. Using an allowable stress of 17,500 psi,find the required thickness according to Section VIII, Division 1. Assume thatall circumferential and longitudinal seams are double-welded butt joints and arespot radiographed.

Solution. From Appendix J a value of, = 0.85 is obtained. From Eq. 8.1,

PRt=-=- SE - 0.6p

100 x 25

17,500x.85-0.6x100r = 0.17 in. I

Exarnple8.2. A seamless cylindrical shell with an outside diameter of 30.0 in.is butt-welded to seamless ellipsoidal heads. The circumferential seams are notx-rayed. Find the required shell thickness ifthe allowable stress is 15,000 psi andthe intemal design pressure is 250 psi. Use Section XIII, Division 1 rules.

Solutinn. From Appendix J, with a value ofE = 1.0 (seamless shell), allow-able circumferential stress must be reduced to 8070 since the circumferentialseams are not x-rayed.

From Appendix I, the required thickness equation in terms of outside radiusis given by

PR

SE + O.4P

250 x 15

(15,000 x 0.80)(1.0) + (0.4 x 250)

= 0.31 in.

Probhms

8.1 An ASME pressure vessel with an inside diameler of4 ft has a seamlessshell. The head{o-shell seams are partially radiographed. Find the re-

t

Page 114: Process Equipment

206 DtStON Of CYt"tNORrCAt" SHE|TS

quircd thickness il'thc alkrwablc stress is 20,()00 psi and the design prcs-sure i$ 2900 psi.

Answer: t: 3.81 in.

8.2 What is the maximum allowable pressure that can be applied to a cylindershell with an outside diameter of 6 ft, thickness 1.25 in., and an allowablestress of 17,500 psi? Let E : 0.85.

Answer: p = 524psi

8.2 EVATUATION OF DISCONTINUIW STRESSES

In Chapter 5 we showed how stresses are evaluated at different locations due tothermal and mechanical conditions. The magnitude of these stresses must bekept below a given allowable shess. This allowable stress is established in theASME Code, VIII-2. The designer has to establish first whether the stress is ata local or a gross shuctual discontinuity, as defined in Fig. 8.1. Next the stress

STRUCTURAL

DISCONTINUITY

GROSS STRUCTURAL

DISCONTINUITY

LOCAL STRUCTURAL

DISCONTINIJITY

A source of stress or stfainintensification which affectsa relatively lafge portion ofa s truc ture and has a

slgnlficant effec t on the

overall s tres s or strainpattern. Exahples of gross

structural d I sconti n ui ti es are

Icad-to-shel'l and flange-to-!hcll junctlohs, nozzles, and

.lunctions between shells of(llfferent d i ameters or

A source of stress or stralnintenslf{cation which a ffec ts a

relati v€ly small volune ofmat€rial and does not have a

significant effect on the overall

stress 0r strain pattern or on the

s truc ture as a l1lhole.

Flsuro 8.1 Slrucrurol Dirconlinuities (Coortesy ot tho Ameri.on Socisiy ol r.te.honicol Engineers,)

8.2 TVATUATION OF DISCONTINUITY STRISSIS

is categorized as a primary, secondary, or a peak stress as shown in Figs. 8.2and 8.3. In Fig. 8.4 is a description of the two categories of thermal stress. Oncethe stress categories are established, the stresses at a vessel's different locationscan be classified as in Table 8. l

Table 8.2 shows the allowable stress for various stress caiegories. Applicationof Table 8.2 to various stress categories is given in the following example.

Example 8.3. Calculate the stress at points A, B, and C of the vessel in Fig.8.5. LetR : 60 in., L= 2.0625 in., 11, = 1.9313 in., P : 500 psi, .S. =15,000 Psi, P = 0.3, Eo = 30 x 106 psi.

STRESS

CATEGORIES

PR II4ARY SECON DARY

A stress developed by the constraint

of a structure. Secondary stress isself-limiting, Local yieldinq and

minor distortions can satisfy the

condltlons l'hich cause the stress tooccur and failure fron one application

of the stress is not to be expected,

Examples of secondary stress are geheral

thermal stress and bendi ng stress at a

gross structural discontinuity.

Peak stress does not cause any noticeable distortion

and is objectlonable only as a possibl€ source of a

fatlgue crack or a brlttle fractufe. Examples of peak

stress ar€: I ) thernrl stress in austenitic steel

cladding of carbon steel vessels, 2) thermal stress

li the vrall of a vessel caused by a rigid change in

teFperature of the contalned fluid. 3) the stress at

a I ocal structural discontinuity.

Fisure 8.2 Str$s Colesories (Courr$y of rhe Americon So.iery of rvle€honicdl Ensineer3.)

Page 115: Process Equipment

2lo DtslGN of cYLlNDRlCAt SHtLLS

tRlt4ARY STRtSS

stress is not classlfied as a primary stress'

A stress developed by the lmposed loading

|lhich is necessary to satisfy the la$s of

equilibrium, The basic characteristic of

a primary stress is that it is not self_

limiting. Primary stresses |,lhich considerably

exceed the yield strength l,lill result in failure

or at least in gross dlstortlon. A therrial

BENDINGI'4E14BRANE

An exanple ls the bending

staess ln the central

portion of a flat head due

membrane sttess is the menbrane

stress in a Shell Produced bY

external loadr dnd monent at a

perFanent suppoft or at a

noz2le connection.

nn e*'ampte of a local PririarY

stress is one which is so

distributed ln the structure

that no fe-distributlon of'load occurs as a result of

yielding, An exaniPle is the

stress in a circular cYlinder

due to internal Pressure.

general prima rY membaane

Figure 8.3 Primory Slre$ Cotosoria3 (Courtelv of lt'e Ahericon Socisiv of M3€honicol Eneine€rs )

Solution

Point A. From Fig. 8'6 and Eqs. 5.9 and 5' 10,

oo = 14,300 Psi

o'=0Psior = 7150 Psi

The stress differences are

14,300 | psi

-7150 | psi

8.2 EVAI.UATION OF DISCONTINUITY STRESSES 2I I

or o = | -71501 psi

Hence, maximum stress = 14,300 psi. From Tables 8.1 and 8.2, the maximum

stress for a general primary membrane sffess is

S, : 15,000 psi > 14,300 Psi O.K

Point B. Frcm Fig. 8.7 and Eqs. 5.3 and 5.4'

ae : 14,800 psi

o., : -500 psi

or = 7150 psi

TIlE RI4AL STRESS

normally sho!ld under a chang€ in tefiperature.

A self-balancing stress produced by a non-uniform

distribution of tenperature or by differing thermal

coefficients of expansion. Thermal stress is developed

in a solid body whenever a volume of material is

prevented from assu'ning the si2e and shaPe that it

Local thermal stress uhich

is associated wi th almost

conpl ete suppression of the

differential expansion and

thus produces no significant

distortion. ExanPl es of

I ocal thefmal stresses a|"e:

I ) stress in a snall hot sPo

in a vessel v/al l.

2) the difference betl/leen th

actual stress and the

equlvalent I i near stress.

3) the thermal stress in a

cladding material.

General thermal stress is classified

as secondary stress. ExamPles of

general thermal stress are:

I ) stress produced bY an axial

tempera tufe distribution in

a cylindrical shell.

2) stress produced bY the

tempe rature dIf ference

betqeen a nozzle and the

shell to t,Jhich it is attached.

3) the equivalent linear stress

produced by the radial tenperature

distribution in a cylindrical shell

Figure 8.,{ Ihermdl Stress Cot€gori6 (Courr$y of lhe Aftericon Socierv of Mechdnicol Ensineers )

Page 116: Process Equipment

Tobb 0.1 Clorrlflcotlon of Slrun (Rrforrncr l)

0

o

a

a

o

{av. &dslull sclio.t

o

a

212

Tobb 8.2 Slreu Cotrgorlrr qnd Llmltr of Strcrr Intrnrlfy (Rrf l)

SirartEe.dlns

!o Pnhe.y or eR0n6.

-

U* &5iEn load3

---- Us op.aungloads lPr +P. +Q +F H s. ). , \-/

tt-I--,--.---t----*-1--1 | itP. F{ s.) I I i i :T\-/ | | | i I

I | | r-.+ - - -;.-r- /'\ I- --l- iI P. Hr.5 s,) llPr+PD+O+ rs. ) '-l- \__/ l---l- \__/ :L----T-------r i !

.- -r- /-\ r :

lP(-PD H1,5 s-) L__---*f ----.t

-

\--'l I

Fisure 8.5

213

Page 117: Process Equipment

2ta Dltloltl Of CYtlNoRlCAt 3H!rr3

.-....._"

Fisur.8.6

=._"a

n, oe

Figur€ 8.2

The stress differences are given by

r0_, = 115,3001 psi

4_r : l_2650lpsi6,_, = l-7650lpsi

Hence, the maximum shess = 15,300 psi, which is about 27o above the allow-able sffess of 15,000 psi.

- Point C . The discontinuity forces at point c are shown in Fig . g . g . From this

ngure,

8.2 EVATUATION OF DISCONTINUIW STRESSES

r'" = +e) - 500 x !'0-x-2 0625 = 7734 in lb/in'

Mt=M,+N,e=M,+7734

r, : 60 + '#:6l.olt3 in.

rh = 60 + +! = 60.5157 in.

B=

o, = ,^'.!o'1 ,, = o.so35Etz\t - p-)

215

Also,

3(1 - p') = 9.8465,,1h/

Fisure 8.8

Page 118: Process Equipment

216 Dt]Ot{ of cful{DflcAt 3H!U.3

Thc lirst cornputibility cquution is given by

defl€ction of shell = deflection of head

or

wo * wlsn ! wy" * wql^,"n"n: wp I w9 I wy1l6, **where for the shell

Pr? m2,987It'- =

-" Et, Es

N,e _ 366,454t*" = zB'o,= k47.3822M,."" : ___Eo _

''': 4- - 4r3'4s69Q. zp"D, Eo

and for the head

Prl . |,242.851we=EA\t - lt)= E"

*^ = 2'QrA - 1155.56650

' Eoh Eo

2Mhi2 188.o22M, t.454.162.ur: -EJo = E, r -E-Substituting these values into Eq. 1 gives

M' + r1.1563Q = -10,150.55 (2)

The second compatibility equation is obtained from

rotation in shell = rotation in head

or

0N*+ 0M" - 0ol.*.u : -Iun- Lal^rc"a

where for the shell

(l)

8.2 EVATUATION OF DISCONTINUIW 5TRE55IS

^ N,e 83,991aw"= D,= h^ r0.86M,ar, =

En

217

- 47.3822QEo

and for the head

^ 4A3Mh 6l.t86lM, . 473,213

E6t1r6 Es Es

^ zA,Q 188.022QO^= -' Eoh E,)

Substituting these values into Eq. 3 gives

M"+ 1'.9521Q= -7733.99

Solving Eqs. 2 and 4 gives

Q = -262'55 lb/in'

M' : -7221.47 in.-lblin.

Mr: 512.53 in.lb/in.

totaly = l$y

The actual forces are shown in Fig. 8.9.

o2p'D

0s:

(4)

(3)

Fisurs 8.9

Page 119: Process Equipment

2ll DlltoN of cYuNDRtcAt SHttts

noop sress ar point C =!3y:35,000psirs

axial stress at point C : ff : ZSOO psi

axial bending stress at point C : Y = 720 pri

circumferential bending stress at point C = 220 psi

These stresses are divided into two categories in accordance with Table g.2:

l. Local membrane stress (Pr)

o6 = 35,000 psi

o1 : 7500 psi

a, = -500 psi

maximum stress difference : 35,500 psi

From Tables 8.1 and 8.2 the maximum allowable local membrane stressis equal to

1.5S, = 22,599 < 35,500 psi overstressed

2. I-acal membrane plus secondary stress (pr + O)

a6 = 35,000 + 220 = 35,220 psi

ot = 7500 + 720 = 8220 psi

o;: -500+0 : -500 psi

maximum stress difference = 35,720 psi

From Tables 8.1 and 8.2 the maximum allowable local membrane olussecondary stress is equal to

3S. = 45,000 psi > 35,720 OK I8.3 ASME PROCEDURE FOR EXTERNAL PRESSURE DESIGN

A comparison of Figs . 5 . 1 7 and 5 . I 8 indicates that the buckling due to pressureapplied to sides and ends is more critical than the pressure applied to the endsonly. Accordingly, the ASME code, VIII, uses Eq. 5.17 as the basis for design.This equation is modified to take into consideration nonelastic bucklins and

8.3 ASM€ PROCEDURE FOR EXTERNAL PRTSSURE DTSIGN

cxpresses the basic relationship as

219

,,: + = i*'(L)'Defining A = e""

(8.4)

Equation 8.4 is plotted as shown in Fig. 8.10. Hence, for any given value ofL,D", and, t, a value ofA can be determined from Fig. 8.10.

The allowable compressive stress in the elastic region can be determined fromthe equation

AEo-FS

where FS is factor of safety and E6 is modulus of elasticity. Or in terms ofDressure

,2AEg

(D,/'XFS)

In the plastic region, ASME uses quasi-stresFstrain curves similar to those inFig. 8.11 to determine plastic buckling. These curves are plotted on log-loggraphs with a factor of safety of two for stress. Because the stress-strain curvesdiffer for different temperatures, a number of curves for different temperaturesare plotted in Fig. 8.11. Hence, allowable stress is given by

(factor I from chart)(factor of safety of chart)o=T (8.s)

or

2"8o=FS

If allowable pressure is needed, then

oe x/ tY^: a= ,1;"1

^ zto-D. 4tB

FS (D,)

Page 120: Process Equipment

8lolgv:l

$ 33933 BssFF e ?3s 3

g;a.>

E.nJR

- 5:.c fqfiAtt55c;.:.'-a9

E.E

- s 5Fq 9 fl-

; f :('+Tet.:J I'= bti;+;bEEE9

4 -Fo'd g9aE 8.i; !a

tl

-8 -6 -6

:l V5- 11-'t

\ \ \\

\

39PP9

:* R F R R

221220

II

II

i

g

-6

Ej

E

E

E

'6

I

E

daoE

5g

!""I .."

j6

Page 121: Process Equipment

olsloN oF cYt"rNDRrcAL sHEtrs

P : 4

----!-@"/t)FS

ASME uses a factor of safety of 3.0 for buckling of cylindrical shells subjectedto lateral and end extemal pressures. Hence, for elastic region (D./t > l0),

2AEo

3(D,/t)(8.6)

and for elastic or plastic region (D./t ;- lO),

P = .t4B,t3(D./t)

where A = factor determined from Fig. 8.10 and is equal to e",

B : factor determined from Fig. 8.11

D, : outside diameter of cylinder

Eq = modulus of elasticity

P = allowable extemal pressure

r : thickness of cylinder

For D,/t values less than 10, ASME uses a variable factor of safety that rangesfrom 3.0 for values of D"/t = 10 to a factor of safety of 2.0 for values ofD"/t = 4-O. This reduction occurs because for very thick cylinders, bucklingceases to be a consideration and the allowable values in tension and comoressionare about the same . Hence, for D"f t < 10 the allowable value of P is tfie lowerof the quantities Pr and Pz given below.

For D./t < lO,

^: (T# - 00833)'

^ 2ol. I \"= DJr\'- oJ,)

(8.7)

where o = two times the allowable stress in tension or 0.9 times the yieldstress of the material, whichever is less.

Note also that for values of D"/t < 4, the following equation can be used:

8.3 ASME PROCEDURI FOR EXTERNAI" PRESSURE DTSIGN 223

(E.lr )l.l

The ASME procedure for the design of cylindrical shells under extemalpressure is complicated because of the various parameters that must be consid-ered. A summary ofthe procedure is shown in Fig. 8. 12 as an aid to the designer.

Example 8.4. The length of a cylindrical shell is 15 ft, outside diameter l0 ft,and is constructed of carbon steel with minimum yield strength of 36,000 psi.The shell is subjected to an extemal pressure of 10 psi. Find (a) the requiredthickness using ASME factor of safety and (b) the required thickness using afactor of safety of 2.0.

Solution. (a) Assume

t : 6 rn.

Then

4:zzo L=1.2st '-- D.

From Fig. 8.10, factor A = 0.00018. From Fig. 8.11, modulus of elasticity arroom temperature is 29,000,000 psi. Hence, from Eq. 8.6

p _ (2x0.009_l-8..1!Z? x 106) : r0.9 psi o.K.(3)(32u)

A check is needed to ascertain that buckling is in the elastic rather than the plasticregion. FromFig.8.ll with A = 0.0018, a value of B:2600 psi is obiainedin the elastic region of the curve. Hence, the above solution ;f l0.g DSi isadequate.

ur.r:]in.6

(b) For a factor of safety 2.0, assume

4=38at

\D./t)'

t = 0.3125 in.

I

Then

Page 122: Process Equipment

Cd loulot. Oo/t

l. Oo./t, l..r Lhar 4 ?

o = idtrr" Aanft.t L 4 oolculolar L lo

l. L./Do gF.ot.r. thdr 50 ?

l. L./Do 1... ttrar O.O5 "

Coloulot.! A ad u..

E rt,r- not.rlol. ofi.r.i, vtLh A

Ext rrd eD..oi |ot.l.nE r€tir-. I lfltE lzchlol ls crd..cd B

I. A lo r.lght off oa .c61. ?

t. A to l.it, otfroO .col. ?

Ia Oo./t ar .lO ?

O.l.rmln 2Sl |fl.|-.St l. ol lor. l. ll..tr... fFon 9.$..c1| on C

I. 2Sl, < O.96U ?

I. Pol < Poa ?

Figure 8.12 The ASME method for daerminins moximum ollowobte oxternot pr€ssure on cvtinders.

224

From Fig. 8.11,

8.3 ASME PROCEDURE FOR EXTERNAI PRESSURE DESION 223

I.rom F'ig. 8. 10, factor A : 0.00014 and from Eq. 8.6

p : zAEo ASME factor of safety' 3(D"/t) specified factor of safety

_ 2(0.000t_41_ll?9 x 106 x 3.0

= 10.6 psi O.K.

Returning to Fig. 8.1 1 with A = 0.00014, it is seen that the value from the chartindicates an elastic behavior.

ur",:jin. rlo

Example 8.5. A cylindrical shell with length 18 ft and an outside diameler 6ft is constructed of carbon steel with a yield stress of 38,000 psi. Determine thethickness needed to resist an external pressure of 300 psi.

Solution. I€t r = 1.25 in.

L: z.o 4: st.oD.t

From Fig. 8.10, factor A : 0.00095. From Eq. 8.6 with Eo :29 x 106 psi,

2x0.00095x29x106p3 x 57.6 = 320 psi

Now check for plastic region. From Fig. 8.11, factor B : 12,000 psi in theplastic region. Hence, the first of Eq. 8.6 cannot be used. From the second ofEq.8.6,

P-4x12'oon,: 3x57n = 278 psi inadequare

Try r: 1.375 in. Then

!=sr.o and A:o.oo11

Page 123: Process Equipment

226 Dl3tON Of CYUNDR|CAL SHEttS

lJ = 12,400 psi

dx It donP: '=^:" = 316 psi O.K.' 3 x 52.4

Use r = 1.375 in. IProblems

8.3 The thickness of a l3-ft diameter reactor is 5.50 in. and its effective lenethis l8 ft. Ifthe design temperature is 900'F, what is the maximum allowa6leexternal pressure?

Answer: P = 300 psi

A vessel has a 15-ft outside diameter and effective length of 6 ft. If it issubjected to 15 psi extemal pressure, what is the required thickness (to thenearest l/ 16 in.) if the design iemperature is 300'F?

Answer: t = 7/16in.

A jacketed pressure vessel with an intemal diameter of 12 ft is subject€dto an interni pressure of 400 psi and a jacket pressure of 200 psi . The shellthickness is controlled by the intemal pressure using an allowable tensilestress of 15,000 psi at 800T with an E factor of 1.0. Determine therequired stiffener spacing from Figs. 8.10 and 8.11.

Answer: L = 16.2in.

A distillation tower is subjec0ed to a vacuum of 15 psi. lf D" = 9 ft,t = 0.75 in., and stiffener spacing = 8 ft, what is the maximum permis-sible lemperature?

Answer: T : 900"F

8.4 DESIGN OF STIFFENING RINGS

In deriving Eq. 5.17 for the maximum strength of a cylindrical shell undercxternal pressure, it was assumed that the ends of the shell were simply sup-F)rted. For this to be true, stiffening rings, flanges, and so on (Fig. 8.13) arenccded as lines of supports. These supports are assurned to carry all the load thatthc shell carries due !o external pressure. By refering to Figs. 8. 13 and 8.14,Iotal force in stiffener is

8.6

E

9

E

'6

Ep

EE

i5 a,

,r&.oge;AF

I

i-FI

.JI

+I

-JI

+-l'

JI

+

;+-I

227

Page 124: Process Equipment

DESTON Ot CYltNDRtCAt SHfl.tS

s ti ffener

Figure 8.I.t

PD.L = 2F

PD"L

The stress in the shaded area of Fie. 8.14 is

Io- '- - PD.- L(t + A,/L) 2(t + A,/L)

In this equation it is assumed that the area A" of stiffening ring is ,,smeared', overthe total length z.

Using the terminology of Fig. 8.11 and expression 8.5,

28'FS

The expression for strain is

o

8,4 DESIGN TOR STIFFENING RINGS

12I

,:4P

': FS PP"2 2(t + A,/L)

With a factor of safety (FS) of 3.0 expression 8.5 becomes

-3PD"a:or,aatra

I 2116

U;

E l1ti Itf=-:- A Di,G + A,/L)L

The stiffening ring must also be checked against buckling. The classical expres-

sion for the buckling of a ring due to external pressure is

(8.8)

(8.e)

Es D')"A + A'/L)L

With e", = A, the expression for l becomes

. DzL\t + A,/L)AI: a

This equation can be used in conjunction with Eq. 8.8 and Fig. 8.10. In doingso, a hial A, is normally selected and I is calculated from Eq. 8.8. Using the

value ofB, which already incorporates a factor of safety of 3.0, a value ofA is

obtained from Fig. 8.11. With this A, the required moment of inertia is calcu-laled from expression 8.9

Because the stability of the stiffening ring is essential in calculating the shellstability, a higher factor of safety is used by ASME in the stiffening ringcalculations as compared with shell calculations. With a factor of safety of 3.5,exoression 8.9 becomes

. DZL(I + A"/L)At:-- A-(8.10a)

Page 125: Process Equipment

230 DIS|ON Ot CYUNDRTCAT SHEItS

The svuilable / obtuined liom Eq. tt. lOa must be lower than the availabletmoment of inertia of the stiffening ring. This inertia is calculated without

considering the contribution of the adjacent cylinder. If the composite 1of thering and the effective cylinder are considered, then a penalty of 28Zo is appliedto Eq. 8.10 and a new expession given by

,, _ DzLa + A"/L)' - lo.9

(8. r0b)

must be used. The actual f is calculated from the available rins and shell areasas shown in Fig. 8.15.

Example 8,6. A long cylindrical shell is constructed of carbon steel with ayield stress of 38,000 psi and a radius of 36 in. If the stiffeners are spaced at a4-ft interval, calculate the required shell thickness and the size of stiffening ringsfor an external pressure of l0 psi at 100"F.

Solution. l*t

r : 0.1857 in. = 0.67D-- = tt+t

From Fig. 8.10,

A = 0.00028

From Fig. 8.11,

A : 21000 psi

a

Fisure 8.15

.ing..By comparing expressions 8. 1la and 8. I lb, it can be concluded that in order

for the column aD to be as strong as the plate, its length must be about one-half

8,5 ATIOWABI.E GAPS IN STITFENING RINGS 23I

Hence,

4 /4ooo\r=;t ,* l: l0.4psiJ\--.,

Use a shell thickness of3/16 in. and try a 3 x 3 x 3/16 angle stiffening ring.

A, = 1.09 in.2 and I = 0.9622 in.a

r /t0x72)R = : ----------l-"

: 4 (u187 5 + l og/4a: z)/u PSr

From Fig. 8.11, A : 0.00018.

, _722 x 48(0.18?5 + 1.09/48 x0.00018)A

: 0.67 in. a OK

8,5 AITOWABLE GAPS IN STIFIENING RINGS

Gaps in stiffening rings are normally provided to allow for drainage of vesselcontents or permit piping and other internals to extend through the ring. Exam-ples of various gap arrangements are shown in Fig. 8.16. The maximum allow-able gap can be calculated by assuming the distance between points a and b ofFig. 8. 17 as a simply supported column of length l. The maximum buckling loadthat can be applied to this column is given by

^ lf'I1olI'

The strength of the column must be equal to or greater than the cylindrical shell.For large diameter shell the curvature is small and the buckling streneth of theshell approaches that of a simply supponed flat plate. The riinimuit criticalbuckling strength of the simply supported plate abcd (Fig. 8.17) loaded in thecircumferential direction is given by

_ 4i2Enl 4T2EJI'c, =;r=- _ = ----=-

t-tr - lt-t t'

t

(8.1 la)

(8.1 lb)

Page 126: Process Equipment

Grp lnor to.tc..d I rtm.rth. hrckn.r. ot rh. $.lt ptlrd

Thii.&iion rha h64 momsnt of i..ni!r€qutr€d tor.i^q unl.r r€qun€m€ns ot

L.ngth of.ny g.p in u6eppo.r.d .lt nor o.r..sd l.ngrh ol .c ih*. in Fig. UG.29_2

Tht larion lhatt h!v. mfr@r oti...ri. r.qui4d to. nng.

Figur' 8 1 6 voriou orrong€rnenrs oI rrittuning ring. for cyrindri.or vessers 3ubiecd ro exrernor preasure(Ref. 2).

S]

_l- Typ. ot onttrucrio. _+

1xa- ̂';

232

8,5 ATTOWABTE GAPS IN STIFFENING RINGS 233

Figure 8.17

that of the plate. Therefore, the maximum gap length must be one-half that ofa buckling lobe length of a cylindrical shell. In referring to Fig. 5.16 themaximum gap length can be expressed as

-_l _ ttD.g_;_-;; (8. l2)

ASME has developed curves that are based on Eq. 8.12. These curves areshown in Fig. 8.18. A comparison, however, between Eq. 8.12 and Fig. 8.18indicales some differences. These differences are due to the fact that Fig. 5.18,which is used with Eq. 8.12, is plotted using the first two terms of expressionfl in Eq. 5.27a whereas Fig. 8.18 uses all terms. Therefore, the results of Fig.8.18 are more accurate.

Example 8.7. What is the maximum gap allowed in a stiffening ring of a shellwith D. = 7.O ft, L : 15.0 ft, and r : 1.0 in.?

Solution

'-: t+t

L = a.zsr

Page 127: Process Equipment

-d!

.s

E3$-E

;as!5=

bet-5;IJ=_-@io5

;

E

8I 889 S R

"":#ii3,6+Id=

"+r3

*"""p;'L;

d;:; ";:

g gfig g F

rTog'reu1lq1 - neurrg epcrng

234

and

for cylinders

lrronr F'ig. 5.lll, N

G = 16.8 in.

8.6 OUT.OF-ROUNDNESS OF CYLINDRICAL SHELLS UNDEREXTERNAL PRESSURC

In the fabrication of cylindrical shells, slight out-of-roundness invariably results.This is due to forming, welding, or postweld heat-treating operations. Normally,intemal pressures tend to minimize out-of-roundness, whereas extemal pres-sures tend to increase it. Because of that, and to prevent failure, extra pre-cautions must be taken in fabricating shells that are subjected to external pres-sures.

In Fig. 5. 16 it is assumed that the shell is approximated by a series of columnsconnected end to end. The length of each column is one-half a lobe length, or

, = nDo-2N

The slendemess of each column is expressed by the ratio //r where r is the radiusof gyration. Since r is eqtal to t2/\/12 in a shell wall. the equation becomes

t _ 5.44r N(t/D.)

The eccentricity of each column in expressed by e. If it is assumed that theeccentricity ratio e/r affects the strength of a column in the same way as theshell, it can be concluded that

for columns

8.6 OUI-OF.ROUNDNESS OF CYTINDRICAT. 5HIItS

= 4 and fiom Eq. tl.12,

G ::+ : o.2oD^(4X4)

T

elrr

e 5.44------ca-t/y12 N(t/D.)

Page 128: Process Equipment

DESION OF CYI.INDRICAI. SHELLS

!: c't N(t/D)

(8. r 3)

(8.14)

where C1 : 1.57.

Experiments have shown that for constant tfD, ratios, the value of eftincreases with an increase in Lf D.ratios. This, however, applies only in the caseof intermediate length shells. For this range, Eq. 8.13 was found to give ade-quate results. As the length gets longer, tests have shown than an increase inL/D"has no influence on ef t. On the other hand, tests have shown that as thelength decreases, the value of e/l increases slightly. Thus, Eq. 8.13 needsmodification to take into account the two extreme cases. Thus. disreeardins theincrease in e/t as L/D. decreases. an empirical equation of the fo;

9: Ct ..'- . nt N(Jf,j- "'"is found satisfactory. In using the values of C1 and C2 as obtained from tests, theequation becomes

C : o, o,'=8 + o.ol5Nt N(t / D")

Figure 8.19 is a plot of this equation.

Example 8.8. Calculate the maximum out-of-roundness allowed in a cylindersubjected to extemal pressure with D, : 5.0 ft, Z - 14.0 ft, and t : 0-75 in-Compare the result with that obtained from Fig. 8.19.

5.60 D- = totR

Solution

237

@EoB

q QE

. E=q 66o €o

ct €.0P6

dF

E

'i3{

,9d

II uI I

V I/

tl / I

( / /

//,1

"1/t 4

ls

ilI tt-*:1If

/ I I/ I

/ / I I I I

/

I

3.ssps F s 8 t I tt3R8rTog rcurralql; lraueqq epnrng

Page 129: Process Equipment

2il D|lrol{ o; cYuNDilcAr tH[t3

From Fig, 5.18, N = 3. From Eq. 8.14,

f nnrr -l

"=Lffi)+o'or5(3)J(o7s)e : 0.39 in.

From Fig. 8.18,

e : O.53t

e = 0.40 in.

8.7 DESIGN FOR AXIAT COMPRESSION

For axial compression, Eq. 5.29 rnay be written as

T

.".=*Lo

or

A:lt :99Eot RJt

The allowable strain can be expressed as

FS(R,/r)

A large factor of safety is normally used in this expression because a slightout-of-roundness can significantly reduce the critical sfain. ASME uses anapproximate factor of safety of 10.0. Hence, the expression for allowable com-pressive stress in the ASME is for elastic range,

NOMINCIATURI 239

(8.1s)

For plastic range,

ot= B

where B = is obtained from Fig. 8.ll using A = 0.125/(R,/t).

Example 8.9. A cylindrical tower is constructed of stainless steel 410 mate-rial. Its radius is 6 ft and thickness is 0.5 in. Determine the maximum allowablecompressive stress at room temperature.

Solution

From Fig. 8. 11,

Eo = 29 x 106 psi

For elastic region,

0.062510o,: - n/t

o,=fifo.oazs x 29 x 106)

: 12,600 psi

A =W: o.ooo87

&=3=roo, u.)

For plastic region,

and

A = Il,fiX) psi <- use

NOMENCTATURE

A = shain obtained ftom extemal pressure charts

A" = area of stiffening ring

I

Page 130: Process Equipment

210 DtStON Oi CyUNORtCAt SHH"|"S

I = stress magnitude in a cylinder due to external pressure

D, = outside diameter of cylinder

6 = joint efficiency

E6 : modulus of elasticity

F : peak stress as denned in Table 8.2

/ = moment of inertia of stiffening ring

1' = combined moment of inertia of stiffening ring and adjacent shell

L = effective length of shell

P = intemal or extemal pressure

P6 = primary bending stress as defined in Table 8.2

P1 = pnmary local membrane stress as defined in Table 8.2

P- : primary general membrane stress as defined in Table 8.2

Q : secondary membrane plus bending stress as defined in Table 8.2

R = inside radius of cylinder

R, = outside radius of cylinder

S = allowable tensile shess in the ASME Code, VI[-1

& = alternating stress in the ASME Code, VIII-2

S, : allowable tensile stress in the ASME Code, Vm-2

t : thickness of cylindrical shell

REFERCNCES

ASME Boiler and Pressue Vessel Code, Section Vm, Division 2, Alrs rnative Rules-pressureVessels, ANSVASME BPV-Vn-2, American Society of Mechanical Engineers, New york,1980.

ASME Boiler and Pressure Vessel Code, Section VItr, Division l, prcssure Vesrels,ANSUASME BPV-Vm-I, American Society of Meahanical EDgineers, New york, 1980.

EIBTIOGRAPHY 241

BIBTIOGRAPHY

Windcnburg, D, F., "Vessels under Extemal Pressure," in Pressure Vessel and Piping Desiqtl:

Collected Papers 1927-1959, American Society of Mechanical Engineers, New York, 1960.

tk)lt, M., "A Procedule for Determining the Allowable Out-of-Roundness for Vessels under

External Pressure," in Pressure Vessel and Piping Desiqfi: Collected PaPers 1927-1959,

American Society of Mechanical Engineering, New York, 1960.

Page 131: Process Equipment

Inside surfoce of o vessel hecd. (Courtosy of the Nooler Corp.. St. to'rir, Mo.)

243

CHAPTER

DESIGN OF FORMED HEADSAND TRANSITION SECTIONS

Page 132: Process Equipment

9.I INTRODUCTION

A large variety of end closures and transition sections are available to the desisnengineer. Using one configuration versus another depends on manv factors suihas method of forrning, material cost, and space ."ihi"tionr. Some frequentlyused heads are:

Flanged Heads.

These heads (Fig. 9.1c) are normally found in vessels operating at lowpressures such as gasoline tanks, and boilers. They are also used-in high-pressure applications where the diameter is small. Various details for theirdesign and construction are given by the ASME Code, VI[-l.Hemispheical Heads.

Generally, the required thickness of hemispherical heads due to a grventemperature and pressure is one-half that of cylindrical shells with equivalentdiameter and material. Hemiheads (Fig. 9.10) are very economical whenconstrucied of expensive alloys such as nickel and titanium----either solid orclad. In carbon steel, hemiheads are not as economical as flaneed and dishedheads because of the high cost of fabricalion. Hemiheads are iormally fabri-cated from segmental "gore" sections or by spinning or pressing. Segmentalgore hemiheads are economical in thin, large diameter equipment or thick,small diameter reactors. Because hemispherical heads are thinner than cylin_drical shells to which they are attached, the transition area between the headand shell must be contoured so as to minimize the effect of discontinuitystress. Figure 9.2 illustrates the hansition requirements in the ASME Code,vm.

Elliptical and Torispherical (Flanged and Dished) Heads.

These heads are very popular in pressure vessels (Fig. 9.lc and d). Theirthickness is usually the same as the cylinder to which they are attached. Thisreduces considerably the weld build-up shown in Fig. 9.2. Thus, because therequired thickness in areas away from the knuckle region is less than thefurnished thickness, the excess can be advantageously used in reinforcingnozzles in these areas. Many mills can fumish such heads in various di_

2U DISION OT IORMED HTADS AND TRANSITION SECTIONS

amelers and thicknesses that are competitive in price.In a true elliptical head the radii of curvature vary between a jacent points

along a meridian. To simplify the calculations and fabrication, the ASMECode established the following various approximations. A 2: 1 ellipticalhead can be assumed to consist of a spherically dished head with a radius of9OVo and a knuckle radius of 17go of the shell diameter to which thev areattached, as shown in Fig. 9.3. The smallest knuckle radius allowed for aflanged and dished head is 67o of the shell diameter and a spherical radius of1007o of the shell diameter.

9.I INTRODUCTION 245

--r-.].'

_1 ,

(TORISPHERIcAL)

( g) IlISCEL!ANE0Us

Figure 9.1 commonly usad lormed closurc heods.

Conical and Toriconical Heads.

These heads shown in Fig. 9.1e and / are used in hoppers and towers as

bottom end closures or as transition sections between cylinders with differentdiameters. The cone-to-cylinder junction must be considered as part of thecone design due to the high unbalanced forces at the junction. Because of

_T

(a) FLANGED(b) HEI.lISPHERICAL

(c) ELLIPTICAL (d) FLAIIGED & DISHED

(e) C0NICAL (f) T0Rl c0lt IcAL

Page 133: Process Equipment

II

lilc

l- '".ca<1l2las-.hl

rb

F

taper./, may inctudethe width ol the weld-

{cl (dl

Fisure 9.2 H€od-to{hell iunction. (Courrety of the Americon Societ}' of ldechonicol Ensi'ieers)

{a) ASiIE 2:1 Head

I

<112k,-.hl

T246

(b) ASI.IE Flanged and 0ished Head

fisure 9.3

where

(9.2a)

9,2 ASME EQUATIONS fOR HEMISPHERICAI HIAD DISIGN 247

thcse high fbrces, the ASME Code, Vlll-1, limits the apex anglc to a max-

imum of 30" when the cone is subjected to intemal pressure. Above 30'adiscontinuity analysis is done or a toriconical head used to avoid the un-

balanced forces at the junction.

Miscellaneous Heads.

Many chemical processes require unusual vessel configurations. The heads ofsuch vessels can have an infinite number of contours. One such contour is

shown in Fig. 9. lg. The design of these heads is very complicated and there

are no simple methods of analysis. Experience, proof testing, and sophisti-

cated analyses are generally used to determine required thicknesses.

9.2 ASME EQUATIONS FOR HEMISPHERICAT HEAD DESIGN

The ASME Code, VI[-l, has combined Eqs. 6.1 and 6.7 for internal pressure

into one simplified equation:

PR (e.1)2SE - O.zP

where t: required thickness

P = intemal pressure

.lR = inside radius

S : allowable stress

B = joint efficiency

This equation with E : 1.0 is plotted in Fig. 6.3 and it approximates the more

complicated Eqs. 6.7 over a large range of r'fri- Othet forms of Eq. 9. 1 are

shown in Appendix I.For external pressure, Eq. 6.35 is taken as the basis for the ASME Code

equations. Defining e". : A, r : R,, and modulus of elasticity as Es, Eq. 6.35

can be written as

0.t25Es R"/t

. 0.125" R"/t

A = critical shain

R, = outside radius

t : thickness

Page 134: Process Equipment

214 DISION Of FORMED HTADS AND TRANSITION STCTIONS

The critical strcss in a sphcrical section is given by

P",R.a*: Zt

or

P., = 2% =4+R"/t R./t

and the allowable pressure is expressed as

zAEo(e.4)

FS(R,/')

Using factor of safety (FS) : 4.0 and substituting Eq. 9.2a into 9.4 gives

p _ o.0625Eo- (R./ t)'

where P = allowable extemal pressure

Eq = modulus of elasticity

The ASME procedure for determining the allowable external pressure for aspherical section is to detemine fust the A value from Eq. 9 .2a. The allowablepressure can then be obtained by referring to a stress-strain chart similar to theone shown in Fig. 8.11. IfA falls in the elastic region, then P is calculated from84.9.2b. If ,4 falls in the plastic region, however, a value ofB is determinedfust from the chart. The allowable pressure is then calculated from exoression9.3 as:

(e.3)

(e.2b)

(e.5)

(9.2c)

P" = 20-

FS(&/r)

Substituting B : o",/2 inl.o Eq. 9.5 gives

p= B- R./t

where B = factor determined from Fig. 8.11.

Equations 9.2 form the ASME basis for determining allowable external pres-sure for sDherical sections.

9,3 ASME DESION EQUATIONS 249

lixamplc 9.1. Using the ASME criteria, determine the allowable cxternrlprcssure on a spherical shell with R, = 60 in. and t : 0.5 in. Use the 300'F linein Fig.8.ll.

Solution, From Eq. 9.2a,

n l rsA:ffi=0.00r

From Fig. 8. I 1, with A : 0.001, a plastic behavior exists and Eq. 9.2c must be

used. Hence, from Fig. 8.11

B : 11,000 psi

and

":*@ = nt o" I

9.3 ASME DESIGN EQUATIONS FOR ELTIPSOIDAI AND FLANGEDAND DISHED HEADS

The general solution of Eq. 6.39 is very cumbersome because 12 is a variablefunction. However, the stresses obtained from Eq. 6.39 are important becausethey can be added to the membrane stresses of Eq. 6.37 which results insignificantly reducing the total stress at the vicinity of the junction. Therefore,this equation can be advantageously utilized by the designer in reducing therequired head thickness. The ASME used this fact in developing design param-eters for ellipsoidal and torispherical heads.

A study was mader with ellipsoidal heads to determine the effect of the ratioa/b on the stress level at the head-to-shell junction for a constant ratio 32 of head

thickness t to shell radius r. The study indicated that the point of maximum stressin the head changes with a change of afb.Forheads shallower than a/b of 2.5,the maximum stress is in the hoop direction at the outside surface of the knuckleregion and is in compression as shown in Fig. 9.4. For ratios of a fb between 2.5and 1.2, the maximum stress occurs at the junction and is a hoop tensile stress.

The stiess magnitude for various ratios ofa/b is shown in Fig. 9.4. A simplifiedequation used by the ASME Code, VIII-I, approximates the theoretical stressratios of Fig. 9.4 for values of af bbetween2.6, which is the maximum allowedby the code, and 1.0 for a spherical head:

- : il'. (-tl] (e.6)

Page 135: Process Equipment

;t$

DISION Oi TORMID HEADS AND TRANSIIION SICTIONS

at6

Fisur€ 9.4 l,{oximum ske5s in ElliFoidol Heo&. (Ref. t, p. l3,t).

A plot of this equation is also shown in Fig. 9.4. The ASME Code uses the Kvalues given by Eq. 9.6 to determine the required stress ratios needed in obtain_ing thickness of ellipsoidal heads. This is accomplished by multiplying thecalculated thickness of a cylindrical shell with diameter D by'K valuis. Hince,for ellipsoidal heads,

(e.7)zSE - 0.2P

where t : thickness of ellipsoidal head

P = internal pressure

D = diameter of shell to which head is attached

l< = sfiess intensity factor obtained from Eq. 9.6

S : allowable stress

6 = joint efficiency

For torispherical heads, tests conducted by H<ihnr and others have shown thatthe stress at the knuckle area due to internal pressure reaches the yield value longbefore the spherical region does. Hrjhn plotted an empirical equation that cor_relates well with available test data, as shown in Fig. 9.5. To ivaluate Hcihn'sempirical curve, Fig. 9.5 shows anotler curve that indicates the stress rn an

___-_ Lh.or.t, loo I vo lLr..tmot. votu.. etvon bU Eq.{9.O1

lle hooD etr€e6 of

I le nerldlonol EtroBs otde eual'oc€ of knucklo o-eo

I

1 rffz,tf;r] i

e

d

-6

g

lrcdoqo-

d9;i"P:.{6iE5

,^=

6odoq-:doact

ci

3*3533ss€J1s ur\oJc 01 sseJ,ls ur^rr r xour Jo o|1ou

o x-o*r

-E, tt.o.- o

---.'ia *,- tJrxo0-oxl(

-ti 6to ", o.l

IEL_4tl-!i-;;-F;-3

q-

:sEiE,6

l0^6il-\.

-:Ztlli-l

C.

(-lI't{

-_!

-jlI

l'o -l.!tot9.aIO-

.lLi:L -)o

-l

li't^.,lJ]a)tolts

roo (.l-

'l_.o-o

t.

ttl

//

rt

251

Page 136: Process Equipment

equivBlent ellipsoidal head whose thickness is equal to the shell thickness. Thiscurve indicates that Hrihn's curve is liberal for small values of knuckle to crownradri r/L. Accordingly, the ASME Code, VIII-I, developed an empirical curvethat parallels both Hdhn's curve for large values of rfL and the ellipsoid curvefor small r/Z ratios, as shown in Fig. 9.5. The ASME curve can be expressedby the equation

DIsION O? TORMID HTADS AND IRANSITION SICTIONS

Thus the ASME equation for the torispherical heads is given by

PLMzSE - O.zP

where r : thickness of torispherical head

P = internal pressure

Z = spherical crown radius

M = stress intensity factor obtained from Eq. 9.9

S = allowable stress

g = joint efficiency

r = knuckle radius

n =)(z + (e.8)

(9.e)

In practical applications researchers noticed that Eq. 9.9 gave conservafiveresults for the majority of head designs but became unconsirvative for lareeratios of r/t. This ratio was not considered by the ASME in its derivation of E-q.9.8 because Fig. 9.5 was based on a constant value of r/r. Accordingly, researchwas conducted to evaluate the buckling behavior of the knuckle region for headswith large ratios of //t. The plastic analysis concept was used arid shown2 thatthefollowing equation can adequately predict the behavior of torispherical headswith large rf t rutios:

o"/FS = (0, *,,;);.,'(, -,,;)(i) - o 0006

Sglving. for _r

and fetting or/FS : S, the following approximate equarionobtained and used by the ASME Code, VIII-2:

nl= -t.zent - 4.ss246(; + 28.e3318G)

9.3 ASMI DISIGN IOUATIONS 253

(9.10)+ fo.oozw

- z.z4,,os!) + rs.oszr(r)] r" I| /r\+ 10.26879 x 10 a - 0.442621;l +L \U/

where t : required torispherical thickness

-L : spherical crown radius

L ..r

' "'-,(;i]l('";)]'

r = knuckle radius

D = diameter of shell to which head is attached

P : intemal pressure

S : allowable stress

A plot of Eq. 9.10 is shown in Fig. 9.6.

Example 9,2. What is the required thickness of a 3 : t head ifD = 144 in.,P= 100 psi, S: 17,500 psi, E: 1.0?

Solutian. From Eq. 9.6, with a/b = 3,

K: 0.166712 + (3.0f1

= 1.83

From Eq. 9.7,

(100x144)(1.83)

2x 17,500 x 1.0 - 0.2 x 100

= 0.75 in.

Example 9.3, What is the required thickness of a flanged and dished head ifD=24O in., L=2AO in., r: 15 in., S:17.500 psi, E= 1.0, andP : 50 psi?

Solution.

I

Page 137: Process Equipment

.17 l2: I Etl,plo'dar h€.d)

,005

Thickne.s of Formed

.01 .02 .03 .04 _05

Heods (Courre.y of lhe Ane.icon Sociery of /vtechonicolFigure 9.6 RequiredEnsineers.)

254

9.3 ASMT DESIGN EOUATIONS

l;rrrn Eq.9.tl.

l-M=zG+vr6): 1.75

From Eq. 9.9,

50x240x1.75t:-'-2xl7joox1.o-02x50: 0.60 in.

Because the thickness is obtained from Eq. 9.9 and because this thickness issmall compared with the diameter of the head, the requirements of Eq. 9. l0 mustbe checked.

r15D 240

P;J

: 0.0625

50

17,500

= 0.002857

!I

and from Eq. 9.10,

/r\ln l;l : -s.54851

\L/

;= o.oo38e

t = 0.93 in.

Hence, for this head a minimum thickness of 0.93 is to be used. I

9.3.1 Ellipsoidol ond Torisphericol Heods under Exlernol Pressure

For extemal pressure, the knuckle area is subjected to a tensile stress. Hence the

critical area that is necessary for consideration under extemal pressure is the

spherical region. Thus the ASME criteria for all ellipsoidal and torisphericalheads under extemal pressure are the same as those for spherical heads.

Page 138: Process Equipment

116 DIIIO}I O' IOTMID H!ADs AND TRANSITION SGCTIONS

9.4 ASME EQUATIONS FOR CONICAL HEAD DESIGN

From Example 6.7 it is seen that the hoop force Np is twice as large as thelongitudinal force N5 in conical heads subjected to internal pr"rr*". Th" ASMECode, VI[-I, uses Eq. 1 of Example 6.7 as the basis for establishing therequired thickness of a conical section subjected to intemal pressure. The Jqua_tion is given by

PD2 cos a(Str' _ 0.6p)

where P = internal pressure

(e.l l)

D = inside diameter of cone at the point of consideration measuredperpendicular to the longitudinal axis

,S = allowable stress

g = joint efficiency

a = one-half the included apex angle of the cone at the center line ofthe cone

"I:TOr" 9.4.

. What is the required thickness of a conical head attached to a

cyllnder whose inside diameter is 40.0 in. if the intemal pressure is 450 psi, theallowable stress is 20,000 psi, E = 1.0, and a = 20.0?

Solution. From Eq. 9.11,

(2X0.940X20,000 x 1.0 - 0.6 x 450)

= 0.49 in. I9.4. I ASME Simplificotion of Discontinuity Anolysis due fo Iniernolrressur€

The ASME Code, VtrI-1, uses the stress expressions obtained in Example 6.9f9r inlernal pressu€ as the basis for establisiing simplified l.ite.iu fo, dir"on_tinuity analysis at the cylinder-to-cone junction. At ihe large end of the cone(Fig,. 9.7) the discontinuity analysis results in the following i*o.*piessions fo,me longlrudlnal and hoop stresses in the shell:

,=!(o'+x{rz\

""=7(, - rrn

"\

T]

I'I

_t_

9.4 ASME EQUATIONS FOR CONICAT HEAD DESIGN 257

I--+. l+I

2raon6

+il rvl_t

Fig'rr€ 9.7 Discontinuiiy iorcas dus ro internol preslur€.

where, in this chapter, a is used rather than q' and X and Y are given by

X = 4.559U2 tan d

Y = 1.316(V - 2V) tan a

and V and V2 are given as in Example 6.9.The longitudinal stress in Eq. 9.12 is in tension for all values of a and does

not govem the design criteria. The f term in the circumferential stress expressionin Eq. 9.12 is positive for all practical applications. Hence the quantity a" variesfrom a maximum tensile value of Prft to a compressive value that depends onthe angle a. The ASME Code, VIII-I, limits the maximum compressive circum-ferential stress to a value of Pr/r. Using these criteria, the quintity yl|rt;nEq. 9.12 must be limited to a value of 2.0. Values in excess of 2.0 must besupported by a ring added at the junction. The area of the ring is given by theequatron

I\l I-nT,l?

___L

tr2 tan q (Y\EIt - 2)(e.13)2 Y\6rt

A plot of the quantity y shows that it can be approximated by the expression0.005a as shown in Fig. 9.8. Substituting this value into Eq. 9.13 gives

The ASME Code, VI[-l,1.5SE and thus

(9.14)t2tanall, ['

400 \(9.12)

limits the comnressive circumferential stress to

Page 139: Process Equipment

258 DTSION OF fORMTO I{TADS AND TRANSITION SECTIONS

t.o

oS

o.e

o.2

/X=O.C t2 6- \-7

'7Li =,r.5591I

'z Lan o\

4 --2 <=-l---<ly,o.brri!Y= 1.3t6<,V | -zvz tLonc,.

tO' 30' 40. SO.

o<

Figure 9.8 X ond Y volues for externot prossurc.

l.sSE : At

E [ssz,V7= ! P

Equation 9.14 thus becomes

Prl /^,=G('_

or for the large end of cone,

12 = radius of cylinder at large end of cone

J = allowable stress

t : joint efficiency

A = 326.6\/FEE

a = one-half the apex angle of cone

326.6\/F7SE\-- " 1t^"

. P,1 /. A\o':2sE\'-i) t"

where A, = required area of ring

P = intemal pressure

(9.15)

9,4 ASMT IQUATIONS FOR CONICAL HIAD DISIGN 259

liquation 9. l5 is used by thc ASMB Cirde , Vl ll- I , as thc bitsis litr chcckinglllc.ioint bctween the cylinder and the large end of cone due to internal prcssuro.

At thc small end ofthe cone (Fig. 9.7) the circumferential and longitudinal stress

cquations due to internal pressure are

Because both expressions include a negative term, the equation for or controlsbecause X is numerically larger than Z Limiting the maximum compressivestress to Pr/t, the term in parentheses in the equation for o1 is

< 1.5

and a stiffening ring is needed for values of XYr/t greater than 1.5. Therequired area of the stiffening ring is

Prl ran q l- t.s 'll_=-=-tl _.:l

zSE I xt/r,/tl

From Fig. 9.8, it is shown that the quantity X is approximated by 0.012a. Hencethe required area can be expressed as

. Prl tan af , 125 'l

2sE L' d,rtl

,: !(o '-',4)""=?('- ",4)

^': #(' - *) "" "

where A = *G

(9.16)

(9.r7)

By assuming that the maximum allowable longitudinal stress is limited to ,St,the expression

Pr.SE =;

can be substituted into Eq. 9.17 to give for the small end of cone,

r, = radius of cvlinder at the small end of cone

(9.18)

Page 140: Process Equipment

-*"--"W*-ffiUfY6ffiU'iii,aibt iio mmnror uapng

Exanple 9.5. Doslgn thc conc ehown in Fig. 9.9 and check the cone-to-shcllI junctions. L€t S = 20 ksi, E = 1.0, and p = 150 psi.

Solutian. From Eq. 9.11,

For small end

For the large end,

A = 326.6\m =28.28"

and from Eq. 9.15 the required area at the large end is

^=ffiffi(r-ff)<os,t= 0.64 in.2

A=89 = 7.71

100)

Fisurc 9.9 figur. 9.10 DLconrinulty for.e. dua lo cx|lrnol pr€!!ure,

9,.1 ASrvU IOUAT|ONS fOR CONICAI HIAD DlllON 261

and the required area

,=ffi(t-1ff)<o.sttt= 3.70 in.2

9.4.2 Conicol Shells under Exlernol Pressure

The goveming equation for the design of cones subjected to extemal pressure is

obtained from @. 6.43. Using a factor of safety 3.0, Eq. 6.43 becomes

P. 0.87(t,/D)25 (9.19)Es. L"/D,

This equation that expresses the cone in t€mrs of an equivalent cylinder ofthickness r" and length tr, is analogous to 84. 6.42 for cylindrical shells. Thus

the ASME Code, VI[-l, applies the same equations for the design of cylin&icalshells under extemal pressure for the design of cones with applicable values oft" urd L":

9.4.3 ASME Simplificotion of Discontinuity Anolysis due to ExternolPresgure

The discontinuity forces due to external lnessurea at the large end of cone are

shown in Fig. 9.10 and expressed as

I

{irtt*-_:I_

Page 141: Process Equipment

262 DI3ION OI IORMTD HIADS AND NANSTTION STCTIONS

u,__p_!t*r{^r,I I'''

'--&1'-"2)r \ t/where X : 9.34 Vz tan tt

Y = 2.57 (Vy - 2V2) tan aN, : axial compressive force = Pr2f2t + g

Q : axial force due to wind, dead load, etc.

lhe v-alues of X and I in Eq. 9.20 can be approximated by the expressions inFig. 9.11. A comparison of o; and or given by Eq. 9.20 indicates that themaximum compressive stress is given by ar; a conservative maximum allowablecompressive stress value is Pr2/f and thus

o.o27a E Pr''V;=N*-l

A stiffening ring is necessary if this quantity is exceeded. The required area ofthe ring is given by

_ (Prz/N,) - 1fO .027 a\/ r2/ t l

(e.20)

A,: (N,tanr(;;)lt

oEJla

x

z.ot,et.61.1t.2t.oo.8o.6o.+o.2o

.7x=bs4vzrLno< -./.

X:O.O27d rrttt'

'.t'

Y =o. to64 \- f_le. SZ.y - zvr,'Lonq^to. 20.

o(Figure 9.ll X ond Y voluer for externol pressure.

o'

pressure load at small end stiffening n"t: O!&i#

cos a

9.4 ASMI EQUATIONS TOR CONICAT HEAD DESIGN 263

lly limiting the axial stress to an allowable value of SE, the above equation canbc written for large end of the cone,

o'=*'#""1'-i(|*2.4):] (9.2r)

(9.22)

where A: 104

At the small end of the cone the stress is eiven bv

and the maximum compressive stress by 4. Limiting the allowable compressivestrcss to -(P/r/r), the first of Eq. 9.22 reduces to

(9.23)

_r,,_r,ill.r.- _P,,^t

or N, s 0, which indicates that at the small end of the cone the axial force N,must be resisted by a ring with an area for the small end of the cone

o _ N,rr tzn a" .sE

- Pr. "l/2o" = 1- r;N,t I'' -

-N-/ /^r:;l,t * "v;/

In addition to providing the required arca at a cone-to-shell junction, it isnecessary to design the ring at the junction to prevent buckling due to externalpressure. The procedure is similar to that for the design of stiffening rings incylindrical shells. A conservative approach used by the ASME Code, Vltr-l, indesigning cylindrical shells under extemal pressure assumes that intermediatestiffening rings support all the load applied to the shell. Using the same criteria,the load on the cone in Fig. 9.10 due to extemal pressure can be proportionedat the large and small end stiffening rings as follows:

pressure load at large end stiffening ring : ZnP (r2 I r)(r2 - r)3sina

PSE

Page 142: Process Equipment

2U DTSION Of TORMID HIAOS AND TRANSITION SECTIONS

'Ii)t l l()td itt lirrgc cnd duc ttl axial conrprcssitln, prcssurc on conc, an<I pressureon cylinder is

, = +tan q +, tun o + !. eliffi*or

where

t,_r2tana, Lt ri- rl

Total load at small end due to axial compression, pressure on cone, and pressureon cylinder is

^ Prt PL, 14 - r?/"= ^ tan c + -=- + =-P -r f, t?trr ctz I br2 t0ll d

F = P(M) +, tan 0

F = P(N) + f2 tar, d.

(9.24)

(9.2s)

where

rv=?tun o+L: +:3 lrlL Z O/2 l&Il (t

Equations 9.24 and,9.25 establish the maximum applied force at the cone_to_cylinder junction. The critical buckling stress of a iircular ring is

3Eolo" :

nr,

where A, is the total effective area given by

A' = + + Lj + e, for large end of cone

A' = + + Lj + e, for small end of cone

NOMENCLATURI

Ily using rr1 = E,A. thc above equation reduces to

Ar2 A,(e.26)

which is the required moment of inertia of a cone-to-shell stiffening ring.For design purposes, the value of A in Eq. 9.26 is obtained from a

stress-strain relationship. This is achieved by considering the stress in the ringas

Fr(9.27)

Applying a factor of safety of two in the foregoing equation and using theExtemal Pressure Charts in ASME (hat have a factor safety two), a designcriteria can be established as follows:

1. Calculate f. from Eqs. 9.24 or 9.25.2. Establish

3. Enter the Extemal Pressure Charts with a (factor B) and calculate thestrain A.

4. Use Eq. 9.26 to establish the minimum required moment of inertia. TheASME allows a 307o increase in value if the composite ring-shell mo-ment of inertia is considered and the equation then becomes

ADZA,

15.6

NOMENCTATURE

A : strain as obtained from Fig. 8.10

At : area of stiffening ring at cone-to-shell junction

,B = stress factor as obtained from Fig. 8.11

D : diameter

D1 : base diameter at small end of cone

Page 143: Process Equipment

26 OISION O' IORMID HTAO3 AND TRANSITION SICTIONS

l)r - base diumeter at large end of cone

6 = joint efficiency

8s = modulus of elasticity

, = head depth

I = moment of inertia

lK : factor for ellipsoidal heads as determined from Eq. 9.6

Z = spherical crown radius of flanged and dished heads

Z' = effective length of cylindrical shell

L" : effective length of conical section

= 70 + Dt/D:.l

M = factor for flanged and dished heads as obtained from Eq. 9.g

P = pressure

P" = allowable extemal pressure

It = inside radius

R, = outside radius

r = knuckle radius

rr : base radius at small end of cone

/2 = base radius at large end of cone

S = allowable stress

r = thickness

t" = effective thickness of conical section: tcos d

a = one-half the cone apex angle

4 : circumferential stress

(,r = longitudinal stress

REFERENCES

L Brownell, L. E., and E.H.Yorlll.g, Process Equipment Design, lolmWiley, New york, 1959.2. Shield, R. T., and D. C. Drucker, "Design of Thin-Walled Torispherical and Toriconical

Pressure-Vessel Head,s" in Pressure Vessels anl Pipirrg: Design atd Anatysis-A Decade ofProSleJr, Ameican Society of Mechaoical E4ineers, 1972.

Bf sf.tooRAPHY 267

.1. Bourdtnun, l{, C., "Strc$scs al Junction ol Conc and Cylindcr in Tanks with Cono Bottuns orEnds" in Prc.rsare ye.rszl aul Piping Design: Colkcted papers 1927-,/9Jg, Amcrican Socictyof Mechanical Engineers, 1960.

4. Jawad, M. H., "Design of Conical Shells under Extemal Loads,,' Jounnl of pressure VesselTechnology, pp. 230-238. Vol. t02, 1980.

BIBLIOGRAPHY

Fliigg€, W., Strcrrer ir, S,ells, Springer-Verlag, New york, 1960.

Page 144: Process Equipment

CHAPTER I OBLIND FIANGES, COVERPLATES, AND FLANGES

264

Iypicolflons€: r.ody for in.tollins. (Courlesy G+W Tdylor-Bonmy Div., lqylor Forse)

269

Page 145: Process Equipment

SIIND fLANOTS, COVTR PIATES, AND TLANGES

IO.I INTRODUCTION

One of the more common types of closures for pressure vessels is the unstayedflat head or cover. This may be either integrally formed with the shell or weldedto the shell, as shown in Fig. 10.1; or it may be attached by bolts or somequick-opening device as shown in Fig. 10.2. It may be circular, obround,square, rectangular, or some other shape. Those circular flat heads that are

(b)(a)

'tt-I

|-..............

T|-?\ I) tt II Fi-)-"--w

Int srol or wlld€d tlct h€ods.

IT(e)

Figoro l0,l

Fetaining

IO.I INTRODUCTION 271

I .--.i.nili--l lhl/il rhreadedi I ll'hl- "*\ --ltll-llll-J- - -t+-u-

(d)

Fisur€ 10,2 Bolt€d or quick-op€nins flol h€o&.

bolted into place utilizing a gasket are called blind flanges. Usually, the blindflange is bolted to a vessel flange with a gasket between two flanges as shownin Fig. 10.3. Although flat heads or blind flanges may be either circular ornoncircular, they usually have uniform thickness. In addition to the flat head orblind flange+ype closures, many large vessels use a circular, spherically dishedcover with a bolting flange, as shown in Fig. 10.4. In all cases, the bolts ofthehead attach either to a bolting flange on the end of the shell or to a thickenedshell.

In general, "failure" of a bolted flanged joint is due to excessive leakage atthe gasket, with very few failures in the metallic pressure boundary. Occa-sionally, problems encountered with bolts result from excessive tightening inreducing the leakage problem during hydrostatic testing of the assembly. Some-times excessive stresses in the bolts cause them to break or to stretch until theclosure leaks.

The basic equations used for the design of flat plates and blind flanges in theASME Code, VI[-1, are based on a flat plate with uniform thickness anduniform loading over the entire surface due to pressure. Depending upon the

Page 146: Process Equipment

l

I

Figur. 10.3 Elind flonsG-intesrol flonge conn.cnon.

h'.1__{|I

Kiucrh \lU ! R.d,u' \-\ca,rer \

Loos F1169. Typ.

Figure l0-4 Sphericolly dish€d cove|'s with bolting[nsino6r', ftom Fig. l-6 of rhe ASr{E Code, V I-i.)

272

Gastel

fTI

a

t-I

tbt

-l-1n c::

|-1/2A-''--.------.1I F-l/a la + 8l+I I ---?,,/-"),.#f,1t2 I

t2c(d)

flonses. (Courte.y Americon Socisry of Mechdn.col

r0.t tNTRoDUcTtoN 273

dc(ails of the corner construction shown in Fig. 10.5, various C-factors are usedthat require different minimum head thicknesses. The maximum deflection ofthe plate is assumed as not more tltan one-half the thickness and all the stresses

are keDt within the elastic limit.

icmkor!!dd . _- _^_

(rt lb ll lb.2t l.)

r* = ? rr nr.. nor r.$ rh.n 1.25 rr

c' 013 sk.rch.r{.llr) lsl ctrclr..cov.d,c- 033n, cmin. - o.2o,0,

"on-C',cur.r Cov.^, C -033

i., ir) ror

i-- L- _ tth.^..2t, i jrrr,rf l:l'^ ,.. .,.

' .WZ 'hnror75n ,,-,.,.i'i-'::lffi:.,,,M .' lt M,.,,.:r:- i_4;"1"6;,: |', 1 14/4,.1,, l; rn:-,^.'o.25,,'"' {ll $-",+#' L",Jr{- | - -VA " "''^ #l-r.,

c'o.r7o, c. o.r? c-033D :J^H:" * **' c.o3o

C.0.10 C m'n.. 0.20 C-o.20or0.13

ffiStt [.\ i| firj'I

@*4) llNniI d ll\l llf r{lf ll

rcKlt 1- h+

C. o.33

Fis',r€ 10.5 Un3toyod flor heods dnd covers. (Court6y Americon Soci€ry of r{€€honicol Ensineerc, tom Fis.

UG-3,1 of rhe ASME Codo, Vlll-I.)

c-0,33

C - O.2S

Page 147: Process Equipment

274 BTIND FI,ANOTS, COVTR PTATTS, AND fIANGES

IO.2 CIRCULAR FI.AT PLATES AND HEADS WITH UNIFORM

TOADING

When an exact solution involving a discontinuity analysis at the shell-to-headjuncture is not wanted, flat heads are generally calculated based on the assump-

tion that the edges are simply supported or fully fixed. The true condition lies

somewhere between.Exact equations for circular plates were developed in Section 7. l. In using

those equations as a basis, the equations below were developed using the head

diameter d instead of the radius term a. The following nomenclature was also

substituted in the equations of Section 7.1:

Poisson's ratio (p = 9.3;p = pressure loading Qsi)

E' : modulus of elasticity (psi)

d = diameter of head (in.)

T = nominal thickness of head (in.)

P : total presswe load (lb) = 6.7*t Ort

With the edges assumed to be simple-supported,Maximum stess is located at the center and equals

o^ = o.zs+fi (10.1)

Maximum deflection is located at the center and equals

w* = 0'0554#

Maximum rotation is located at the edge and equals

o* = o.s2s:L"'"-'E',Tj

With the edges assumed to be fully-fixpd,Maximum stress is radial and located at the edge:

o* = o.zto f;Maximum deflection is located at the center and equals

(10.2)

(10.3)

IO.2 CIRCUTAR TIAT PI.ATTS AND HEADS WITH UNITORM TOADING 275

w^ = 0.0B6#

Tangential stress at edge equals

o': O'Ilrcf;

Radial and tangential stress at the center equals

^ . -_ POI: OI = U'IJJ'i

( 10.5)

(10.6)

(10.7)

(10.8)

(10.e)

When the circular flat plate is loaded under uniform pressure p over the entiresurface, simplified equations of stress are

,: o.3ose(xf

/ )\2o = o.r88P(;/

for simply supported edge

for fixed edge

In actual designs, neither of these edge conditions is likely to be realized. Fullyfixed is very difficult to obtain in any constiruction.

Example 10.1. Determine the maximum stress in a flat head under internalpresswe of 1000 psi, diameter / = 48 in., and thickness r = 7 in. for bothsimple-supported and fixed-edge conditions. Assume carbon steel withfr = 0.3.

Solutian. Determine the total loading

P : 0.785 pd2 = 0.785(1000)(48),

P = 1.809.000 lb

For simple-supported edge use Eq. 10.1:

, : o.:l+!!.ffi : 14.550 psi(10.4)

For fixed edge use Eq. 10.4:

Page 148: Process Equipment

276 0UND FTANOIS, COVfR ptAT[S, AND ftANOIS

,, = 0.239 !l -1109-(xx)t--lj-: tlttzopsi I

Example 10.2. For the flat head in Example 10. l, determine the deflection atthe center for both edge conditions.

Solution, For simple-supported edge use Eq. 10.2:

rr R09,000x48fw = 0.0554*r.l x toltzt' = u'uzrz rn'

For fixed edge use Eq. 10.5:

, = 0.0136#" r0.)or24gx4l

= 0.0057 in.

Problems

10.1 What is the maximum shess in a simple-supporied flat head whenp : 56psi, d : 24 in., t : 0.75 in., and p = 0.3t

Answer: o^ : 15,840 psi

10.2 What is the maximum stress for the conditions in hoblem 10.1 usins thesimplified equation?

Answer: c,,," = 15,820 psi

IO.3 ASME CODE FORMUTA FOR CIRCULAR FLAT HEADS ANDCOVERS

In the ASME Code, Vm-1,1 and Section I,2 the minimum required thickness ofcircular, unstayed flat heads and covers without bolting are calculated by thelollowine:

I

t=d (10.10)

E = butt-weld joint efficiency for a joint within the head

S : allowable tensile stress (psi)

p : design pressure (psi)

C = 0.10 through 0.33 depending upon the construction details at the

tcplsrwnere

Answer: t6n = 5.792 n.

IO.3 ASME CODT FORMUI.A FOR CTRCUTAR FIAT HEADS AND COVTRS 277

head-to-shell juncture (see Fig. 10.5) and contains a factor toincrease effectively the allowable stress to 1.5 S because the stressis predominandy a bending stress

d = effective diameter of head (in.) (see Fig. 10.5)

t = minimum required thickness of flat head (in.)

Example 10.3. Determine the minimum required thickness of an integral flathead with intemal pressurep equal to 1000 psi, S = 15,000 psi, d = 48 in. withno corrosion, and no weld joints within the head (E = 1.0). The arrangementis the same as that given in Fig. 10.5, sketch , - 2, with m : l.O.

Solation. From Fig. 10.5, sketch b - 2, C = 0.33 m: 0.33(l) = 0.j3.From Eq. (10.10),

t=48 : 7.120 in. I

Example 10.4. Determine the minimum corner radius to make Example 10.1acceptable (valid) to be used.

Soltrtion. The cylindrical shell thickness r, must be calculated using Eq. UG-27(c)(1) of the ASME Code, VII-1:

PRl::=---------: 1000 x 24' sE - o.6P 15,000x1 - 0.6x1000

From Fig. 10.5, sketch b - 2, the rule is for

= 1.667 in.

,, > 1.5 in. r.j" : 0.25t, : 0.25(1.667) = 0.417 n. ACl lProblems

10.3 A flat head is constructed according to Fig. 10.5, sketch d. The diameterd = 12in., thickness r = l.25in.,E: l.0,andS = 15,000psi. Whatis the MAWP (maximum allowable working pressure)?

Ansyer.' MAWP = 1250 psi

10.4 A large flat head is made from pieces that are weld€d together and spotexamined so that ,E : 0.85. The corner details are similar to Fig. 10.5,skerch/ with ltt = 1.0. The diamet d = 60 in.,,S = 12,500 psi, andthe internal pnessure p = 300 psi. What is the minimum requiredthickness?

0.33 x 1000

15,000 x 1.0

Page 149: Process Equipment

278 0UND ftaNoEs, cov[R plarts, AND fl.ANGtS

IO.4 COMPARISON OF THEORY AND ASMT CODE FORMULA FORCIRCUTAR FLAT HEADS AND COVERS WITHOUT BOLTING

As previously mentioned, the ASME Code formula contains a factor of 1.5within the C factor to adjust for the permitted higher level of allowable stressbecause it is chiefly caused by primary bending stress. If the 1.5 value isremoved from the values of C, the range of C values in the code adjusts toC = 0.15 to C = 0.5. Rearranging Eqs. 10.8 and 10.9 into the same form asEq. 10.10, we see that C : 0.15 through C : 0.5 encompasses the two ex-hemes from fully fixed edges where C = 0.188 to simply supported edgeswhere C = 0.309.

The low value of C : 0.15 in the ASME Code is for a special head-to-shellconfiguration with an inside comer radius of at least three times the headthickness. The structural effect of this edge condition results in reducing theequivalent pressurized diameter on the circular flat head from the normal di-ameter d to a diameter of 0.893d such that the Eq. 10.9 becomes

o=orssp(o8e'il=r"(il (10.11)

IO.5 BOLTED FTANGED CONNECTIONS

The most usual type of joint for easy assembly and disassembly used in theprocess vessels and piping system is the bolted flanged connection. A convenientmethod to design and calculate flanges with ring-type gaskets that are within thebolt circle was first published by Taylor Forge in 1 937 .

3 These rules were furtherdevelopeda and incorporated into the ASME Code, VI[-l, some years later.These rules, which are still used to calculate this type of flange, are in Appendix2 Of thE ASME COdC, VIII.1.

Rules for calculating flat face flanges with metal-to-metal contact outside ofthe bolt circle are given in Appendix Y ofthe ASME Code, VI[-1. This designincorporates a self-energizing-type gasket such as the O-ring gasket. fhe origi-nal rules were restricted to analyzing identical pairs of flat face flanges. Currentrules have been improved to permit analysis of both identical and nonidenticalpairs of flanges.

Further development of design rules in the ASME Code, VI[-1,5 came withthe issuance of reverse flange rules that use a ring-type gasket with no additionalcontact of the faces. These rules were added to Appendix 2, ASME Code,VIII-I.

In addition to these rules for flange design in the code, many designs are usedin which rules are not in the ASME Code. One common type is the full-facegasket flange. There are many others that may be designed for ASME Codeapproval by meeting the requirements of U-2(g) of the ASME Code, VIII_I.

Before any flange design calculations are performed for a vessel to be ap_

I0.6 CONTACT FACING 279

provcd according to the code the dcsigner should recognizc th t s(nr1c calculltions can be avoided. If the flange is the type described in Appentlix 2 ol thcASME Code, the code permits using flanges with recognized standards thatcstablish items such as dimensional standards, materials, and pressure/temper-ature ratings. The code accepts flanges designed to ANSI 816.5 .,pipe Flangesand Flanged Fittings,"6 API 605 "Large Diameter Carbon Steel Flanges",T andANSI 816.24 "Bronze Flanges and Fittings, 150 and 300 lb,'.8 Several otherstandards are not included; however, when the flanges are selected by thismethod, no additional calculations are required to satisfy the ASME Code.

When calculations are necessary according to Appendix 2 of the ASMECode, VIII-I, for a nonstandard design or when it is desired to upgrade astandard flange, similar design calculations are required for blind flanges (circu-lar flat heads with bolts) and for regular bolted flanges. Although each item isdiscussed in geater detail in the following paragraphs, the basic steps in de-signing a flange are as follows:

l. Establish design pressure and design temperature.2. Select gasket material and dimensions and facing type. Calculate N

and b.3. Calculate loads for both gasket seating and operating conditions.4. Determine bolting sizes and gasket width check.5. Establish flange dimensions (usually using those from a standard flange).6. Using loads and dimensions, calculate moments for both qasket seatine

and operating conditions.7. Determine required thickness of flange.

10.6 CONTACT FACINGS

For ring+ype gasket design as given in the ASME Code, VI[-I, Appendix 2,several types of flange facings are used. Some of the more usual types are theraised face, the tongue-and-groove, and the lapjoint. When these types are used,the full seal loading is taken by the gasket because no other part of the face isin contact with the adjacent face.

In addition to the types of facing where the gasket must carry the seating load,one type of closure and facing depends upon the adjacent faces to be in contactwith each other, but it does not require a large seating load for initial sealing.This kind of closure is used on both the ring-type gasket design of Appendix 2and the flat face flanges with metal-to-metal contact outside the bolt circle asdescribed in Appendix Y ofthe ASME Code, VIII-1. This construction utilizesa self-energizing or pressure-actuated O-ring gasket that is internally pressurizedto seal the gasket and does not depend upon initial gasket seating by the boltsthat cause compression of the gasket (Fig. 10.6).

There are also special types of gaskets and facing designs that become self-

Page 150: Process Equipment

ETIND TTANOES, COVTR PIATIS, AND IIANOES

FACING DETAILSo. Sell

Energizing

O.Rin9

b.

/'' -)/ l\Cold tr.t.t Finbi

Met.llic

4\T-

Ring JointGroove

,,.-1.n o/y %F*\ b=, I \-1\__r/T;'l-\-l

Wirh SearingNubbin

Figur. 10.6 Typicol Gocing d.roil..

sealing frorn the gaskets rotation and deflection that are caused by contactloading ftom a retaining ring and head closure. Some of these are called the deltagasket as used in Bridgeman closures, the double cone gasket, and the wedgegasket. In all these cases, the initial gasket seating load is low. As the pressurein the vessel is increased, the gasket rotates and deflects into a special facing inwhich the sealing load increases as the pressure increases. Care must be takenwith this type of closure because the gasket often "seizes" and it may be difficult!o get the closure apart. In many instances, the gasket may be silver, gold, orplatinum plated to help prevent the "seizing."

Delta R ing

Ring & BevelCold WaterFinish

Lap Joint

10.7 GASKETS 281

r0.7 GASKTTS

A large variety of gaskets is needed in process equipment. The diverse pro-cesses, temperatures, pressures, and corrosion environment require gaskets withdifferent configurations, materials, and properties. Some of the frequently used

gaskets are:

l.t3.4.I

6.

7.

Rubber O-rings

Metallic O- and C-rings

Asbestos

Flat metal

Spiral wound

Jacketed

Metal ring8. High-pressure type

10.7. I Rubber O-Rings

These gaskets shown in Fig. 10.7a are used extensively in low-pressure applica-tions such as storage tanks and air receivers. They are normally confined in agroove to prevent exhusion and their maximum temperature limit is about250'F. Because the required seating stress is negligible, the number of boltsneeded in the flange is kept to a minimum. A groove finish of 32 rms is usuallyspecified.

10.7.2 Metollic O- ond C-Rings

The metallic O- and C-Rings in Fig. 10.7b and c have a wide range of applica-tions for both extemal and internal pressures. They have a good springbackcharacteristic and a low seating stress. The gaskets may be manufactured fromwidely selected matbrials compatible with the flange. This eliminates the prob-lem of thermal expansion between the gasket and the flange and increases theirapplicable temperatue range.

O- and C-gaskets seals along a contact line. Accordingly, a finish of about32 rms is needed in the flange seating surface to properly seal the gaskets. Incritical applications a silver plating is specified to help sealing.

The O-rings manufactured in ftree different styles shown in Fig. 10.7c are theunpressurized, pressurized, and vented types. The unpressurized one is used athigh temperatures whereby the increased pressure from the sealed gas cornpen-sates for the loss of strength. The vented ring gasket is used at high pressures

for better sealine.

Page 151: Process Equipment

EtIND TTANOIS, COVER PIATES, AND TI.ANOES

10.7.3 Compressed Asbestos Goskels

'fhese gaskets in Fig. lD.1d normally consist of 707o asbestos, 2O7o ntbberhinder, and l0% filler material and curative. They can be cut to fit various shapes

und configurations such as heat exchangers with pass partitions and oval andsquare openings. Thicknesses are normally fumished beween fr and i in' and

rcquire a seating surface finish of about 250 rms. Asbestos gaskets are normallyused for tempemtures up to 850T. A rule of thumb for determining the adequacyof Nbestos gaskets for a given temperature and pressure is to limit the productof temperature in T times the pressure in psi to about 300,000.

ITilll I

_)l(a) Rubber O-Ring

tressurized tessurized

I7I Htr)t )tO- Ring

(d) Asbestos (e) Flat Metal

figur. 10.7 lypo6 of oq.kcls.

r0.7 oAsKtTs

Fisu.. lO.7 TyF of solk6b (conrinu.d)

10.7.4 Flqt Melol Goskets

These gaskets (Fig. 10.7a) are made from a wide variety of materials that canbe cut from sheet metal to any desired configuration and width. Some frequentlyused gasket materials and their temperature limit are:

Material Max. Temp. ('F)

IpadAluminumBrass

Copper

212

400

500

600

(t) sp iru t

Page 152: Process Equipment

800

900

1000

1200

1200

1200

1500

1500

1800

*l Tt1l q".9,: need a high searing force for proper seating. Accordingly,tney are best-suited for high-pressure applications . The seating stirface must havea finish of about 63 rms.

S€rated gaskets require a smaller seating force than flat gaskets and thus areused in screwed flanges where friction forces are to be miiimized.

2t1 IUttlD ttaNots, covER ptaTts, AND FtaNors

Materiul Max. Temp. ('F)

Titanium and zirconiumCarbon steel

Monel400 series stainless sieelNickelInconel

300 series stainless steel

IncoloyHastelloy

Lens

Double Cone Bridgeman(i) High Pressure

Fisure 10.7 TyF! of golkei! (conrinud)

r0.7 oASKETS 285

10.7.5 Spirol-Wound Goskels

Spirul-wound gaskets (Fig. l0.1f) are very versatile and used in numerousnpplications. They are especially suited for cyclic conditions where the excellentnpringback makes them ideal for repetitive loading. They:ue manufactured toI rlcsired width by spiral winding a preshaped metal strip with a filler materialbctween the strips that consists of asbestos or teflon composites. Asbestos-filled

Iuskets are limited to temperatures of 850T, whereas teflon is limited to 500"F.For most applications spiral-wound gaskets are retained in a groove. In raised

luce flanges, an outer ring is used to prevent the gasket from extruding and thet:hevrons from excessive deformation. Sometimes an inner ring is also used torninimize erosion and to reduce temperature fluctuation in cyclic conditions.

Many factors affect the performance of spiral-wound gaskets such as tightnessof wraps, material of filler and strips, height of strips, diameter of opening, andsurface finish. The gasket seating surface finish is about 125 rms.

10.7.6 Jockeled Goskels

'these gaskets in Fig. 10.79 are normally used for pressures up to 500 psi in largediameter vessels where flange out-of-roundness and tregularities are large com-pared with small flanges . They may be purchased as plain or corrugated and theyseal at the inner and outer laps. The outer metal jacket are made from a widevariety of metals. The filler material is normally made of asbestos, teflon, ormetallic. The asbestos filler limits the temperature application to about 850'F,whereas the teflon is limited to 500'F. The metallic filler is used at the hishtemperatures. The seating surface finish is about 63 rms.

10.7.7 Metol Ring Goskets

The metal ring gaskets shown in Fig. l0.1h are used in high-pressure andtemperature applications. Their small cross-sectional area makes them ideal forcompact flanges. The required high seating stress has the same magnitude as thepressure stress. The rings are made from many varied materials and are some-times silver plated to improve sealing. The gasket groove finish is about 63 rms.

| 0.7.8 High-Pressure Goskets

I€ns, delta, double-cone, and Bridgeman configurations shown in Fig. 10.7icomprise the majority of the pressure applications where the seating saess isrequired to be low due to physical limitations of bolt spacing and flange width.They are used extensively in pressure vessels operating above 1000 psi and aremade of softer materials than the seating surfaces to prevent damage to theflanges or covers. In general, these gaskets are expensive to fabricate and

Page 153: Process Equipment

216 IIIND 'IANOIS,

COVIR PIATES, AND TTANOES

m1lchinc; rcquirc vcry tight k)lerunces; and need very smooth seating surfaces of16 rms or better.

. High-pressure gaskets have a large surface that is subjected to the vessor

ll,.e.rnall pr:r*t::.

+ccordingly, a free-body diagram is no-ully n"""rrury rodetermlne the additional forces transmitted to the flanges and boltjresulting frompressure on the gasket.

The individual design requirements for lens, delta, and double-cone gasketoare given in the next three sections.

10.7.9 Lens Ring Goskets

The lens ring- gaskets in Fig. 10.8 are normally used in small flanges. Thc

:f:r.-::"j^",:1T19j ttg rins. through points a to b, must be equal to or larger

f:_T::i1t-Tl "f p: flanc: !o pyent crushing of the gasket. Thus knowingIne nslde-dameler of the gasket and the required bolt area, the outside diametercan be calculated from

oo =llr,+ (D),]'/

where OD : outside diameter of ring gasket (in.)

ID = inside diameter of ring gasket (in.)

Aa = actual bolt area of flange

5-

fcl"r16

Figur. 10.8 t.n. so3k6t,

10.7 oASKETS 287

l'hc outside thickness of the gasket is established to allow tbr an 0.25 in.clctrirnce plus 0.0625 in. for a centering ring, ifrequired. The pitch diameter lbrgrskct seating reaction is established as

c=(rD)*1(oo-ro)3

whcre G = diameier of gasket reaction.'the spherical radius of the gasket surface is taken as

p=G/z" sin 0

where R : spherical radius of gasket surface (in.)

I : angle of friction (for mild steel, it is 20")

l.'rom the geometry, the inside thickness of the flange is calculated from

where t = inside thickness of gasket (in.).The width of gasket seating is normally

(At(1.s)(design bolt stress)

z(GX3)(yield shength of gasket material)

where N = gasket seating width (in.).Figure 10.8 shows the flange and cover surfaces at the vicinity of the gasket

machined to have a slope of 20'.

10.7.10 Delto Goskets

The delta ring gaskets in Fig. 10.9 are extensively used in the United Staies forhigh-pressure applications. These gaskets rely on the inside pressure to wedge

them in the gasket groove for sealing and thus do not requhe any initial seating

or bolting shess. The general dimensions that are shown in Fig' 10.9 apply to

rings of all diameters. The pitch diameter G is normally taken as

G=ID+0.125

and tlle gasket seating width N is usually equal to 0.125 in.

t=:-+)l' 16 -l /ODYI- \, i I

Page 154: Process Equipment

IIINO II.ANOIS, COVER PI.AT!S, AND FTANOES

Figur. lO.9 Dclto go!k6t.

10.7.1| Double-ConeGoskets

Double-cone gaskets are very popular in Europe and can be fabricated in variousslzes. A typical detail is shown in Fig. 10.10. The required cross-sectional areais given by

f t 1tl2OD = l:A, + (rD),

IL1r Iwhere OD : outside diameter of gasket (in.)

ID : inside diameter of gasket (in.)

A, = actual bolt area of flange (in.r)

10.7 oasKlts

The seating length N is determined from

and the pitch diamet€r G is expressed as

G=OD-0'5N

The height of the gasket is usually set so that the net pressure force does not

exceed the seating force. Thus,

Figur6 '10.10 Doublo-cono gosk6t.

(cos 60)(aXc)(3)(yield strength of gasket material)

tzxrr(|)<,- 60) = (P)(,r)

Page 155: Process Equipment

290 ITIND IIANOIS, COVTR PI.ATES, AND TIANOES

' - (rXN)(sin 6o)--- P

where I = seating stress of gasket material (psi)

P = internal design pressure (psi)

10.7.12 Gcsket Design

!a1f1t.fei1e,_r cnaraderistics depend upon the material and the design of the

gasKet rtself. -fhe gasket faclor m and, the minimum design seating sEess )l irre

P^l:':j:o,ro th: cTk"jjlry and the gasket marerial. flrhou;h-the rn and ytactors have been in the ASME Boiler and pressure Vessel CodJsince the 194iedition, they are suggested values only and are not mandatory. The originatiesting and development of the m and y factors are described ln an articii UyRossheim and Markle that does not give the underlying background for thespecific.values. V9ry

_fu* changes have been made to ttiese faciors since theywere originally published.

.A.s the

-result of many inquiries to the ASME Code Committee regarding the

validity of the m and J factors, a large-scale investigation has been undertakenby the hessure Vessel Research Committeero of the frelding Research Councit.As experimental tests progressed, it became obvious that thJrz and y factors are."J1t"9 t" many items not previously considered. There is a closJ corretationwith the amount of tightening of the bolts, the gasket type, and the material, forthel are all related to the leakage rate of the j-oint. "

.g.nc-e the_gasket tlpe and material have bCen selected, the effective gasket

width for cabulation may be determined. For solid flat metal and for thJ ring_type joints' the basic gasket seating width bs is found by the formuras rn columnI of Table 7-5.2 of the ASME C;de, VI[_l, whereas for all other types ofgaskets' ba is delermined by the formulas in column rI. The effective gasketseating width D is found by applying the following rules:

D=06 when bo = iin. b: O.slbo when De )|rn.With D deiermined the location of the line of gasket load reaction can bedetermined as well as the values of G and h6 for calculating flange moments.

.ln designing a flange, it is important to recognize that two'desiln conditions

cxrst-the gasket seating and the operating conditions. Gasket seattg conditioncxlsts when an initial load is applied by the bolts to seat the gasket at ambienttcmperature with no intemal pressure. The minimum initial biolt loaO is

W"e = tbGy (10.12)

r0.7 GASKETS 291

'l'he operating condition exists when the hydrostatic end fbrce from the internal

dcsign pressure tends to open the joint, for the gasket retains enough resiliencyl() keep the joint tight. Loadings and stresses are determined at design pressure

rund design temperature. The loading for the operating condition is

W.t: H + n,:f,C'zp + mGp(Zb) (10.13)

To avoid crushing the gasket in those bolted flanged connections where the

gasket is carrying all the loading, it is recommended that the initial loading does

not exceed the gasket seating stress y. Once the actual bolting areaA, is selecied,

a check may be made to determine the required minimum gasket width by the

fbllowine formula:

N^"=ffi (10.14)

Example 10.5. A vessel has the following design data: design pressure

p = 250/U.. psi; design temperature = 250'F; a spiral-wound metal, fiber-filledstainless steel gasket with an inside diameter of 13.75in. and widthN = l.0in.The gasket factors are m = 3.0 and y = 10,000. Bolts are SA-325 Grade I with& = Sa : 19,200 psi. Is the gasket width sufficiendy wide to keep from crush-

ing out?

Sohttian. Determine the effective gasket seating width as follows: N =1.0 in., b" : N/2 = 0.5 in., b = 0.5!bo = 0.3535 in., effective gasket di-ameter ls

G = 13.75 + (2 x 1) - (2 x 0.3535)

G = 15'M3 in.

Gasket loadings are

H : o.785G2p: 0.785(15.043F(25N1 = 444,1ss

H,= 2brGmp = 2(0.3535)r(15.043X3X2500) = 250,600

Wa : H * He = 444,1A0 + 250'600 : 694'700

W^z: rbGy = z(0 3535)(15.043X10'000) = 167,100

Since fi = Sa : 19,200 psi, W.r sets the bolting arca A^ as

A^=Y# = 36.182in.,

Page 156: Process Equipment

292 IUND ftANOrS, COVIR plarrs, AND FtaNots

AD = octuul bolt {reu = 36.ti in.2 lbr l6-2-in. diumeter bolts. Minimum gaskctwidth is

.. 36.8( 19.200)fl^" = zlq000).(15.0a, : 0 748 in versus I in' actual

One-inch wide gasket is sufficient to prevent crushing. fPmblem

10.5 A solid, flat, stainless steel gasket with 'l2

: 6.5 and y : 26,000 is usedin the vessel described in Example 10.5. The preliminary gasket insidediametef is 12 in. and the gasket width is 1.0 in. whai is the easketseatine load?

Answer: W,,2 = 384,000 lb

IO.8 BOTTING DESIGN

In designing bolting for flanges, the initial item is selecting the bolting matenal.It must be a malerial compatible with the flange material . ihat is , there musr norbe any chemical or galvanic action between the bolting and ffange material thatwould cause the bolts to seize in the tkeads. Under certiin circurn'stances, rt maybe necessary to plate the bolts or to make them from special material to prot€;tthem from the environment. Although it is not neceisary to select a 6oltingmaterial with a tensile shength close to that of the flange material, one shouldcarefully consider the effects of strain elongation and rehxation of boltingmaterials that have a high tensile strength and requte a smaller cross-secdona'iarea.- In addition, when high sFength material is used for the bolting, care mustbe taken not to rcduce the number of required bolts to such a small

-number that

excessive bolt spacing is developed. r I

Wlren the bo_lt spacing exceeds (U + t), secondary flange bending is devel-oped between the bolts to the extent that it affects the ;ormal flange bending . Toaccount for this effect, the flange bending moment M0 must be iricreased by theIactor

(10.l5)

where d = nominal diameter of bolts (in.)

t : flange thickness (in.)

To detennine the total required cross-sectional area of bolting, both the gasket

actual bolt spacing

10.8 BotT|NG DESTGN 293

scnting and operating conditions must be examined.The minimum required bolting area A, is th€ greater of

W.z

s, otW^r

Sa

where & : allowable bolting stress at room temperature (psi)

S1 = allowable bolting stress at design temperature (psi)

W.1 = operating load: H + H, (see Eq. 10.13)

1Y.r = gasket seating load

From this minimum required bolting a;ea A. the actual bolting area A, is

selected. In order to obtain a bolt loading for calculating moment for gasket

seating, the minimum required bolting area and the actual bolting area are

averaeed as follows:

w:0.5(A.+Ars" (10.16)

Certain times during the operation of a process vessel the bolts in a boltedflanged connection are subjected to actual stresses in excess of the allowabledesign stresses. This may be especially true during hydrostatic testing. Caremust be taken to enswe that during this testing, no permanent elongation ofthebolting has occurred. If so, the bolting may have to be replaced before the vesselis put into service. Realizing this is especially important if each of two suppliersprovides half of the bolted flanged assembly and one does not know what boltingis supplied.

Example 10.6. A vessel flange uses 16-2-in. diameter bolts. Flange sfresscalculations indicate that a flange thickness of t : 4.5 in. is adequate. The boltcircle diameter is C = 22.5 in. Will secondary bending stresses be developed?

Solutian. The maximum permissible bolt spacing without a penalty is(2d + t1 = (2 x 2 + 4.5; = 3.5 in. The actual bolt spacing is

rd _ n(22.5\1V -]6- = +Az n.

Because the actual spacing is less than the rnaximum spacing without a penalty,no secondary bending shesses are developed. I

Example 10.7. Suppose a vessel requires Z-2 j -in. diameter bolts on a flangethat is 5.5 in. thick. What is the madmum bolt circle that will not causesecondary bending shesses? The minimum bolt spacing for 2 j -in. diameter boltsis 5i in.

Page 157: Process Equipment

294 lutito ftaNolg, covER ptATEs, AND frANOrS

Solullon, Maximum spucing is

(2d + t) = (2 >< 2i + 5.5; = 19.5 tn.

Diameter of bolt circle is

lo'5 x 24 = 80.2 in.n

based on maximum spacing. I

Problems

10.6 Sixteen bolts at I l-in. diameter are io be located on a bolt circle ofG = 32 in. The flange is 2+ in. rhick. What is the factor rhat is due tosecondary fl ange bending?

Anstrer: l.l2

10.7 The minimum spacing for the wrench to fit I |-in. diameter bolts is 3 | in.Twelve bolts are to be used on a bolt cide of 15l-in. diameter. What isthe minimum flange thickness that does not cause secondary flange bend-iog?

Answer: 1.0 in.

IO.9 BTIND FTANGES

The minimum required thickness of a cicular, unstayed flat head or blind flangeattachedty bolts and utilizing a ring-type gasket that causes an edge moment isderived from the assumption that the flat plate is simply suppofted; the gasketload line G and is loaded by a gasket seating load or a combination of easketloading and a uniform pressure loading . The combination of these loadingJat thegasket and at the bolt circle causes an edge moment ofMg/zrG, as shown-in Fig.10.11. ff the edge moment ffi is assumed to be equal ta Wh", tlre theoreticalstress at the center of the flat plate is

" _3(3 + tt)p (GY + 1 /wrrc\"- :z F)-"G\-F) (10'17)

Sening trc = 0.3 and E = weld joint efficiency within the flat plate,

sE:(*rye\-r..(W) (10.18)

IO.9 BI.IND FTANGES

H

)Fisurg lo.l I loodings on blind flons€.

Solving Eq. 10.18 for r gives

(10. r9)

This is identical with the equation in the ASME Code, VI[-l, except that theconstants of 0.3 and 1.9 are used in the code instead of the exact constants of0.31 and 1.91 and the gasket load G is substituted for d. The general ASMECode equation for circular flat-bolted heads is

,:oJgll\, *t'n-LYl',

t=G (10.21)

For operating condition the intemal pressure p as well as the gasket loading areapplied. For this condition, Wr : H + Il, at operating temperature with anallowable tensile stress of S1. The equation for operating condition is

(10.20)

For the gasket seating condition, the internal pressure equals zero and the onlyload is the gasket seating load W" at ambient temperature with the allowabletensile stress of S.. The equation for gasket seating condition is

Page 158: Process Equipment

Figure 10.12 shows a sample calculation of a blind flange.

E-xample_ 10.E. Considering the pressure vessel described in Example 10.5,the vessel is to have one end closed by a blind flange. What is the minimumrequired thickness of the blind flange? Design data are the following:

296 ITIND ?LANOI3, COVTR PLATIS, AND FTANOTS

t=G

Design pressure p = 2500 psi.Design temperature = 250'F.Flange material is SA-105.Bolting material is SA-325 Gr. lNo corrosion exists.Allowable bolt stress at gasket seating19,200 psi.

Allowable flange sfress17,500 psi.

(t0.22')

and operating conditions =

at gasket seating and operating conditions =

Gasket is spiral-wound metal, fiber filled, stainless steel, 13.75 in. insidediameter times width N = I in.

Solution. Following the information calculated in Example 10.5, once theactual bolt area A, is found, the design loading for the gasket seating conditionW, can be determined as:

W: 0.5(A^ + Ar)S, : 0.5(36.2 + 36.8X19,200)

% = 700,800

The moment arm is determined from

hc = 0.5(C - G) = 0.5(22.5 - 15.043) = 3.729 in.

fJgt Pxample 10.5, the design loading for operating condition is lll.r =694,700.

. The minimum required thickness is determined as the greater thickness of thatdctcrmined for gasket seating load according to Eq. 10.i1 or for operating loadrrccording to Eq. 10.22.l.i)r gasket seating,

_ ll.gwhc .__.. I t.9(700.800x3.729), = uV s,uoi = ts.o+:{ffi :4.343in.

0.3p | .9W,,1ha;

s"E - -srEcl-

t0.9 EUND FTANOES

For operating condition,

t:GrF

t = ls.(Ml.v 17,500 x 1.0 (t7,500 x 1.0x15.043t

Therefore, the minimum required flange thickness is t : 5.329 in. I

Problcms

10.8 Suppose the flat head in Example 10.8 is made by butt-welding flat platestogether. The welds are spot examined so that E = 0.85. What is theminimum required head thickness?

Answer: t, n = 5.780 in.

x -crr/. - 41{,12t. -,51c - d - ,-'12

l. OO, l..iir dillina. C.|l.1-+6. 6 l4hlig

2. Xc .addj.el rfiktid. I '.{ft.d l, l.d.!

3, Ud{ or[.Rin rF..tjrd, l!.G .l $r'l 0..!.Br b. d.ri..d .nt d.. .r- '.i!lni lo'

Fisur€ 10.12 Elind flonge romple colcolorion sh€€|. (Courrery G+w roybFBonney Div., Toylor Forge.)

O.3p , |.9W.rhcsrE- - s"EGt

Page 159: Process Equipment

298 IIIND IIANOIS, COVER PLATES, AND TLANOES

10.9 Suppose the bolt circle diametsr is incrcused ro C = 24 in. What is thcminimum required head thickness considering both gasket seating andoperating conditions?

Answer: tnn^ = 5.671 in.

IO.IO BOTTED FTANGED CONNECTIONS WITH RING-TYPE GASKETS

The design_rules for bolled flanged connections with a ring+ype gasket that isentirely within a circle enclosed by the bolt holes and with no iontact outside of

, Wh€n it is necessary to design a bolted flanged connection because no stan_dard flange of the proper size is available, the standard pressure/lemDeraureratings are not adequate, or sperial design factors are to be used for the gasket,the procedure in Appendix 2 of the ASME code is used. The design of nanges,bolting, and gaskets by the ASME Code rules is essentially a ftal_and-enorprocedure where some dimensions are set and remain fixed, whereas otherdimensions such as the flange thickness are varied. Stresses in the flange and thehub are calculated. If any of these shesses exceeds the allowable tensile stresses,a "new" flange thickness is selected and the stresses are recalculated until theyare satisfactory. The trial-and-error method is essentially due to the compleitheory used by Waters, Rossheim, Wesshom, and Williams to solve the problemin the original development. The WRWW method, which was ultimatelv incor_porated into the ASME Code in 1940, is ar elastic analysis of the intiractionbetween the vessel or pipe, the hub, and the flange ring assembly. The shell andhub are resolved by a discontinuity analysis that was previously described inChapter 5 and the flange ring is considered as a flat plate with ihe center Dartrcmoved (Fig. I0.13). Interactions of rotations and deflections are oermiiteduntil lhe balance is obtained.

. The basic assumptions in the analysis are that the flange materials are elastic,that is, no creep or_ plastic yield at lower temperature ocJurs, the bolt loading iiassumed or determined from the gasket factors, and the moments due to loadinssare essentially constant across the width ofthe flange. In addition, rotation of tie

IO,IO sOTTED fI.ANGED CONNECTIONS WITH RING.TYPE GASKETS

I ) (l| ) (llr

(a) Moment Loadlng

(b) Direct Loadlng

t-t+ f+.llrr,-ri'r'roIllll.l-----v------J

'tt 0z(c) Combined Loadlng

Figure '10.13 Flongo loodin$ for alo:ric anolysii.

flat plate is assurned as linear with no dishing effect and superposition is accept-able.

The solution of the complex problem is simplified for code use by cwves,formulas, and tables that contain constants depending upon the geometry of theflange assembly. Formulas for various coefficients are given in the code thatpermits cornputer programming of the basic equations for rapid solution.

The code designates flanges with ring-type gaskets to be three types for

Page 160: Process Equipment

EIIND FTANOIS, COVER PLATES. AND FTANOTS

Bnalysis: int€grsl, loose, und optionul. lntegral means that the pipe, hub, andring are one continuous assembly from their original manufacture as eithcrforging or casting welded together by full penetration welds. lnose means noattachment of the assembly to the pipe or no ability of the juncture to carry sheafsand moments other than those required to seal against pressure. These types offlanges are called slip-on, lap joint, and threaded, and they may or may not havchubs. Optional means flange designs that, by construction, are integral, but thcanalysis is permitted by the simpler method for loose-type flanges. Examples ofthese various types are depicted in Fig. 10.14.

The calculation of a flange with a ring-typ€ gasket first involves selecting thematerial for the flange, bolts, and gasket in a manner very similar to the blindflange. Next, the facing and gasket details are set, the loads due to intemalpresswe are determined, and the required bolting area and bolt sizes are selected.The bolt circle is then decided; and the loads, moment ams, and moments dueto both gasket seating and operatihg conditions are determined as with the blindflange. By knowing these and the geometry used to determine K and other hubcoefficients, stress calculations are made for both conditions. The longitudinalhub stress, the radial flange sness, the tangential flange stess, and their variouscombinations are comparcd with allowable stresses.

The method of calculation is virtually identical for welding neck flanges andslip-on or lap-joint flanges except that the axial pressure load is applied at aslightly different location. For the ring flange design, the tangential flange stressis the only one calculated. The minimum required thickness can be directlydetermined from

(10.23)tM*V s-B

,..IExample 10.9, What is the minimum required thickness of a welding neckflange as shown in Fig. 10.lzla with the following design data? (Nore.' These dataare the same as those used for the blind flange in Example 10.8. In Fig. 10.15is a sample calculation of a welding neck flange.

Design pressure, p. = 2,500 psi.

Design temperature = 25O"F.

Bolt-up and gasket seating temperature = 70'F.Flange material is SA-105.Bolting material is SA-325 Grade 1.

Gasket details are spiral-wound metal, fiber filled, stainless steel, insidediameter is 13,75 in. and width is 1.0 in.

Solutinn

1. Allowable bolt shess at design and seating temperatufes = S, =19,200 psi.

I6

IO.IO BOTTTD TTANGED CONNECTIONS WITH RING.fiPE GASKETS 301

I

FE--d *--'t1+

(.)

tr=-tr_rel \__

(d)

IT l-T

9t 12 l9lt\A 9 j 12

(s)

Opii.nrl lYF. Fl.n96.Th6. M.y b. C.ldl.r..t.r Eirh.. Looro.or Inr.9..t.Typ.

(i) (i) (k) (1)

Figur6 lo.l,t Typer of flonger. (Courl,ely Americon So.ieiy of Mechonicol Engin€.rs, from Fig. 2-.1 of theASME Cod., Vlll-I.)

2. Allowable flange sfress at design and seating temporatures = S/ =17,500 psi.

3. Gasket dirnensions are

b.= N/2 = 0.5in. and b=0.5Vro=0.3535G = 13.75 + (2 x l) - (2 x 0.3535) = 15.M3 in.

{-..*,o

(h)

Page 161: Process Equipment

302 BTIND fI.ANOES, COVER PIATES, AND FLANGES

'r= 13.154

Io-:". I P;Pe s'zera't L. tza

B = to.7t "

c. 2t,5'

t6- 7"' eot::s -

Figure lO.l,C(d) Flons€ dim€Bions ior Ex. 10.9.

Determine bolt loadings and sizing of bolts with N = l; b = 0.3535;y= 10,000; m=3.0.

, : Xo,, = 2|o5.o43)'z(zsoo) : 444,323

H, = 2btrGmp = 2(0.3535)zr( 15.043X3.0X2500) :250,591 ,Wa = H + Ho = @44323) + (250,591) = 694,914

W^z = nbGy : z(0.3535)(15.043X10,000) : 167,060

A. = the greater of W f Sbh : 694,914) /(19,200) = 36.2 in.'z

or W,ef 56" = 067 ,0ffi) /(19,2C0) : 8.7 in.'z

Aa = actual bolt area = 36.8 in.'z 16 bolts at 2-in. diameter

W.: 0.5(A^ + Ar)Sr. = 0.5(36.2 + 36.8X19,200) : 700,800

Wo=Wa=694,914

Calculate total flange moment for the design condition.

Flange Loads

a, : XB'p :

!{ro.ts)'{zsn) = 226906

He = Hp:250,591

Hr : H - Ho : 1444,3231 - Q26906) = 2r7,4r7

Leaer Arms

hp=R+'0.591 = (2.5) + 0.5(3.375) = 4.1875

h= 6'at

I

I

4.

hT

I orrron coxorrronr

lltr

a.115 '

t0.75 "

l6 - 2"toont t r. a41'

Figuro lo.l5 weldins neck flonse sdmple colculotion sheet (Courtesv G+w Tovlor-Bonnev Div ' Tovlor

Fors..)

J7i.^l u."^L azl-1,l;ber fi//el,s u/eer tt"elrl t5 t.o. i t" ",tt

/e'

Ac =,5lc -6r = t.1L

rc =.5(c - cr - t71'65

.s(s, + srfq .5 {sr + srl =

.5lsi + s,lr.5lsx +5rl = 13. oO

= 1/3t.+t = Z.o

lf Lh i9oc., no..g ro + t .uttiptE .il .. lr .6or au.rld b,

Cdrvnd- D.+

Crxt.a-- tt'i..

-

303

Page 162: Process Equipment

Itll'lD flANOt!, COVIR p[Arr3, Al,tD frANOrs

nr; - O..J(C * 6) = 0..5(22.5 - 15.043) : j12BS}r=0.5(R*g1 * ft6):0.5(2.5 + 3.375 + 3.7285) = 4.9613

Flange Moments

Mo = Hp x hD = (226,910)(4.1875) = g5g,17g

Mo- Hox hc= Q5O,5g0)(3.7285) : g34,33g

Mr = Hr x h, : (Zt7 ,420)(4.3018) = t,O43,gg}Ma" = Mo + Mc + Mr = 2,928,490

Calculate total flange moment for bolt_up condition.

Flange Load

He = W: 700,800

Lever Arm

hc=0.5(C-G):3.7285

Flange Moment

Mon= He x ft6 = (700,800)(3.7285) : 2,612,930

7. Use the greater of Md. or M6"g1/S); Ms = 2,92g,490.E. q}11pe consrants from the ASME Code, VI[-I, Appendix 2: K:A/B = Q6.s)/(ro.7s) = 2.16s. ^F,-":"

i,e..-i 7 i, "s"Ju'i uro-,,r = 1.35 z = 1.3e y : 2.2e ii : z.ii."*""^'sr/ go = 3.375/1.0 :3.275

h=Vrry'=V@jr1D=3.27sh/lro = 6.2s/3.2t9 = 1.906

From Fig. 2-7.2, Section VIII-I, I. = 0.57.From Fig. 2-7.3, Section WII_I, y = 0.04.From Fig. 2-7.6, Section WII-I;y = 1.g.

e = F/ho= (.57) / (3.27s) = 0.1738

d = (u /v)hoeT = e.s1 / .o4e.279)(t)2 = 2g5.76

9. Calculate stresses. Assume a flange thickness t = 4.5 in.L = (te + 1)/T + t3/d = (1.320) + (0.443) = 1.763

6.

IO.IO BOLTID FTANGED CONNECTIONS WITH RING-fiPE GASKITS 305

Lon g itudinal H ub Stre s s

sx = fMn/ LglB : (t)(2,928,490) / (r.763)(3.37 ra(0.7 s)

sa: !3,s70 q9!

Radial Flange Stress

s^= Qte + r)Mo/LtzB = <z.uzaf,s:x:rrii;li:..763)(4.s),Oo.7s)s" = lLsg-Q-pg

Tangential F lang e St e s s

g7: (YMs/t2B) - ZSa

= (2.29)(2,928,490) / (4. r, 00.7 5) - ( 1. 39X 1 5,590)

Sr = 9140 psi

10. Allowable stresses

56 < 1.5Sy: (1.5X17,500) = 26,250 >-11,10 pC)

Sa < Sr: 17,500 > 15,590 psi

$ < Sy: 17,500 > 9140 psi I

Example 10. 10. What is the minimum required thickness of a ring flange withthe same design data as given in Exarnple 10.9? The inside diameter has beenincreased to fit over the outside of the shell to where,B = 12.75 in. The boltloadings and bolt size are the same as in Example 10.9. A sample calculationsheet is shown in Figure 10.16.

Solution

1. Calculate total flange moment for design condition.

Flange Loads

H, = !oB2 p = X02l s),(zsn) = 31e,2oo

He : Hp = 250,600

Hr= H - HD= 444,300 - 319,200 = 125,100

Lever Arms

ho = o.5(C - B) = 0.5(22.5 - 12.75) = 4.875 in.

Page 163: Process Equipment

306 BTIND TI.ANOES, COVIR PTATES, AND FI.ANOCS

hc = 0.5(C - G, = 0.5(22.5 - 15.043) = 3.729 in.hr = 0.5(ho + hd = g.514.gr1 + 3.729) = 4.302 n.

Flange Moments

Mo = Ho x h": (319,26)(4.575) = 1,556,000

Mc = He x h6 : Q5O,ffi)(3.729) = %a,5ggMr = Hr x h, = (125,1N)(a.302) = 53g.26iMa" = Mo + Mc + Mr= 3,029,000

Bolt-up moment is the same as in Example 10.9, Muu = 2,613,000.Shape constants arc K = A/B = 26.5/12.75 = 2.078From Fig. 2-7 .l of tlrc ASME Code, Ylfi-l, Y = 2.812.Required thickness is based on design condition as

, : M*Y _ (3.029,000x2.812)

': iE = -1r21x1)@.n : 5'8e8 in r

t3.

4.

I 2 cerrn I r^oE!"., r zfoo ftL ssir.l ..:."d raf.l,

{itc v f;rl€dr stainl?r, jf.elItl'lD J( l'dii<

G. tr lt +QtD4r .'r<.A,B.ql

Korrcl focezrooFiA- to5

5A'tz6 GP.lroao AxD aott cltcuultoNS

litllapsi rv.' - 5,cr E i6'Lo6o

^- -a:j w-,/r q wi/s\- 9.1 4 tC.x, z 25tc^r: ZE O,5 tc @1."9

117., a';, H -efr/! - 4t14,tt. w =,!l^. + Ats. - 100,€ooJ1t wn-,r.+n- 6,j1,1t{

l.vlt arra

150 ,ti = rolb = tt5t6,096q.-*.t-h- zto,tq I It E.5t< - ct = 3.1295 ,14 = rdg = 934,j21tt,-r -i/!- lZ5)132- :.51 lD + ri.l = {.iol6 u' -8fi - t1a.79tv. = 1,028,618

- loorSoo A. =.rtc - cl - 2,1285 N. - 2,ctz,1r1

tb

6 tn^tr cof.3r^Nri r:^/. rz.o'18 r-- L^z_b.h p..hr .ro.c, 2. + ,.,Lnirtr /rdi;;Eclvr .!d n h '.qe.ri6r 5'| \J r" +-;-

,-,[x=r* @'={ *i.mi

adrd.d- Dd.-6.1.J-}lvib.r-

Figure 10.16 Rins llonse lomple col.ulorion sheet. (Court€sy c+W Toytor-Bonney Div., Toytor Forge.)

IO.I I REVERSE FTANGES

l'robhm

10,10 Suppose a solid flat 2j chrome steel alloy gasket with 13.75 in. inside

diameter and width N = Lin., m = 6.0, and y = 21,800 is used withthe flange in Example 10.9. What are the gasket seating and the

operating loads?

Answersz design condition is I7,' = 734,599 tO

seating condition is W^, : 244,rOO ,O

IO.I I REVERSE FTANGES

Rules for the design of reverse flanges are given in Appendix 2 of the ASMECode, VI[-1.5 This type of flange is often used to form a reducing joint. The

solution of the reverse flange is similar to that for the raised-face standard flange

with the ring-type gasket within the bolt circle except for some minor differ-ences. Figure 10.17 shows some loads that are applied in the reverse direction'

Rwer$ flonge looding ond dimen3ions.Fisurs 10.17

Page 164: Process Equipment

308 IUND ftANoxs, covrR puTEs. aND rrANG[S

'lhis muy cuuse sorns ol the moments t0 be applietl in thc opposite direction liomthose loads on a regular flange. However, the analysis is the same after thc"new" total moment is determined. Again, the moments arc determined for boththe gasket seating condition and the operating condition. In Figure l0.lg is asample calculation sheet of a reverse flange.

Additionally, a new term aa is introduced to convert some terms from reqularflanges io reverse flanges; fra and K are redefined and based on the reverse fl-anseinside diameter; and a new equation is added to calculate the tansential flaniestress at the inside flange bore.

A special precaution is noted. When K < 2, results are faidy satisfactory;however, when I( > 2, the results become increasingly conservative. For thisreason the ASME Code procedure is limited to where I< s 2.

Derivation of the new equations for reverse flanges is similar to that for theregular flange except shears and moments are applied at the outer edge of the ringflange where discontinuities occur between the flange ana *re truU. WittrK = A/B', the conversion term ca is determined for converting T, Il, and y toT,, U,, alrd If, which is obtained as

"=*['.*.#*)Substituting this expression into the regular equation for tangential shess

(1,0.24)

(10.2s)

Example 10.11. A reverse flange is joined to a regular ring_type joint flangeto form a reducing connection . The total bolt-up momint ls coitroiting anA equitto Ms = 2,613,W. The flange bore d, = 13.25 in.; the outside diameterA = 26.5.n.; and the flange thickness r = 5 in. What is the tangential flangestress at the hub and at the inside bore?

Solutian, The tangential flange stress 51 at the hub is

" _Mol,, zl.,z \jtr= *,zl+ - i\l* r*7it, = #*#f r.ut - fl(r* ] " s " o.r:r)l : szzopsitj.zJ\zJ) L 4.14\ 3 --/]

'fhe tangential flange stress Ji at the flange bore is

s+ = kly _zK'?(_t + gofB'f L (K, - l)i l

I Drt|ox coxofioxt

5/rr/ "t"-"/- 'a.tat,fi l. r {,t/el, t& ;ahs 4a//r.75't0 ' / ' ltde- -

Kai'ed {""e-

IOAO I llwt lr|| - l Or{t|.lt.=J(C+i'-23-t)=

r.r -,r'r' - _ I,Orl,tq lfi*r- x.t - t81,1o- zz 1q f. y't f

* - Z,trL'?V

r(5r+ s.)rJ(s' + e!) = 816EO ?e\

= I't,|o'l rtlr.ir. rta. 9r ( ! a') =?

rr = r:-rj.jb.t r = 0.957

I=.ch/d - Z5r loatr.+ l),,P=

4sr +tn.t 3l +n= qt6rlr".9, rrg, sr t^r r') = ff

t =./3r+ | = l.

Fisurs 10.18 Rwerse flonse somple colculotion she€|. (Courtesy G+W Toylor-Bonney Div.. Toylor Forge.)

309

Page 165: Process Equipment

ll0 luND ftaNots, covln puTrs, AND ItANOES

_ z(+Xl +lx5 x.(,. _ 2,6t3.(xx)L oar3.2s(25) L-'" #*itti = I6'o5opsi r

Example 10.12. With the reverse flange given in Example 10.11, what is theminimum required thickness based on an allowable flange stress of 17,500 psi?

Solutia3. The tangential flange stress at the flange bore of 16,050 psi iscontrolling. Because / appears in several terms in a no;linear manner, the easiestway to select the proper thickness is by nial and error. For the initial trial, usea square relationship as follows:

16,050 17.500--tl-: l1z- or t:48in.

The term ,\ is recalculated as 3.855. Using this, the .ti = 16,900 psi. Bysuccessive recalculations, the approximately correct thickness is , : 4.6g in.which gives Si: 17,500 psi. IPmhlcm

10.11 Using the details of the flange described in Example 10.11. what is theminimum required thickness if the material of the flange is changed to onewith an allowable stress of 15,000 psi?

Answer t-i\ = 5 -26 in.

IO.I2 FULI-FACE GASKET FTANGE

919 gp" ot flange that is frequently used but no design methods exist in the

lfME "C:* is the flange using a full-face gasket, as shown in Fig. 10.19.

Figure.10.20_ is a sample calculation sheet. This type of flange is designedaccording to the provisions of U-2(g) of the ASME Code, Sectiorivll, Divisionl. This code paragraph permits using good engineering design for those con-structions where no rules exist in the code. Although the analysis is similar tothat used for a raised-face , ring-type flange , a countermoment is introduced fromthat part of the gasket that is outside of the bolt circle. In addition, the decreasein section strengtl at the bolt circle from the bolt holes must be considered whenthe radial stress at the bolt circle is determined.

lmplolng this type of gasket is usually limited to designs where a ..soft,,gasket (with a low m and 1, factor) is used and the design prlssure is low. Thisis necessary to keep the loads and bolt size within reaso-n ti fit *ithin th" fl*n"geometry even though the countermoment usually results in a low flange mi_ment and a minimum required flange thickness.

IO.I2 FUI.L.FACT GASKET FIANGE 3l I

Figura I gosket loodin$.

Several important design assumptions made in the analysis are uniform gasket

pressure over the entire gasket, inner edge of flange assembly unrestrained, and

no reduction in gasket pressure area due to bolt holes. Other restrictions and

limitations necessary for the raised-face, ring-type gasket flange, such as linear

rotation about the centroid of the ring, prevail.Assuming a uniform gasket pressure, determinations are made of the dis

l-l_tA I

0.19 full-foce

Page 166: Process Equipment

312 tNo ttANots, covrR p[ATrs, AND FtANOIS

tonce$ or momcnt olTns lrom the bolt circle to the ccntroid of the annulus fromthe bolt circle to the outside diameter and from the bolt circle to the insidcdiameter. In solving for the distances, the angle is assumed to be small and thcarc lengths are evaluated as sfiaight lines. From Roarkr2 and using his termi-nology, the basic equation is

Horvever, converting to the terminology used in the ASME Code and as shownin Fig. 10.19a, the equation becomes

a-

b=

Therefore, substituting Eqs. 10.26b,

A_C

,=i(T#)

,, (A-C'^)(U+Cl- 6(A + C)

2

"^err,J

*(#)hL

c, d, and e, into Eq.

(lO.26a)

(10.26b)

(10.26c)

(10.26d)

(rO.26e)

lO.26a,

(10.27)

Fiour€ 10.19(0) Full-foce gosket dim€nsions.

3r3

I oraa.. corDmoxt 2

F'tt - F'.e ,/1eturtL.f 'be.z - |ltt=7 qrlE

5 to9

sA-rzt cv.l ro^0 aro fori calcul lo|trlj= 6tor + ti'.r = l,tq,tqQ

^- =ebcL'of wd/s. d w-Jt= 17., n )c.1b

Itt,=26ra6r = | 18,q86 ^,= N.A \^.2 t(.- z"Q tJte

tlEoo ftl trtD = t/tt.r1'

= 4 t r' 5 t1 w=tl .+^,1t.= 706,t16lr )qzoo Fi E=cnr/.= 1t,168 tr'at=r./:. ttc,= 94a, 4q6

14 reL wr'=tt +lt.r+t|'r = 7At,1l3I ltv ar

5 it - r)trl. - 1,'t,o4\ r. - r+ .5r, - tl,t 1 Pt-,d6- tZt,r72,tt-E-ED- 1L,17-4 |'-Jtr+.,+tEl - { Zt, & - rrir - l1{,,rO{

V. - ?t1,h.6

6 = !!:!E!-*9=- = 2.9915' (. =bg.4Lgl= = r.oz?2'

,.o=\a -l|.= LlAtSoa *" = h.L- = o. 11 f6 a.=8.t-t'= 1C4 tozL

8 t:* 3nls3 CIICULllDOT-€4din, 6 x er,o sur rrcrort16!, |kb, ti = nJIEI = 1tt 71 ?tar.rErFEgr: Pb/f - t1,71o ?,1r-r. tla 9=-.t/f -u.- ?,95':-j.5(5r+ s.l'Jl3r +5'l - q' ToL,?r L

'-i - 0 t118t/iDrrt 5trE$ al tolt oto.t..-:;iffi = n,qL4 ?,. .-lh&.'-20116t\I'ti;-,.217

16- 2"uotst t1.tt1"

/ nr.3s torMuta tactott

. -r.+l r l.:5t calak+r = l.4IO

-afi - t. ool l

, -.tla - O,o.lo1r -t+a - r,o1',

-=rL,rt - H?.l6

t br rp.d.. o....' 2. + r.*htrt l;EI 2.+l

C-r-a- Od.-

o.d.a- L'r.+

Figurc lo.2o Fvll-Goce flonge lomple colculorion 3ho6t

Page 167: Process Equipment

3I4 II.IND ?U\NO!S, COVER PTATTS, AND TIANOTS

ln a similar munncr, the distance or moment &rnt k)w&rd the inside diameter h1;is determined as

C_B -0"=+('!:'\5 \O + c /. C_Ba:

2

, = .r(?*)

,= *(?;And substituting Eqs. 10.269, h, and i into Eq. 10.26f gives

c-B

and solving for ft6 gives

(r0.28)

9n9" t"_*9 gasket loadings and two moment arms are determined, theanalysis of the flange is the same as for other flanges. The method is equallyapplicable to integral flanges, loose flanges, reverse flanges, and any othei typeof flange. It is important to remember to use a..soft,'gaiket that keeps tfre tottloading within acceptable limits.

Example_10.13. A welding-neck flange with the same geometry as that inExample.10.9 except for the thickness is used with a full-facJ gasket. The designpressure is 320 psi and the "soft" gasket is vegetable fiber with m = 1.75 andy = 1100. What is the minimum required thickness?

Solution

l. Determine the lever arms of the inner and outer parts of the sasket:

h. = G - B)(28 + C\ _ (22.5 - t0.75)\2 x 10.75 + zz.5)'" 6(8 + C) 6( 10.75 + 22.5\

-

(r0.26f)

(to.26s)

(10.26h)

(10.26D

6(10.75 + 22.5)

ha = 2.5915 in.

IO,I2 FUIL-FACE GASKET TIANGI 3I5

.. (A - c)(u + c) (26.5 - 22.5t(2 x 26.5 + 22.5)

6(C + A) 6(22.5 + 26.5\

hb : 1.0272 in.

Determine the gasket dimensions:

G = C - 2hc:22.5 - 2 x 2.5915 = 17.317 in.

. c-B\ (22.5-10.75)t =- = 2.93?5 in.-44

y= l10O and m = 1.75

Determine the loads:

n = Tc.p = +,r7.317)r(3z}) : 75,3684'4

H o = ZbtGmp = 2(2'937 5) n(17 .317)(r.7 5)(320) = 178,986

/r,^\ .? sqr 5)HI : \rt)H' = @;^t'is,r8rl: 45r'55e

Wt= H + Hp+H; = 75'368 + 178,986 + 451'559 = 705'913

Hsn = blrGy = (2.9375)r(17 .317X1100) = 175 '79o

/ h^\ /, 5015\Hb'= \nHc'= @rfi5rw= 443'4e7

W,a = Hay + Hb, = 175,799 + 443,496 = 619,286

Determine bolting requirements: A' is the greater of Wa/S"ot W^z/S.

A^ = 36.76 in.'z based on ffiAt = 36.8 in.'z based on 16-2-in. diameter bolts

W = 0.5(A^ + A) : s.5136.76 + 36.8)(19'200) = 706'176

Determine flange moments at operating condition.

Flange Loads

H, = loB2p = f,go.t s1,1szo) = 29,oM

Hr = H - Ho = 75,368 - 29,444 : 46,324

Page 168: Process Equipment

316'IIND

ILANOIS, COVER PI.ATES, AND FI.ANOES

Lever Arms

[o=R * 0.59' = 2.5 + 0.5(3.375) = 4.t875 in.

lr = 0.5(ft i g * h) : 0.5(2.5 + 3.375 + 2.Sgt5\ = 4.2333 n.

Flange Moments

Mp : Hphp : (29,044)(4.187 5) = 121,622

M7 = H7h7 = @6,324)(4.2333) = 196JOq

M. = Mo + M, = 121,622 + 196,104 = 317,726

Determine flange moment at gasket seating condition.

Flange Load

He = W" - H = 706,176 - 75,368 = 630,808

Lever arm

h',_ = hahh - (2.5915X1.0272)"o - ho + hb- Q.915) + [onr) = 0'7356 in'

Fhnge moment

Mr: H6h'[ = (630,808X0.7356 = a6a,O22

All flange geometry constants are the same as in Example 10.9.Calculate flange stresses. Assume flange thickness t = 2.03 in. This isset directly from the radial flange stress at the bolt circte which is

sF=, M' - 6(4u,022)" t"(rc - Nd) (2.0j),(22.5t - 16 x 2)

SF = n,a@ psi < 17,500 psi allowable. stress

Inngitudinal Hub Stre ss

L=

Sr=

+a= 1.0021 +0.0407 = 1.0428

\4e,022)

6.

1

te+lT

L'?n (1.0428X3.375f(10.7s)

Sa = 3634 psi < 26,250 psi allowable stress

IO.I4 f LAT-TACE FTANGE WITH MEIAI-TO-MTTAI CONTACT

Radial Flange Stess

3t7

^ tlte + l\M" (t.4'104)t4M,O22)Lt2B (1.042Sx2.03)110.75)

Sn : 14,77O psi < 17,500 psi allowable stress

Tan Be ntial F lange Stre s s

VMs,: --+ - zs,t'B

Sr = 3457 psi <

Problcm

2.29(464,022)(2.03f (10.75) - (1.39)(14,77 0)

17,500 psi allowable stress t

10.12 Assume a flange with a flat-face gasket has an applied moment ofMo -- 464,000 with a bolt circle of C = 22.5 in. using 16-2-in. bolts.What is the required thickness of the flange if the allowable skess is15,000 psi?

IO.I3 FTANGE CATCULATION SHEETS

Answer: t,"q'd. = 2.19 in.

Calculation sheets are included for the following types of flange design:

Sheet 1. Welding neck flange with ring-type gasket

Sheet 2. Slip-on or lap-joint flange design with ring+ype gasket

Sheet 3. Ring flange with ring{ype gasket

Sheet 4. Reverse welding neck flange with ring-type gasket

Sheet 5. Slip-on flange with full-face gasket

Sheet 6. Welding neck flange with full-face gasket

IO.14 FLAT.FACE FTANGE WITH METAT.TO-METAL CONTACTOUTSIDE OF THE BOIT CIRCLE'",'O,''

Rules for the design of flat-face flanges with metal-to-metal contact outside ofthe bolt circle are given in Appendix Y of the ASME Code, VIII-I. The rulesare for circular, bolted flanged connections with identical and nonidentical pairsof flanges. The pairs of flanges that are in metal-to-metal contact across thewhole face and the gasket load to compress the gasket are small. (see Fig. 10.21)The rules also apply to identical pairs of flanges with a metal spacer added at theouter edge between them.

Page 169: Process Equipment

torrD afto aorY calcut '|or{S

It

ro/ro r llvar /lr|r

,!lsr + 5r,.! tsi + S,j =

aEotr.

SlSr + trlo'.5(t, + t'i =

lr b.l iFdne d.od.2. + r,'.hi?t /i"L,Da.rr .d i. h .br .qd'or b', v -;=;-

Csrea- O.r.

6.r., |{Jih.'-

Sh6.r l. Welding neck flcng€ with ring-ryp€ g6kei. (Co,.rrresy c+W Toylor-Bonnoy Div., Toytor Forg€.)

3t8 3r9

Shsor 2. Slip-on or lop-ioint flonse v.irh rins-typ€ sd3ker. ( Courre3y G+W Toylor-Bonney Div,, Toylor

Forge.)

rOAO l val ^rr - |rorlxl

-----J@!!

Page 170: Process Equipment

tl0 ll.lND .ANO!s, COV!n p[AtES, AND trANOls

ning flonga yrith ring-iypo golk€t. (Cou|.tosy G+W Toylor_Bonney Div., To),lor Fo;Shs€i 3.

The.basic development assumes that the flanges are in tangential contact at theouter.diameter or at some point between the b;ft circle ;; th;i,r'te. oiam"te,at a distance llc from the boit circle. Ttre gasket is assurneJi. ti-rJrilr"o,ng u"ageneraGs a negligibre load during operation and is located in rir,"iia tn" u"rr"twall. The major difference uetrieen ttris ryp",f d;" ;il'tr,"'Jrg_typ" o"_scribed in Section 10.9 is the additional pryi'nl ;fil;;;iliit; contact ofthe two flanges.To organize the calculations svsiemadcally, it is necessary to classify assem_blies and to categorize each individual nann".

-- "--veJqr !v !ru!.

C hs s ifcation o! As s e mb ly

Class l. This is a pair of flanges that are identical except for the gasketg'oove.

Class 2 . Ii consists of a pair of nonidentical flanges where the inside diameterof the reducing flange Jxceeds one_half the U.it "i."f" Ou."to*

Class 3- This is a flange combined with a flat head or a reducing flange wherethe inside diameter is small and ao", oot "*"""0-

on"_tlif" fieiort ctctediameter.

2olrr --- 1,-.:...:.---:-:-=-._.....Y-

rv.r - brc,la,;,.-=^-=Zi w-,tt,- s-,,.-

trll*' Lsc I -e,r/. c"I.

5

.Jlrb + rEl E

t-

k_/, trb rlttat lt,

6 rxpt coxrr^'m l-tL3,nfl;:r,,1*-;E;F-

7

,=J+l @1, 5:t

Co"ur.d- O.r.

G.*.d_ ili5.,--

I prrr 2

4 to^o eno rotr cercur.r6ii

^-,44 ||-1/s.' w-tts,-

r tavl| atrI

1."'.e

iD=J(C+r,-2$-tJ=ti=.5(c-G)

^,=.r{.-F-iiiiiiS,iiiidiii'fi iF,il,,i -""'!,iit,y,,,:,.^*,-,.". M.l

I "',i,:. rtttsS carculaiox-{rf, rolin, 6 xAtD |lut t^cro$r{e, xu5, 5r =ti./I!r'

tcie. tle., S'= tufr/t, -ZS,tO,6rt.+rt/B= z

1:/ r rsr + sr,or J{s{ + s,, =r".".a,.s,o,r'r=+ [v-,xit(Jj ""+[+:!Ilr#rl t-)-9 "?.::' ttr$t cllcutano|r- sdd..

.rub, g = Ircllo,r rr =+.a, r

! rod,crae.,sr = pn./lt l;-------=_+r.^o fl!., S'= ^cfr/r' -Z',to.6rt.+n/R= Ur=drU

llji .la, +sa- rrs, + s,r =r-, n,.. s" 1^l 11 = f, [v

_ i::" i i,' ] = 7 trrls3 Forr ui,a ;^cort

? x r_..r-T*-+

e-rrr:-i-------.']lY El k_r'=

| [.n'rV I

t--|r---T-| | / h ]_-,_ ,__<.'t r ttI I 4'"F-r-bJ +il--l,o l.-----r=

aadl. <t_A:Cmptrd- D.h.-*----

Chxr.d- N!ib.r=--

Sh€€l ,a. R€verc€ w€ldins n€* flonse wirh rins-fyp€ goskst. (Court$y c+W Toylor-Sonney Div., TdytorFors€.)

321

Page 171: Process Equipment

IOAO : lavn rrr - |tot,Nt

,r lA-Cll2A+Cl=""=-:rc+.i-

h,i= l'.1"., -

7 ttrg totnutt ttctotg

I Llr !Fd'! .s.i' 2. + I rlrirt

C..'a.itr Dd.-

O.d.a-

Sh.at 5, Slip-on flons6 with tulLlcce soska. (Court€sy cfw ToyloFBonney Div., Taytor Forss.)

322 323

I o8rox cDaa!|no{t 2. 3

4 loao ^to

lott carcuraroxtw.r= bror + Nir = Ar = rr..tr.t wd/s. d w.Jt =

IrliWn=fi+i!+fi'?=

I TIVlt T

tc-tlra+o=-=-=iiT6-

E "i* ttatS CArqrlAnOx-Ot rato, o x |lo nof tac'otlttr|lr,h=nJr6rr.aEt tr- ar

= P*/If f

r@. 6E sr = ..1/ I -l5l rJl!, + li'Jl$ +5rl '

t^Dur str!3s At |olr ot<ll u

7 nra$ tourula tacloti

It !.lr D.d'. .B.dt 2. + t dldrlr I t lr r.drr.inlb.e!fu !r! I 2.+l

C6er.{-- o.r.-

6rr.a- f&iL'-

Shcet 6.

Page 172: Process Equipment

321 II.INO FIANOIS, COVTR PTATES, AND FI"ANOTS

Figur6 10.21 Flor-foce flonge wirh mebl_to-metolconto.r ouisid. of tfie bolt circle,

Catagory of Flonges

9i*g.IV^ t. This is an integral flange or an optional flange calculated as anmtegral flange.

ca'gory 2.It consists of a loose-type flange with a hub that is considercd toadd shength.

:l"g.y 3. A.loose-type flange that is with or without a hub or an optionaltype calculated as a loose type where no credit is taken for the hub in any case.

Once the class and category are established, the analysis is similar to thati"9" fr:g Appendix 2 flaige except for tt

" udaitionJrl"oings iuus"c uy ttr.prying effe{t where the contact near the ourcr diameter occurs . iiis Jontact torceH3 and its_moment arm lk involve an interaction between tfr" Uoft

"iongution anCflange deflection and the moments Me and Ms.

The required bolt load for operating conditions is

W:H+Hc+Hc (r0.29)

IO.I5 SPHERICALTY DISHED COVERS

'Ihe ASME.Code contains special rules for designing spherically dished covers

I-tll I TntnC, "ng flange. The formulas given in the code are approximate

Decause tney do not take into account the discontinuity existing between the

t0.15 sPHERtcattY orsHED covtRs

dished head and the flange ring. The flange thickness is set by the combinationof the circumferential ring stress and the tangential bending stress. Figure 10.22shows the head geometry and the loading applied to the ring flange resultingliom the reaction from the internal pressure against the dished head. It is derivedthus. Using the geometry in Fig. 10.22, the following is set:

adjacent side :(10.30a)

cos B, = adjacent side _\/L'''' - ( _ \/4L'1Err-=Ehypotenuse L' 2L'

membrane force in head to due to oressure : F' =pL2T

(10.30b)

(10.30c)circurnferential ring stress = 5" = pR

t:pD

2t

A ( outeide dianeter)

Fisuru 10.22 Sphcricolly-dirhed covcr.

Page 173: Process Equipment

t26 .tND ttANO!!, COVIR puTrs, AND traNols

Substituting l, = tr', cos B,; D = B; and , = (/ _ B)/2 in Eq. 10.30c,

^ F'cos B, I' a-B)/22When the value of ./c, is substituted in Eq. 10.30d, the equation becomes

s" = *2 ,,"o" 9,,,212@-B)/2

Whdn the value of cos B1 from Eq. 10.30a is substituted,

" - pn t/+Ld-=E. 4T A_B

]anCeryia gtrep] ring due to Me is as follows: from Eq. 9 of 2_51 of the ASMECode, Section VIII, the equation rs

- vM"-' T2B (10.32)

butY = (A + B)/(A - B),so

"= c^;(*=)

(r0.30d)

(10.30e)

(10.31)

(10.33)

Combining the circumferential and the tangential stresses in the ring grves

s, = s" + r, = r4@-=F * ( u"\(e * n\4r e= n - - \f,ri1, _, ) (to.34\

I€t

r = PBldt=E -^^ , _ Mo(A + B)8S(A - 8) s8(A _ B)

(10.3s)

Then

s,=f<n * fiut (10.36)

IO,I5 SPHERICATTY DISHED COVERS

l)ividing by S and rearranging terms to form a quadratic,

T2-27(F)-J=02p -r 1/@ufi or T:F t-1/vta1

(10.37)

(10.38)

This equation is identical with the equation given in 1-6(9) of the ASME Code,v[-1.

Application of this equation is permitted for either internal or extemal pres-sure. The term p is the absolute value for either the internal pressure or theexternal pressure. The value for ffi is determined by combining the momentsfrom bolt loading and gasket loading with the moment caused by the pressureloading from the spherical head on the inside edge of the ring. When this totalmoment is determined, the absolute value is inserted for Mo in the equation.Figure 10.22 shows the loadings caused by the pressure. In Fig. 10.22, theloading shown is due to intemal pressure. However, if the loading were due toextemal pressure, all directions of loadings would be reversed, but the effectivestresses on the ring would be the same. If external pressure were applied to thehead, it would have to be examined for compressive buckling that might set thethickness.

Example 10.14. A spherically dished head is to be bolted to the welding neckflange described in Example 10.9. The dished head is to b€ attached at the upperinside comer with the outside surface even with the ring's outside (see Fig.10.23). What is the minimum required thickness of the flange ring when thespherical head is dished to a radius of I = 28?

Fisure 10.23 Dimgnsioni of sphericolly-di.hed heod in

Ex. 10.14.

Page 174: Process Equipment

329 tuND traNots, covtR phTrs, aND H.ANotS

Solutlon. From the geometry of Example 10.9,

A = 26.5; a = 10.75; L=28=2(10.75\:21.5

D€termine the minimum required head thickness as follows:

, =t# =*ffii = 2.560 in.; use2.625 in.

From geometry calculations

L'=L+l:r.r.t*?@L' = 22.813 in.

cos p1 =22.8t3)z - (10.75

2(22.813) =0.972; h=13.626"

Membrane force in the head due io pressure is

r':pL -(25mV2l'sl' -n- :2r,s" =lo'zolb

Horizontal force = F' cos p1 = GO,24O)(0.972\ = 9950 lb

Vertical force = F' sin Br = O0,'2,40)(.236) = ?A2O lb

Total horizontal force = a(10.75)(9950) : 336,000

Total vedical force : zr(10.75)(Z4ZO) : 91,76

Moment at gasket seating condition is

Load furn Moment

He = W. = 700,800 ho = 0.5(C - G) : 3.729 Mo = H6h6: 2,613,000

Moment at operating condition is

t-oad Arm

IO.I5 SPHERICAI.I"Y DISHED COVERS

Moment

IIp = 11,: 8l,700

He = Hp:250,600

Hr = 336,100 hr = 0.5(R'r g'l h6)

= 4.8O2

Hn = 336,1.0O -hn : -O.5(T - t)

ho = 0.5(C - 8) : 5.875 Mp : H6hp :

he = 0.5(C - G) : 3.729 Mc = H6h6 =

M7 = H7h7 :

Ma = Hnhn :

480,000

934,000

1,614,000

- 168,050r+441,300: -0'5T + 1.313

Mo: Mp + MG + Mr + M, : 3,469,60 - 168'050f

The minimum thickness at gasket seating condition is

(2,613,0W)1?!ll_!!JI)_ = ?,, RsnF=u and r: (nJ:00xmj5)(26i - l0J5): rt'orv

T: F + \/F' + J = *2-s5o = 5.732 in.

The minimum thickness at operating condition is

" _ (2s00x10.75)y'4f11.8 I tP-:-(l0l75f = o 54o' 8(17,500x26.5 - 10.75)

If we assume T = 5.75 and M0 : 2,503,000,

r :32.8so 'ffi;ffi = 31.467

T = 0.540 + + (3r.467): 6.175 in.

If we assume T = 6.25 and Mo = 2,419,000,

I=32.850"?*i:# =ro4tlT = 0.52+0 * y'1g5a0t + (30'4lD = 6.081 in.

The minimum thickness is approximately 6.108 in. Although exact thickness

can be determined , T = 6.25 in. is satisfactory. I

Page 175: Process Equipment

330 EuND frANOrs, covER ptAlrs, AND FtANGTS

l'robhms

10.13 A spherically dished flange with an outside diameter ofA = 36 in. andan inside diameter ofB : l8in. is subjected to a gasket seating momenrof 3,500,000 in.lb. The allowable tensile stress of the flangi materialis 15,000 psi. What is the minimum required thickness at the gasketseating condition?

Answer: t^n = 6.24 in.

10.14 For the flange in Problem 10. 13, what is the maximum allowable flansemoment if the allowable tensile stress is increased to 17,500 psi and tieflange thickness is set at 6.25 in. ?

Answer: M51o* = 4,|O2,NO in. lbs./in. circumference

NOMENCTATURE 33I

NOMENCTATURT

lndividual nomenclature is used throughout Chapter 10. It is usually noted nearto where used. The following list gives some of the general nomenclature.

A : outside diameter of flange (in.)

I = inside diameter of flange (in.)

C = diameter of bolt circle (in.)

E : weld joint efficiency

G : diameter of gasket reaction (in.)

1u' : gasket seating width (in.)

N-6 = minimum gasket width (in.)

P = total load 0b)

R = spherical radius of gasket surface (in.)

S = allowable tensile stress (psi)

S. : allowable bolt stress, room temperature (psi)

56 : allowable bolt stress, design temperature (psi)

design pressure (psi)

nominal thickness of head (in.)

effective diameler of flat head (in.)

minimum requircd thickness (in.)

seating stress of gasket material (psi)

= modulus of elasticity (psi)

= flange loading for design condition (lb)

= flange loading for bolt-up condition (lb)

= basic gasket seating width (in.)

= effective gasket seating width (in.)

= outside diameter of gasket (in.)

= inside diameter of gasket (in.)

= actual bolt area (in.'z)

: flange moment for design conditions (in.lb)

Yory =E,

W^t

Wz

bn

b

OD

ID

Ms

Page 176: Process Equipment

332 tuNO fl-ANOts, COVTR PLATES, AND lt-ANOts

o,

a"

lL

Mn

0*o,

',

flange momcnt for bolt-up condition (in.-lb)

maximum bending stress (psi)

m dmum deflection (in.)

maximum rotation (radians)

or : tangential stess (psi)

ai = radial stress (psi)

a6 = circumferential sness (psi)

poisson's ratio

REFERENCES

ASME Boiler atrd Pressure Veso€l Code, Section VIII, Division I, Pressure Vessels,ANSVASME BPV-Vn-I, Amedcan Society of Me.hanical Engine€$, New Yo*, 1983.

ASME Boiler ard Pressure Vessel Code, S@ton I, Pover Boilcrs, ANSVASME BPV-I,American Society of Mechadcal Engineers, New York, 1983.

Wate$, E. O., D. B. Wesstiom, D. B. Rossheim, and F. S. G. Williams, "Formulas forSft€sses in Bolted Flanged Connections," f/dns. ASME, vol. 59, 1931, pp. 16l-169.Wate$, E. O., D, B, Rossheim, D. B, Wesstrom, aDd F. S. G. Wilham's, Development ofGeneral Formulas for Bohed Flaryes, Taylor Forge atrd Pipe Works, Chicago, 1949.

Waters, E. O., and R. W. Schneider, "Derivation of ASME Code Formulas for lhe Designof Reverse Flanges," WeldittS Research Council, Bulletin 262, October 1980, pp. 2-9.ANSI Standard 816.5, "Pipe Flatrges and Flanged Fittings," American NatioMl Srzndardshstitute. New York.

API St ndard 605, lzrge Diametcr Carbon Stee, FrarSer, ANSVAPI Std. 605, AmericatrPetroleum ltrstitute, Washington, D,C.

ANSI Staftlard B16.24, 'Bronze Flanges ard Fittings, 150 aod 300 lb," America! NationalStandatds Institute, New Yo*.Rossheim, D, 8,, and A. R, C. Markl, "Gasket Irading Con$tants," Mechanical Ebgi ceri g, Vol. 65, September 1943, W. 647-648.

Raut, H. D., and G. F. Iron, "Report of Oasket Factor Tests," Welding Research Council,Bulleti! 233. New Yort. De.ember 1977,

Modern Flange Design, Bulleth 502, Tttt ed, , G aDd W Taylor-Bomey Division, Southfield,Mich.

Roark, R. J,, FormnJas for Stress and Strain,3d ed., McGraw-Hill, New York, 1954.

Water$, E. O,, 'Dedvatior of Code Fordulas for Part B Flanges," WeUinB ResearchCoun il, Bnlletin 166, October 1971, pp. n47.Schneider, R. W., and E. O. Waters, "The Backgrcund of ASME Code Cas€ 1828: ASimplified Metbod of Analyzing Part B Flanges," Tranr, ASME, Jounal of Presrure VesselTechnology, Vol. 100, No. 2, Mt! 1978, pp. 215-219.

Schneide., R. W, and E, O, Wate$, "The Application of ASME Code Case 1828," Irarr,ASME, lournal of Pressure Vewel Technology, Vol. 101, No. I, February 1979, pp.87-94,

12.

13.

11.

14,

S|EUOORAPHY 333

BIBTIOGRAPHY

Bhch, A. E., and A. Bazergui, "M€thods of Analysis of Bolted, FlaDged Connections-A Re-view," Ecolc Pol)4echnique, Monti€al, Camda, Jaluary 1981.

InterprEtive Study on the Design of Notr-Circular Flaoges and Flanges with Extemal Loads" (aprivate report to PVRC , May 23 , 1979 .)

Rrut, H. D., A. Bazeigui aod L. Marchand, 'Casket l€akage Trends" (A private report to PVRC),April 1981.

Rodsbaugh, E. C., atrd S. E. Moore, "Evaluation of the Bolting and Flarges of ANSI 816.5Flarged Joints-ASME Part A Design Rules," ORNUSub-2913-3, Oak Ridge National Labo-ratory, Oak Ridge, TeDn., Septenb€r 30, 1976.

Timo$henko, 5., Theory of Plates and S&ells, McGraw-Hill, New Yo*, 1940.

Page 177: Process Equipment

334 335

CHAPTER llOPENINGS, NOZZLES, AND

EXTERNAL LOADINGS

Page 178: Process Equipment

336 OPENINGS, NOZZIES, AND EXTERNAI' LOADINOS

I I .I GENERAL

All process vessels require openings to get the contents in and out For somc

vessels, where the conients miy be large or some of the intemal parts may need

frequent changing, access is made through large openings in which the entirc

heai or a secioriof the shell is removed. However, for most process vessels,

the contents enter and exit through openings in the heads and shell to which

nozzles and piping are attached. In addition to these openings others may be

required, suCh- as those for personnel entering the vessel through a manway

opining. Other openings rnay be necessary for inspecting the vessel ftom the

outside-thmugh a handhole opening , and still others may be required-for cleaning

or draining tie vessel. Thesl openings do not always have a nozzle located at

the openin!. Sometimes the closure may be a manway cover o-r handhole cover

that ii eithlr directly welded or attached to the vessel or a built-up pad area by

bolts.For some nozzles, additional loading to the iniernal or extemal pressure may

be innoduced from dead loads ftom equipment and piping and ftom thermal

expansion flexibility loadings from the piping and equipment motions' This

Ml

f-F^l

figura tl.l Applied Pras$rre ond externol loodings on noz-zle' FigurG ll.2

I I.I OENERAI,

additional loading may require compensation as well as what is necessary to

rcsist the internal and external pressure loadings, as shown in Fig. 1l.l'Openings and nozzles similar to those occurring in pressure vessels also occur

in piping. This is the case where a branch run is attached to the main run ofpiping. The branch-to-run intersection is subjected to the same pressure and

ihermal expansion loadings as those applied to a vessel nozzle. Although the

nozzles have a similar construction, usually an important difference lies in the

relationship between the ratio of the nozzle diameter to the vessel diameter and

the branch diameter to the run diameter. For pressure vessels, this ratio d/D ismuch less than for piping. In many piping systems, this ratio may be very close

to 1:1, as as shown in Fig. 11.2.In designing openings and nozzles for resisting loadings from internal and

extemal pressures and from external loadings, two types of stress conditions are

important. Fkst, the primary rnembrane stresses in the vessel or run pipe, that

is, the necessary stresses mahtaining static equilibrium must be kept within the

limits set by the allowable tensile stresses. Second, the peak stresses caused by

abrupt changes in the geometry at the nozzle-to-shell comer and cause stress

concentrations must be kept within acceptable limits. These peak stresses are

important in a fatigue evaluation where the design life of the nozzle and the other

Voriotion in d/D rotio of nozzles ond piping.

Page 179: Process Equipment

OPININOS, NOZZICS, AND EXTERNAI TOADINOS

vcss€l parts or piping system are established. A slight change in the details at thointersection may enable the vessel to operate through many more cycles ofpressure and temperature loadings.

Detailed rules for designing vessels and piping to accommodale the primarymembrane stresses and loadings from intemal and external pressures are givenin codes and regulations such as the ASME Boiler and Pressure Vessel Codeland the ASME Code for Pressure Piping B31.'z In addition, some design rulcsare given in the more advanced sections of these codes to permit consideringshess intensity factors (SIF) and stress concentration factors (SCF) in deter-mining peak stresses. The peak stresses are used to determine the design fatiguelife of the vessel. Other codes do not mention peak stresses or fatigue evaluationsand leave the latter as the designer's responsibility. At the present time, none ofthese codes contains detailed design rules for the consideration of extemalloadings from either dead loadings or piping expansion loadings.

I1,2 Stresses ond Loodings ot Openings

Both single and multiple openings require calculations that show that the stresses

and loadings in the shell and head are kept within acceptable limits. Singleopenings are calculated by the reinforcement method, whereas multiple open-ings are calculated by either the reinforcement method or the ligament efficiencymethod. In both cases, the primary stresses are effectively kept less than theallowable stress by replacing the area removed for openings.

For a single circular opening in a flat plate with infinite boundaries in twodirections (not through the thickness) that is subjected to applied forces andstresses along opposite edges of the plate, stresses are increased above thenominal applied stress in the unperforated plate. The stresses decrease awayfrom the opening until the nominal stress in the plate is obtained. The ratio ofthe stress at the examined point divided by the nominal stess is the stress

intensity factor.The shess intensity around an opening may be expressed either in general

terms of applied stresses and geometry or in location of the considered point. Thebasic equation at an opening may be represenied in terms of o and 0, with theangle of the considered point measured from the loading axis.r For the loadingshown in Fig. 11.3a, the or is axial and 0 = rl2 at the maximum sfiess loca-tion. ForFig. ll.3b,lhe q is axial and 0: rl2 atthe maximum stress locationand, o2:0.5or is at right angles to a1 and 0 : 0 at the maximum stress

location. For Fig. 11.3c, the a1 is axial and o2 : o1 is at right angles to o1.

Values of 0 are the same as for the cylinder. When two loadings or stresses are

involved, the effects at the maximum stress location are added. The basiccouation for direct s[ess is

" = Zl'. (;)'] - i [' -' '(;)']

*' '' (11 . l)

I I.2 STRESS€S AND TOADINGS AT OPTNINOS

Figure ll.3 Two-direction'lood combinorio's on flot Plote with circ"ldr oPening'

The basic equation for the maximum stress at the edge of the opening in terms

of the component of stresses in each direction is

(1r.2)o^o:3o1 - o2

where the values of or ?rd oz include plus and minus signs depending upon

whether the applied stress is tension or compression. The stress intensity factor

at the edge oi circular openings for various ratios of applied edge stresses is

siven in Table 11. l.The stress intensity factor for various combinations of stresses is maximum

Page 180: Process Equipment

340 OPININO5, NOZZLES, AND EXTERNAT IOADINOS

Tqble I I.l Streu InlenallyFoctors for Vorious Rolios ofApplied Stress

Stress Ratio

1:0(axialonly)2 : I (cylinder)

I : I (sphere)

at the edge of the opening and decreases away from the opening until the stressapproaches a nominal shess factor close to 1.0.

Using the following nomenclature, various formulas for different combina-tions of applied stresses are developed:

r = radius of circular opening in plate (in.)

r : distance from centerline to point of SIF (in.)

For applied stress ratio of 1 : 0-the condition of an axial tension loadonly-the basic equation for the stress intensity factor is obtained by solving Eq.1l.l with 0 = rl2 wherc cos 20 = -1, giving

3.00

2.50

2.00

"' = Zl'. (;)l - i l' -''0']t-'r

',:ilr. (;)'-,(;)l (1 1.3)

At the edge of the opening, the stress iniensity factor is determined from Eq.ll.2 assuming that o1 = or and or = 6'

o^:3or-0=3.00or (r 1.4)

Substituting various values of r for x in Eq. 1 I .3, stress intensity factors atvarious distances from the edge of the opening are

r 3.00sr21 1.15ar

3r l.Mo14r l.O4o1

For an applied stress ratio of 2 : l-the condition of a cylindrical shell under

l l.2 STRESSES AND IOAOINOS AT OPININOS 341

intemal pressure-the basic equation for the stress intensity factor is found by

combinine the effects of sfesses in two directions according to Eq. l I l:

",, : Zl'. G)l - ; t' . '(;)']

cos 20 where o = I* =; i' . (;)']

The general equation is the summation of the two stresses and cos 20 = + 1

", =Ilz* /r)'* r - 3fr)'+ r + (r)'- t- rf:)'l4L- \r/ \x/ \r/ u/ I

", =ilo. ,(')' . ,(;)']

cos 20 = -1where 0 = 0

(l l.s)

At the edge of the opening, the sffess intensity factor is determined from Eq'

1 1.2 assuming cr : or vnd 02 = 0.5or so that

c* = 3or -O.5or = 2.5oot (1 l.6)

Substituting various values of r for.r in Eq' 11.5, stress intensity factors at various

distances from the edge of the opening are

r 2 5oor

2r l.23at31 1.09or

4r l.05or

For an applied stress ratio of 1 : 1 in a spherical shell or hemispherical head

under internal pressure, the basic equation for the stress intensity factor is

resolved by combining effects of stesses in two directions accoding to Eq. 11.1

that gives

-i['-':0']*'ze

'=t*$' (l l.7)

At the edge of the opening, the stress intensity factor is determined from Eq' 1 I .2

assuming that at = or dllrd cz: 6t as given by

c*:3c1 - ar=200or (11.8)

Page 181: Process Equipment

Substituting vsrious vulucs ol'r li)r r in Lq. 11.7, stress intensity tactors atdislances lrom the edge ol'the opening are

r 2.O0oy

2r l.25or31 1.11o1

41 1.06s,

Exarnple 11,1 A vertical vessel under intemal pressure and dead load containsan opening that is qubjected to applied stresses. The dead load stress is equal tothe circumferential pressure shess. For this stress condition, what is the basicequation for the stress intensity factor at any location from the center of theopening?

Solutian. The applied stress in the circumferential direction is o1, whereas inthe longitudinal direction it is the longitudinal pressure stress minus the longi-tudinal dead load shess. This equals oy, = IO.5o1 and c2DL: -or and thesummation equals -0.5o;. Using Eq. 11.1, the basic equations are

/r\ 4l+31:l lcos 20 where 0 = "

\r/l 2

cos 20 = -l

G): *' 2o where o: trcos 20: *l

oPlNrNoS, l{onfis, AND ExftRNAr toAD|NOS

Exarnple 11.2 For the vessel described in Example 11.1. what is the max-imum stress at the edge of the opening according to Eq. I 1.2?

Soltttion. Assuming that or = o1 and o, = -0.5 rr, the equation for max-imum stress at the edge of the opening is given by Eq. 11.2 as

",=url,. (t'] -;['of /r\21 -loa: --l l+l-l l+ _ll+4L V/l 4L

,, : "ol,

+ rG)' +,.'(:) -' - (")'.' ., (r'],, ="olo. (;)' .'(')'] .

o,o^: 3oy - oz = 3ot - (-0.5ar) : 3.50ar I

I'roblems

I I .1 What is the stress intensity factors for a plate under a stress ratio of 2 : - Ifor the vessel given in Example 1 1.1 at the edge of the opening and at

distances of 2r,3r, and 4r?

I I.3 THEOTY OF REINfORCID OPENINOS

Answeri Incat\on SIF

r 3.50

21 1.2O

31 1.05

41 1.Oz

11.2 In the ASME Code, VIII-2, a local stress region is one in which the stress

intensity of 1.15, does not extend more than VRt In terms of the radius

of the oiening r, how far ftom the edge of the opening in-a hemispherical

head under iniernal pressure is required to have a stress of 1' 15. assuming

S^ = o1?

Answert Ttrc SIF becomes equal to 1.1S. at a distance of 2'66r from

the edge of the oPening.

11.3 As in Problem 11.2, what is the distance from the edge of the opening

along the longitudinal axis in a cylindrical shell under intemal pressure

if required to have a stress of 1. lS,?

Answerz T\e SIF becomes equal to l.lS. at a distance of 2'90r from

the edge of the opening along the longitudinal axis'

I I,3 THEORY OF REINFORCED OPENINGS

AsdescribedinSectionll'2,thereisanincreaseinbasicshessesatanopenlngin aflat plate or shell under edge loadings due to the discontinuous pathway for

the loms (anO stresses) to pasJ from one side of the opening to the other side'

When this happens, otler pathways have to be established- in.order to keep the

orimarv sresies at an acce-ptable level. The basic theory of reinforced openings

ir to suppty pathways with additional material in the region of the opening to

"u.ty tiJ ioud. Uy

-ttt" opening. In designing process equipment and other

pr"s*r" u".t"l., tiis pattrway iJ supptied by the thickening of the basic shell or

iozzle material and Uy adding material such as a pad, as shown in Fig' l1'4'placement of the additional material is important. It must be sufficiently near

the opening to be effective; and yet, it must be added with caution to prevent

Page 182: Process Equipment

OPININOS, NO2IIES, AND TXTENNAI I.OADINOS

Figt re I L,4 ,{€lhods of odding r6inforc€msnt moteriol. (Court*y Arnericon Socisry of it€chonicol Engine€rc,From Fis. UM6.l of the ASr'tE Code, Vlll-l)

another problem such as high thermal stresses. Investigations by the pVRCa andothers indicate that the placement or location of the reinforcement is important.On most pressure vessels, the reinforcement is added to the outside as shown inFig. 11.5. However, on some vessels the reinforcement is added on the insideas in Fig. 11.6; and on still others, some of the reinforcehent material may beadded !o both the outside and the inside as in Fig. 11.7. The best arrangementfor reinforcement is the so-called balanced reinforcement which consists ofabout 35-407o of the area on the inside and about ffi-C|Vo of the area on theoutsidg. On many designs, it is difficult to place any reinforcement on the inside

Tn

.r!,

\,i:\:;i*

T

figure I L5 Reiniorcemsnl od&d to outside of oPening'

lT

5

\tl.t

Figur€ I1.6 R€infor.€ment odded to intid. of op€ning'

345

Page 183: Process Equipment

t.l6 OPININOS, NOZZTES, AND IXTIRNAI. I.OADINOS

Tn

{.a\i,:'l\i-;.jl:i

T

Figore I I .7 R€inlorc6manr odded to bofi insid€ ond o'rrside.

either because it is not accessible or it interferes with flow or drainage. Thebalanced reinforcement is often used at manway and inspection openings whereno nozzle is attached.

For applications in design problems, where the reinforcement requirementsare established, the method of replacing areas is chosen rather than a method thatbalances loads or stresses . An area at the opening for carrying primary loads andshesses is removed. Thus this required area must be replaced by another areaadjacent to the opening that is not used for that purpose. It is desirable to replacethat area required for primary loads by an adjacent reinforcement area. Withinthe reinforcement limits, the reinforcement areas are assumed to have the sameload-carrying capabilities as the area removed for the opening. Consequently,when the reinforcement areas are equal to or exceed the required area, primarystresses have been restored to as near the unperforated plate as possible.

I I.4 REINFOR.CEMENT LIMITS

As described in Section I 1 . 2 , the stress intensity factor for an opening in a shellor head is highest at the edge of the opening and decreases away from theopening (based on a shell wall with constant thickness). When the effectivethickness is increased, as happens with added reinforcement material, the ever-age stresses are lowered. Limits of reinforcement are set parallel and perpendic-

I I.4 RTINFORCEMENT TIMITS

ular to the surt'ace of the shell. These are set at a point at which it is l'elt that the

added reinforcement within the limits is effectively helping to replace the metal

removed at the opening.Two formulas are used for setting the limits measured from. the opening

c9!!er!!e3!91g.1@g!qg".jg@f, with--th" t-c* offlre two inswEis used.

The first answer is equal to the diam6fer of the opening d. The second limit equaltothesumof ?l + T^+ O.5d. AsshowninFig. 11.8, the thickness ofthe nozzle

wall usually determines which of the two limits controls. At a distance d fromthe centerline without reinforcement added, Eq. 1 1.5 for a cylinder gives a SIFof 1.23or and Eq. 11.7 for a sphere gives a SIF of 1.25 q. With additionalreinforcement material, the nominal stress is reduced close to that in an un-

perforated plate.If z nozzle is attached at the opening, it also offers reinforcement arca

available for replacing that area removed from the vessel at the opening.lU-

@iruegAUC!.d9l4bl9-lgled on the wave

damping length of a beam on an elastic foundation. For a cylindrical shell, thislength is a function of l/B, where B for a poisson's ratio of 0.3 is equal to1.285 /Y rt .

The vertical limit was set in the ASME Code as 2.5 [ many years ago when

an assumption was made that r/r of 10 was to be usEif-This limit is about rightfor an internal pressure p of 1200 psi and S : 12,000 psi. The development of2.5 T" is

I

_l\/,- p r.285\/o.tv

= O.246r = 2.46t1.285

For code application, the number was rounded off to 2.5 f. With the wide range

of r/t ratios, which are currently used in process vessel construction, some ofthe codes are setting this reinforcement limit in the vertical direction by

L = O.7S !r-I" ( 11.e)

where L = reinforcement limit perpendicular to shell (in.)

/, = mean radius of nozzle opening in shell (in.)

4, : nominal thickness of nozzle (in.)

Each pressure vessel and piping code treats the calculation of the reinforce-ment area somewhat differently and establishes both parallel and perpendicularlimits in different ways. A discussion of the reinforcement requirements forseveral different codes follows.

Example 11.3 A cylindrical pressure vessel that is 60-in. ID by 6-in. thickcontains a nozzle that is 12-in. ID by 3-in. thick. What is the stress intensityfactor at the reinforcing limit that is parallel to the surface of the vessel?

Page 184: Process Equipment

Ti+Tn+o,td

348

Figur. I1.8 Reintorcomsnt limits porollsl to she'l sur{o.6.

I r.4 RqNtoRctMENT tlMlrs

Solution. The two horizontal limits are set by the larger of

d:12in.

0r

T, + T^ + O.5d = 6 + 3 + 0.5(12) : 15 in'

The limit is set by the 15 in. from the nozzle centerline.

The stress intensity factor is obtained by using Eq' 11.5 to give

",:Xlo. '(*)' . '(iJl = l rkn I

Problams

11.4 If the new reinforcement limit in the vertical direction were based on

r/r = 5 instead of r/r = l0 that was used to obtain the present limit of2.5T,, what is this multiplying factor in terms of T^ for r/t = 5?

Ans*ert The vertical limit is 1.74?1, based on the limit of r/t = 5'

11.5 For an allowable stress of 15,000 psi, what is the maximum design

pressure permitted for an rft = 5 based on the circumferential stress

formula given in the ASME Code, VtrI-l?

Answer: Based on the circumferential stress, the maximum design

pressure is 3260 Psi.

i t.l. t Reinforcemenl Rules for ASME, Section I

The rules for reinforced openings in ASME, Section l, Power Boikrs, permlt

using the replacement of both area and ligament efficiency provided certain

limits are met. Ligament rules may be used for repeating pattems of openings

provided the maximum diameter of any hole in the pattern does not exceed a

diameter determined from Fig. PG-32 of Section I. This figure is a plot of the

following equation with limiting values of K between 0.5 and 0.99:

a,,, =z.ts{WJr-x) (11.10)

with the limits of 0.5 < K < 0.99.

p = intemal design pressure of maximum allowable working pressure

(psi)

Page 185: Process Equipment

3IO OPTNINOS, NOZZTES, AND TXTERNAI. TOADINGS

4nn" : msximum alkrwable diameter of opening (in.)

D, = outside diameter of shell (in.)

fl = nominal thickness of shell (in.)

S = allowable tensile stress (psi)

For shelfs designed to PG-27.2.2.1 of Section I,

K: P?'- 1.6 s?i

For shells designed to PG-27 .2.2 of Section I,

(1 l. l1)

(t|.r2)

N o Reintorcement Re quhe d

The rules for openings in Section I contain proyisions for single openings whenno calculations are required to prove the adequacy of the shell. No calculationsare needed for a cylindrical shell when either of the following is met:

l. d /D < O.25 arrd d^* = 2-in. NPS.

2. d* = maximum diameter using Fig. PG-32.

For openings in forrned heads, no calculations are required to prove the ade-quacy if all of the following are met:

1. Actual center-to-cenier distance between openings is less than I where

A+B

r= PD"-- 1.82 St

L= 2(r + K)

r = --!2:--- 1.82 S?:

A and B : diameiers of adjacent openings (in.)

D, = outside diameter of formed head (in.)

{ = nominal thickness of formed head (in.)

Other terms are the same as for Eq. 1 1. 10.

2. The edge of one opening is no closer than I to the edge of the adjacentopening.

(11.13)

(1 1.14)

I I.4 RTINFORCEMENT TIMITS 35I

3. Except for hemispherical heads, formed heads have dlD = 0.25 Bndd^* : 2-in. NPS, which is the same as for cylindrical shells.

4. For hemispherical heads, the actual center-to-center distance in item I ismet. The value of K is one-half the value of 1( as determined bv Eo.11. 14.

5. For formed heads, d,- of Eq. 11.10 is met.

Size and. Shape of Openings

The shape of the opening when these rules are applicable is limited to circular,elliptical, or obround where the ratio of the large-to-small dimension is < 2.0.When the ratio is ) 2.0, special requirements may be necessary to resist anytwisting moment. For shapes other than those above, a special analysis or prooftest is required.

No limitations are set on the size of an opening by Section I rules. However,the rules in the text are limited to the following sizes:

l. For vessels 60 in. and less in diameler, the opening shall not exceed0.5 D or 20 in.

2. For vessels over 60 in. in diameter, the opening shall not exceed 0.33 Dor 40 in.

When these sizes are exceeded, suggested rules place the available reinforcingarea close to the opening.

Required Area of Reinforcemenl

The total cross-sectional area of reinforcement required for any plane through thecenter of an opening is given by

A = dt,F (r1.15)

where d = diameter of opening (in.)

t, = minimum required thickness of seamless shell (in.)

f = 1.0 except that Fig. PG-33 may be used for integrally reinforcedopenings, where permitted,

F=0.5(cos'z0+l) (11.16)

For torispherical heads when the opening and its reinforcement are within thespherical part t, is the minimum required thickness for a hemispherical headwhen the radius is equal to that of the spherical part of the torispherical head.For a 2 : I ellipsoidal head when the opening and its reinforcement are within

Page 186: Process Equipment

352 OPININOS, NOZTLES, AND EXTERNAT I.OADINGS

u circlc of 0.8 D, ,. is the nrinimum required thickness fbr a hemispherical heud

when the radius is equal to 0.9 D.

Limit of Reinforcement Parallel to Shell

The limit of reinforcement parallel to the shell measured on each side of the

opening centerline is the greater of (1) / or (2) T, + T, + 0.5d.

Limil of Reinforcement Perpendicular to Shell

The limit of reinforcement perpendicular to the shell measured either inward or

outward from the surface is the smaller of (l) 2.5 T, or (2) 2.5 T" + T".

Available Area of Reinforcement

If the thicknesses of the shell and nozzle are uniform and the reinforcement areadoes not extend beyond this uniform thickness, the following formulas may beused for determining the available area of reinforcement. However, if the open-ing and its reinforcement extend into areas with different nominal thicknessesand different minimum required thicknesses, these formulas are not applicable.

1. Area available in shell wall is the ereater of

At=(EL-Ft,)(zd-d)or

At=z(EtT'- Ft,)(T'+n)

2, Area available in nozzle walT is the smaller of

Az=2(T"-t,)(2.57,f

Az: 2(7" - t^)(2.57, + T)

(11. l7)

(11.18)

(11.19)

(r 1.20)

When two or more openings are spaced so that theil limits of reinforcementoverlap, the combined area is used and counted only once. The spacing betweenany two openings is to be not less than 1.33 4". For a series of openings in apattern, the area between any two openings equals 0.7f' of the area obtained bymultiplying the center-to-center distance by the required thickness as shown inFie. 11.9.

I I.4 REINFORCEMENT IIMITS 353

Figorc tt.9 binfo.cing requirom6nb for mlltiple oPnings. (courles), Americdn so.i6tv of r{e.honicdl

Ensin€€rs, Froh fig. PG-38 of the ASME Code, S€crion l)

Example 11.4 Figure 11.10 shows a 66-in. ID steam drum containing fivedifferent diameters and two types of nozzles. What are the nozzle reinforcementrequirements? The design data are

Design pressure = 2875 psi.

Design iemperature : saturation at design pressure approximately 689'F.

Materials 70,000 psi UfS drum plate.

Allowable stress at safiiration temperature : 16,800 psi.

Weld joint efficiency is E : 0.95.

Nozzles are 3+in., 4 in., 5 in., 63 in., nd 24-in. ID.

Solution.

1. Minimum required thickness of shell at E : 0.95 is

PR 2875 x 33' sE - 0.6p 16.800 x 0.95 - 0.6 x 2875 .- -

use 6i in. plate

Page 187: Process Equipment

a

bd

T"l

EX--

x x

2X

A B( D=LIMIT OF REINFORCEMENT

T^

ABCD-LlMll OF REINFORC EMENTFigurc 11.10 .,S.t-on,, ond ,,3€t-in,, nozzles.

2, Minimum required thickness of seamless shell is

PR 2875 x 33=61!rrn' sE - o.6P t6.800 - 0.6 x 2875

3. Minimun required thickness of nozzle is

Pr rR75 r'' sE - 0.6P 16,800 - 0.6 x 2875

4, Maxirnum diameter of a single uffeinforced opening is determined as

D, = 66 + 2(6.75y = 79.5 in.

K from Eq. tt.tZ ls ,*, ,r-32r-

: 287 5 x 79.5

l3 -ffifi;Js= r'tur

K'- = 0'99354

Area available is greater than atea requied and values of 4 that were assumed arc correct.

I I.4 RIINFORCEMENT I.IMITS

Using Eq. I L 10, the maximum diameter is

d-^:2.75 \rr3t675x(i-r0.9 = 4.814 in.

The only single openings are 5 in. and 6{ in.;others are not consideredsingle. Consequendy, all nozzles have the reinforcement area calculated(see Table 11.2).

All nozzles except the 24-in. ID nozzle are "set-on" type and calculatedtogether.

Reinforcement area required by Eq. 11.15 is

A, = dt,F : d(6.294)(1.0) = 6.294 d

8. Limit parallel to shell is greater of

d or T,+7,+ O.5d:6.75 + T.+ r

9. Limit normal to shell is smaller of

2.57, = 2.5(6.75) = 16.875 in. or 2.57,

10. Area available in shell wall is

A, = (2x - d)(r" - t) = (2x - d)(6.7s - 6.294)

A1 =(2X-dX0.456)

11. Area available in nozzle wall rs

Az:2Y(T^-t^)

Tqble ll.2 Reinforcement Cqlculqtions for 3| in.,4 in.,5 in., ond 6f in.Nozzles on o 66 in. /D Steom Drum

,X= parallel Y= normal

355

6.

7

6.'75 +d A, T" d T"+r 2.57, 2.5T, t,^ At Az A,

3.5 22.03 1.8'75 3.s 10.375 4.688 t6.87s 0.334 7.8'7 t4.44 22.314.0 25.18 2.125 4.O 10.875 s.313 16.875 0.381 8.09 18.53 26.625.0 31.47 2.5 5.0 11.75 6.25 t6.8'75 0.477 8.44 25.29 33.736.875 43.27 3.O 6.875 13.188 7.5 16.875 0.656 8.89 35.16 ,t4.05

Page 188: Process Equipment

116 OPININOS, NOIZI.Is. AND EXTERNAT IOADINOS

12. A 24-in. lD downcomer has "set-in" nozzle and calculates d/D =24/66 = 0.36 exceeds limit of 0.33D for vessels over 60 in. ID. Alter-nate rules are also recommended.

13, Minimum required thickness of a downcomer nozzle is

t- = 0.lm(12) : 2.289 in. use ?i : 5l in.

14, Reinforcement area required is

A, = 6.294(24) = 151.06 in.2

Limit parallel to shell is greater of

d: 24 in. or T,'t T, + O.sd = 6.75 + 5.25 + 12 = 24 n.

Limit normal to shell is smaller of

16.875 in. or 2.5/5.25't: 13.125 in.

Area available in shell wall is

At = (2 x U - 12)(0.456) = 5.47 in.2

Area available in r:r.rrzzle wall; wall extends inward for 6j in. as fullreinforcing limit oulward:

At = 2(t3.t25)(5.25 - 2.289) : 77.73 in.'2

Azz : 2(6.5)(5.25 - o) : 68.25 in.'?

Total area available is

At = Ar r A21 I A22 = 151.45 in.2 > A, of 151.06 in.2

Also, check 'tlose-in" limit. Determine limit parallel io shell as thegreater of

0.75d: 0.75(24) = 18 in. or T" + T^ + r = 24 in.

Because the parallel limit is the same for the "close-in" limit, the arearequired of 0.674, is also satisfied without further calculations. I

Exrmple 11.5. Determine the minimum required thickness of a 36-in. IDcylindrical shell based upon reinforcement requirements. The nozzles arethrough-welded as shown in Fig. 11.9c and have 2.25-in ID on a staggered

16.

t7.

18.

19.

20.

I I,4 REINIORCEMENT IIMITS 357

Dattem of three fows on 3-in. centers and 4 5-in. longitudinal spacing, as shown

in Fig. I l.l l. The design pressure is 500 psi at 700"F design temperature The

allowable stress is 16,600 psi There is no corosion.

Solution

l. The minimum required thickness of the cylindrical shell is

PR 500 x l8" sE - o.6P 16,600 - 0.6 x 500

2. The minimum required thickness of the nozzle is

: 0.552 in.

3.

500 x 1.125 : 0.035 in.sE - 0.6P 16,600 - 0.6 x 500

Deiermine the reinforcement limits based on Ts = 1.125 in' and f,. =0.188 in. Limit parallel to shell surface = X = 2.25 in. or (1.125 +1.125 + 0.188) = 2.438 in., use 2.438 in.The limit normal to shell surface : y = 2.57" = 2.812 in. ot 2 5n =0.469 in., use 0.469 in.

2.25" diameter

Fisur€ I l.l I Muliiple op€ninss in cylindricol lhell.

Page 189: Process Equipment

358 OPININOS, NOZILIS, AND EXTIRNAI. I.OADINGS

4. Exnminc thc longitudinal plane l-2. Actual spacing = 4.5 in. parallcllimits without overlap = 2x = 2(2.438) : 4.875 in., exceeds actualspacing. Therefore, limits ovedap and special rules apply.

A,= dt,F = (2.2s)(0.552)(1.0) = 1.242in.2

Ar = (?i - r)(spacins d) = (r.tZs - 0.552X4.5 - z.z5) =Ar = 1.289 in.z

Az = (7, - t^)(2Y) : (0.188 - 0.035)(2 x 0.469) : 0.143 in.,A' = A1 t Az = 1.432 in.z

Asa = (0.552)(4.5X0.7 x 1.0) = 1.739 in.2

A561s: (l.125)(4.5 - 2.25') = 2.531 n.2 > 1.739 in.2

5. Examine the diagonal plane, 2-3. With a row-to-row spacing of 3 in. anda longitudinal spacing of 4.5 in., the diagonal spacing is \,tr + ZB: 3.75in.,0 = tan-' 3/2.25.0 = 53.13.. With a spacing of 3.75in.,the parallel limit of 4.875 in. exceeds the actual spacing; therefore, thelimits overlap and the special rules apply. From Eq. 11.16,F:0.5(cos2 0 + l) = 0.68 for g = 53.t3'.

A, = dt,F : (2.2s)(0.ss2)(0.68) = 6.30r .n.,

Ar = (4 - r'r,)(spacing - d) = (1.125 - 0.68 x 0.552)

(3.75 - 2.25) = 1.124 in.2

A: = 0.143 in.'z

A, = A1 ! Az = 1.267 in.2 > 0.845 in.2

A14a: (0,552)(3.7 5)(O.7 x 0.68) : 0.985 in.,4567s = 0.125)(3.75 - 2.25) = 1.688.in., > 0.985 in.,

6. The assumed values of T, = 1.125 in. and ?i = 0.188 in. are satis-factory. I

Problzms

11.6 What is the minimum required wall thickness (rounded uo to the nextl/8 in.) of a t2 3/4-in. ID nozzle atrached to a 60-in. d by 3.75-in.thick drum? The allowable stess of both the shell and nozzle material is15.0 ksi. The nozzle is attached by a full penetration weld with comerfillet welds with a throat of 0.7 ?i. The design pressure if 1400 psi at room@mperature.

Answer: t-in = 2.50 in.

I I,4 REINFORCEMENT IIMITS 359

ll.7 For triangular anangement of openings shown in Fig. I l.l I with oPen-

ings that are 2.25-in.lD, what is the minimum side length of a spacingthat forms a series of equilateral triangles?

Ans#sr.' Minimum lensth of side is 4.631 in.

I1.4.2 Reinforcemenl Rules for ASME, Section Vlll, Division I

The rules for reinforced openings in ASME Section VIII, Division 1, Pressure

Vessek, arc similar to those for ASME Section L However, the rules forreinforcernent are given as the main choice, with ligament rules used only as an

alt€rnative for repeating pattems of openings. Rules iue contained in both the

iext and the appendices. They are given for both internal pressure and extemalpressure. The rules are essentially the same except that only 50% of the replace-

ment area is required for extemal pressure assuming that the minimum requiredthickness in each case is based on the appropriate formula and design rules forboth intemal and extemal pressures.

N o Reintorcement Re quiNed

Single openings in vessels that are not subjected to special applied loadings, suchas cyclic loading, do not require reinforcement calculations if the openings donot exceed the following size limits.

1. In plate thickness of $in. or less, d,,. = 3-in. NPS.

2. In plate thickness greater than;i"., d* = 2-in. NPS.

Size anl Shape of Openings

The nrles apply to openings that are circular, elliptical, or obround. The lattershapes often result from an opening in a curved surface or from a nonradialnozzle. However, other shapes arc permitted when considered according tou-2(e).

For openings in cylindrical shells, the rules in the text are limited to openingsof the following size limits:

1. For shells 60-in. and less in diameter, the opening is not to exceed 0'5 Dor 20 in.,

2. For shells over 60 in. in diameter, the opening is not to exceed 0.33 Dor 210-in.

When these size limits are exceeded, in addition to the rules in tle text, the rules

in Appendix l-7 are also to be met. These additional rules may require some

reinforcement to be placed closer to the opening than required by the rules in the

Page 190: Process Equipment

360 oP!N|NOS, NOZZUS, AND CXTEnNAL tOADINOS

text. l.'tlr opcnings in sphcrical shells and lbrmed heads, the text rures are merby considering the use of reverse curves and conical sections where possible.There are no specific limitations on size and shape of openings in spherical shellsand formed heads.

Required Area of Reintorceme nt

The total cross-sectional area of reinforcement required for any plane through thecenter of an opening is given by

A: dt,F (ll.2l)

where d = the diameter of the opening on the longitudinal plane of acylindrical shell or any plane of a spherical shell or formed head(in.)

F : conection factor for pressure stress on plane being examined withrespect to longitudinal axis, as shown in Fig. 11.12. This factor isapplicable only to nozzles with integral reinforcement,

t, = minimum requked thickness of a seamless shell based on thecircumferential stress (longitudinal plane) or of a seamless formedhead with the following additional provisions:

1 When the opening and its reinforcement are totally within the sphericalpart of a torispherical head, l. is determined using the hemispherical headformula with both E and M = 1.0 (see Fig. t1.l3a).

2. When the opening and its reinforcement are in a cone, r, is the requiredthickness of a seamless cone.

3. When the opening and its reinforcement are in an ellipsoidal head andwithin a circle that is equal to 8070 of the shell diameter, r, is determinedusing the hemispherical head formula for a seamless shell of radius K1 D ,where D is the shell diameter and K1 is obtained.from Table 1 1 . 3 and asshown in Fig. 11.130.

The value of t, obtained from any of the methods given above is used onlyto determine the required area of reinforcement. The value of t" used to set theminimum required thickness of the shell or head is based on the thicknessfbrmulas that consider all the design loadings and weld joint efficiencies.

Limit of Reintorcement Parallel ta Shell Surlace

When the size of tle opening is within the limits in the text, the limits ofreintbrcement parallel to the shell surface measured on each side of the center-line are the larger of (l) d or (2) T" + Tn + 0.5d.

I I ,4 RETNIORCEMINT TIMITS 361

o" r;o 2oo so" aoo loo coo loo loo eoP

Arrelr ol Pt.na wlih Loneitldltral AtbFisur€Il.l2 Charr tor der€rmins F. (Courreiy Amsricon Socistv of l'lechonicol Ensine€rs, From Fis UG-37

of d's ASME Code, Vlll-l .)

Limit o! Reinforcement Perpendicular to Shell

The limit of reinforcement p€rpendicular or normal to the shell measured either

inward or outward from the surface of the shell is the smaller of (1) 2.57' or (2'S

2.5n+ L.

Avaibble Area of Reinforcement

When the reinforcement limits do not extend outside the zone of nominal wall

thickness of the shell and nozzle, the area available for reinforcement may be

calculated by the following formulas:

Page 191: Process Equipment

t62 OPININO!, NO! T!3, AND TXTIRNAT TOADINGS

1. Area available in shell wall is the greater of

41 =(2"d._d)(ET,_Ft)or

tu = 2(7" + T^ + 0.5 d) - d(ET, - Ft,)

2. Area available in nozzle wall is the smaller of

A,=(sDQ.-h)

A2= 6n+2.5t"\(7.-t,)

(a) rimits for

0.8D = sneci '1

forisphericat Head

(b) Limits for Etlipsoidaf HeadFigt r€ I L I 3 Dorerminorion of sp€ciol limirs ior determing t, to u!€ in roinfior€€rnenr colculations.

(11.22)

(r1.23)

(r1.24)

(11.2s)

When the size of the opening exceeds the limits in which the rules in the textapply' the supplemental rules in r-7 are used in addition to the text rules. Theseadditional requirements follow.

I I.4 REINTORCTMENT TIMITS

Tqble I 1.3'

D /2h 3.0 2.2 2.O

0.99 0.90Kr l 36

2.8

1.27

2.6l.l8

2.4

1.08

D /2hKI

1.8

0.81

1.6

o.73

1.4

0.65

1.2 l 0

0.57 0.50

Required Area of Reinforcement

The total cross-sectional area of reinforcement required for any plane through thecenter of an opening using rules l-7 is given by

A : 0.67 dt,F (l l.26)

Limit of Reinforcement Parallel to SheA

The limit of reinforcement parallel to the shell measured on each side of theopening centerline is the greater of (1) 0.75 d or (2) T, + T, + 0.5d.

Limil of Reinforcement Perpendicular n Shell

The limit is set exactly the same way as for a nozzle that is within the rules ofthe text.

Wlen any two adjacent openings are spaced so that their reinforcementoverlaps, the combined area is used, but is evaluated only once in the combinedarea. The preferred spacing is at least 1.5d"", with 507o of the area requiredbetween the two openings.

Example 11.6. Determine the reinforcement requirements of an 8 in. 1Dnozzle that is centrally located in a 2 : 1 ellipsoidal head. The inside diameterof the head skirt is 41.75 in. The allowable shess of both the head and nozzlematerial is 17.5 ksi. The design pressure is 700 psi and the design temperatureis 500'F. There is no corrosion and the weld joint efficiency is E : 1.0. See Fig.11. 13. 1 for details of a nozzle.

+^' o.taq"- T^r t'6

Fisure I l.l3.l Deroils of nozzle in exomple I L6.

Page 192: Process Equipment

t6a oPtNtNo3, NOZZII3, AND tXTrRNAt" LOAD|NGS

Solullon

l. The minimum required thickness of aZ: I ellipsoidal head without anopening is determined from UG-32(d) of the A3ME Code, VIII-I as

= = - 7oo (41'751PD

= 0.838 in.;zSE - 0.2P 2(17,sn x 1.0) - 0.2(700)

use 1.0 in.

As noied in the definition of r, ro use with Eq. 11.20 and shown in Fig.11.13.1, when an opening and its reinforcement are located in an ellio_soidal head and within a circle equal to 80Zo of the shell diameter, ,. tobe used in reinforcement calculations is the thickness required for aseamless sphere of radius K1D, where D is the shell ID and E for a 2 : Iellipsoidal head is 0.9 frorn Table 11.3. For this head, the opening andreinforcement are within 0.8 D = 0.8(41.75) = 33.4 in.Using the spherical shell radius of R = K tD = 0.9(41.7 5) = 37 .57 5 n.in the hemispherical head formula gives

! = = PR

= - 7oo (37.575)PR

= u. /f) rn.' 2SE - 0.2p 2(17,500 x 1.0) _ 0.2(700)

4. The minimum required thickness of the nozzle is

t

3.

9,

,^= PR' ='- sE - 0_6P

7OO (4)(17,500 x 1.0) - 0.6(700)

= 0.164 in.

!.

6.

,|

E.

Limits paraUel to head surface = X = d or (T, + T, + r), whichever rslarger. X = 8 in. or (4 + | + t.125 = 6.125 in.); use 8 in.Lirnits perpendicular to head surface i s y = 2.57, or 2.52,, whichever rssmaller. y = 2.5(1) = 2.5 in. or 2.5(1.125) = 2.813 in.; use 2.5 in.Because the limit of 2X = 2(8): 16 in. is less ihan 33.4 in. of item 2above, the provision of the spherical head may be used.Reinforcement area required following Eq. 11.20 is

A, = d+F = 8(0.7s5)(1.0) = 6.040 in.,

Reinforcement area available in head according to Eq. 11.21 is

A1 = (ET, - Ft)(U - d) = (1.0 - 0.755X16 - 8) = 1.960 in.,

Reinforcement area available in nozzle according to Eq. 11.23 is

Az= 57"(7, - tJ = 5(1.0X1.r25 - 0.164) = 4.805 in.,

10.

Figure ll.l,1 12 x 16 Monwoy op€nins detoils for exompl€ l l 7.

I t.4 RHNFORCEMENT UMI1S 365

ll. Total reinforcement available from head and nozzle is

A,: A1 'r Az: 1.960 + 4'805 : 6 765 in''

Area provided = 6.765 in.z > area required = 6.040 in.'? If additional

area is needed, use fillet weld area. I

Example 11.7. Determine the reinforcement requirements for a l2-in.x 16-in. manway opening. The l2-in. dimension lies along the longitudinal axis

of the cylindrical shell. The manway cover seals against the outside surface ofthe opening so that the opening nozzle is under intemal pressure' The ID of the

shell is 41.875 in. Both the shell and manway material have an allowable tensile

stress of 17,500 psi. The design pressure is 700 psi at a design temperature of500'F. There is no corrosion and the joint efficiency is E = 1.0' Details are

shown in Fig. 11.14.

Solution

1. The minimum rcquired thickness of the shell is found from

700 (20.938)":'::- = 0.858 in.:

(17,500 x 1.0) - (0.6 x 700)

use 1

2. The minimum required thickness of the nozzle is obtained as

PRt=-=- sE - 0.6P

, : --!lo- =' sE - o.6P

700 (6)

(17,500 x 1.0) - (0.6 x 700)= 0.246 in.:

use 1 i in.

ln.

-a-

ABCD=Limit of Reinf

Page 193: Process Equipment

OPININOS, NOZZUS, AND TXTERNAI. I,OADINOS

Uxuntinution ol thc longitudinal planc where t' = | .0 is determined tiomFig. l l.12.Limits parallel to shell, whichever is larger:

d: 12 in.

T, + T, + 0.5d : 6+ 1 + 1* = S+in.

Limits perpendicular to shell, whichever is smaller:

2iT, = 2.5(r) = 2.5 in.

2+r": z.s(1.25) = 3.125 in.

Reinforcement area required by Eq. 11.20 is

A,: dt,F : 12 (0.858X1.0) = 10.296 in.2

Reinforcement area available in shell by Eq. 11.21 is

Ar = (ET" - Ft)(2x - d) = (r - 0.85sX24 - r2) = 1.7s4.o.2

Reinforcement area available jn nozzle wall by Eq. 11.23

At = 57,(7, - t,,) = S(t)(1.2s - 0.246) = 5.020 in.,Azz = 57,(7, - t^) = 5(1)(1.2s - 0) = 6.256 ;n.z

Total reinforcement area available:

At = At + A^ + An = 1.704 + 5.020 + 6.25O-_ 12.974 in.2

Area provided of 12.974 in.2 ) area required of 10.296 in.24. Examination of circumferential plane where F = 0.5 from Fig. 11.12

gives the reinforcement area required by Eq. 11.20 as

A,: dt,F = 16 (0.858)(0.s) : 6.864 in.2

If the arc length of l6.4in. is used,A, = 7.036 in., Either of these areasis less than A. in item 3 and does not control. The longitudinal planeconhols. I

Example 11.8. Determine the reinforcement requirements for a 6-in. ID noz_zle that is located at the junction of a cylindrical shell and a hemispherical head.The entire opening is in the cylindrical shell, but ttre reinforcemlni extends inDotn drectlons-some into the head and some into the shell. The ID of the shellis 41.875 in. The allowable shess of all material is 17.5 ksi. The design pressure

3.

I r.4 RflNFORCTMENT UMTTS 367

is 70O psi at a design temperature of 500'F. All joints are fully radiographed witht joint efficiency of E : 1.0. There is no corrosion.

Solutinn

1. The minimum required thickness of the cylindrical shell from Example11.7 is

t = 0.858 in.: usel in.

2. The minimum required thickness of the head is

PL 700 x 20.938= 0.420 in.;

use I in.

zSE - O.zP 2x 17,500 x 1- 0.2 x 7W

3. The minimum reouired thickness of the nozzle is

Prt =-=" sE - o.6P700x3

= 0.123 in.;17,500x1-0.6x700use o! in.

4. Limits parallel to vessel surface, whichever is the larger of

d. = 6in.or

T, + T, + 0.5d= I + 0.75 + 3 = 4.75in.; use6in.

5. Limits perpendicular to vessel surface, whichever is the smaller of

2.5T, = 2.5(1\ = 2.5 in.

or

2.5f": 2.519.'lt, = l'875 in.; use 1.875 in.

Reinforcement area requhed by Eq. 11.20 is

A, = dt,F = 6(0.858X1.0) = 5.148 in.'z

Reinforcement area available in shell and head by Eq. 11.21 is

At = (ET" - Ft,, = (1 - 0.8s8X6 - 3) = 0.852 in.'?

Arz = (ETt, - Fil = (l - 0.420X6 - 3) = 1.740 in.2

6.

,1

Page 194: Process Equipment

3e0 oPlNlNos, NOZZ|tS. AND TXTEnNAT TOAD|NGS

E. Reinlorccnrcnt urea available in nozzle wall by Eq. I 1.23 is

Az: 5T,(T, - t') = 5(0.75)(0.75 - 0.123) : .2.351

in.2

9. Total reinforcement available from shell. head. and nozzle is

A, = Ar * Ao + A2 = 4.943 in.2, not enough

L0. Reinforcement area available in attachment fillet weld assuming legdimension of 0.5 in. is

43 = (0.5)'? : 0.250 in.'z

ll. Total including attachment fillet welds is

At = 5.193 in.z ) A, = 5.148 in.'? I

Problems

11.8 What is the minimum required thickness of the nozzle wall (rounded upto the next ] in.) of an opening whose reinforcement is based on anavailable area from both the shell and the nozzle? The opening has a15-in. diameter and is located in a cylindrical shell of 22-in. diameter.The design pressure is 450 psi, the design temperature is 450'F, and theallowable iensile stress is S : 15,000 psi. There is no corrosion.

Azswer.' Required nozzle wall th'ickness is I in.

11.9 Assume the nozzle in Example 11.6 is not centrally located in the 2 : Iellipsoidal head. Instead, some of the reinforcement area extends into theknuckle region. Is the available reinforcement area sufficient for thiscondition? If not, how thick does the nozzle have to be?

Azsrer.' Required nozzle thickness is ?, : 1.25 tn.

I 1.4.3 Reinforcement Rules for ASME, Section Vlll, Division 2

The rules for reinforced openings in Section VtrI, Division 2, are similar to thosefor Division 1 ; but there are some differences . Reinforcement limits and spacingare based on the damping length of a beam on an elastic foundation. The rulesare for either intemal or external pressure with no specific rules given forextemal loadings or for fatigue. However, there are stress inlensity factors thatcan be combined with the intemal pressure stresses to indicate the peak stressesfor fatieue.

I 1.4 REINFORCIMINT LlMlTs 369

Limilalions on Dimensians and Shape of Openings

'fhe rules are applicable to circular and elliptical openings and to shapes of

"p*i"gt "i ,ft" iti

"rsection of circular and elliptical cross-sectional nozzles' In

addition, the following limits also apply:

1. The ratio of the large to the small dimension of the opening is limited to

1.5.

2. d/D <0.5o.3. Arc length between centerlines of openings is limited to no less than

(a) Three times the sum of the radii for formed heads and the longitudinal

axis of cylinders.(b) Two iimes the sum of the radii for the circumferential axrs

4, The rules shall be satisfied for all planes'

For all dimensions and shapes of openings that are not within these limitations'

design-by-analYsis is used.

Openings Not Requiring Reinlorcement Calculations

Provisions are given for circular openings not requinng reinforcement calcu-

lations when ali the following requirements are satisfied:

1. Single openings with d*, = 0'2 V]4r and two or more openings within

a clide- with a diameter < z 5 \/fu , the sum of the diameters is

< 0.25 \/Rt .

2. Center-to-center spacing > 1.5( + d)'3. Center-to-edge of another local stressed area, where Pr is greater than

1. 1S-, is : 2.5 \/Rt .

Required Ana of Reinforcement

Thetotalcross-sectionalareaofreinforcementrequiredforanyplaneisgivenby

A: dt,F (1r.27)

where t, = minimum required thickness by either internal or external pressure

rules, as aPPlicable, (in.)

F = factor depending upon the plane under consideration' 1 0 for

formed heads and on the longitudinal plane' For nonintegral

connections, F = 1.0 for all Planes'

One-half of the required area of reinforcement is placed on each side of an

opemng.

Page 195: Process Equipment

T7O OPlNINO8, NOZZ!Is, AND IXTERNAI" I,OADINGS

Llmll of Relqforcement Along Vessel lVall

The limit of reinforcement along the vessel wall measured on each side of theopenrng when 10070 of the required area of reinforcement is needed is the largerof (l) d or (2) T, + T" + 0.54.

The limit of reinforcement along the vessel wall measured on each side of theopening when two-thirds of the required area of reinforcement is needed is thelarger of (1) r + 0.5 \Ar or (2) T" + f, + 0.5d.

Limil of Reinforcement Normal to Vesset Walt

The limit of reinforcement norrnal to the vessel wall measured from the vesselsurface is equal to the following:

f. fo1-FiS. 11.15a and b, it is the larger of (0.5 \/riI, + n or(1.73x+2.5b+ n < 2.57, and, < L + 2.5t,2. For Fig. 11.15c, when 45 degrees 2 0 > 30 Jegrees, it is rhe largerof

0.5 \Gn or (L' + Z.Stp) < 2.57,.

Y"if . 30 degrees, it is the larger of 0 .5 \/ffi or e.73x + 2.5t0)

3. For Fig. ll.15d, it is the targer of (0.5 \/r^I, + te) or (2.57., + t)= 2.57".

In both expressions above, t" is not to exceedI7 = width of added reinforcing pad.

For all cases, the terms and definitions are:

* = slope offset distance (in.)

0 : amgle from vertical

I' : vertical length of tapered section

r^=r+0.57:

Metal Availablz for Reinforcement

The metal available for reinforcement is obtainedwithin the limits established:

1.5[ or 1.7317 where

from the following areas

l. Excess vessel wall thickness2. Excess nozzle wall thickness which is integral or attached by full_

penetration welds3. Weld metal in fillet welds4. Pad attachment welds (where permitted)

, - 90 dca.

1Lt

Figur€ ll.l5 Deioil! for limir of r€inlorc€monr normol to vesrel woll. (Courtesy Anericon Soci6ty of,i..honi.ol Engin€€is: From Fis. AD-5,{0.1 of the ASME Code, Vlll-2.)

371

Page 196: Process Equipment

OPININOS, NOZZTES. AND EXTIRNAI IOADINOS

Pads (where permitted)

Metal from items 2, 3, and 4 meets the following:

l(aR - o.ilTl < 0.0008 (11.28)

where rri = mean coefficient of expansion of reinforcing metal at designtemperature (in./in./'F)

av = mean coefficient of expansion of vessel metal at designtemperature (in./in./'F)

Af = temperature range from 70'F to design iemperature or lowest tohighest temperature, if greater ('F)

Strength of Reinforcement Metal

1. 1.0 > &/,tv > 0.80.2. Adjust area by S./Sn not to exceed 1.0

where S, = allowable stress of nozzle material at design temperature (psi)

Sy : allowable stress of vessel material at design temperature (psi)

Alternative Rules for Noule Design

As the result of an extensive study for the PVRC5, it was determined that withinthe restrictive limits and rules that follow, a nozzle can be designed that does nothave 100% replacernent of an area but has the nominal strbss essentially main-tained.

Limitations

1. Circular cross section is perpendicular to surface.2. All integral construction use specified comer radii.3. Edge+o-edge of openings - 2.5 \/Fi.4. Material has tfslfs > 1.5.

5. Design is within the following dimensional limits:

Limit CylindersFormed Heads

and Spheres

D/td/Dd/\/Dt

6.

10-200

0.33 max.

0.80 max.

l0-2500.50 max.

0.80 max.

I I.4 REINFORCEMENT TIMITS 373

Required Area of Reintorcement

The required minimum area of reinforcement 4., is

Value ofdl\/Rt, Nozzles in Cylinders

Nozzles in SphericalVessels and Formed Heads

<o.20>0.20 and

< 0.40>0.40

14.os(d/\/-k)1tz- 1.811dt,

0.75 dt,

None, except 12 required None, except 12 required

ls.40(d/\/RDt/2- 2.41fdt,

dt, cos g, O = sin-\(d/D)

Limits or Reinforcing Zone

Reinforcing zone limits and reinforcing area are given in Fig' 1.1'16' Figure

11.17 shois the acceptable transition details. In order to use this altemative

method of determining the reinforcing area, all provisions of the procedure are

met,

Example 11.9. Determine the reinforcement requirements of an.8-in- ID noz-

zle tha:t is centrally located in a 2 : 1 ellipsoidal head. The inside diameter of the

head skirt is 41.73 in. The allowable stress of the head material is 20'5 ksi and

of the nozzle material is 21.6 ksi. The design pressure is 70O psi and the design

temperatme is 50OoF. There is no corrosion. See Fig. 11 18 for details ofnozzle'

Solutinn

1. The minimum required thickness of the 2 : 1 ellipsoidal head using Fig'

AD-2O4.1 of the ASME Code, VIII-2, is determined as follows:

; = ;* = 0.034 which siue. | : o.ozt

I = 0.9D = 0.9(a1.75) = 37 575 in.

t = O.OLLL = O.o2l(37 .575) = 0.789 in.;

use 1.O-in. thickness

Using AD-201(a) of the ASME Code, VtrI-2, the minimum required

thickness of the nozzle is

P 700x 4

t

s - 0.5P 21,600 - 0.700= 0.132 in.; use 1{ in. thickness

Page 197: Process Equipment

v.x.r 416, Nod.r

Cylindric.l Sh.llr

374 oP!N|NOS, NOZZ|tS, AND [XT!RNA| TOAD|NOS

bl A.inlo.d.r Zar. Li'irltl Lc- OSas li / RPI3R

fo. nozrld in cylin l.ic.l.h.th

l2l La ' 128 k./ 213|Bh/a+g.'tIfor notrl.3 in h.dt

(3) Th. c.ni.r or l. or L, i! .r llr. ionct!.. ot rh. ourrldrrorl.clr ol th! .hdl r.d .02116 of rhicknt.r, ...nd a',

{a) l. condrudioff whr. th. .o.. bosfthry p.$6 rhrollh. unilorm rhictn!3r mll r.gh.nr, th! .on. born.Lry m.y !a.on3id.r!d.31. o.l, through !h. thi.ln'.i

lll H.lch.d'..3 r.pr .nt !{.il.blc rlinlorc.hanrr..,a..

l2l M?r.l .1.. whhin rh. ronc bou..hry, in |rc.$ ot tha.raatorhcd bV ri. inr.rildion ot th. b.!ic rh.[r, rh.l ba conrida.ad.! conrrabutin! ro th. ..qut.rl &.., Ar, Th! b.jc th.[!.,rdrtimd .r h.vi.g iniid. r.di!! ,, thictn rt a, inrkt! r..liv. ,,

l3l Th. .vriltbl. r.'nldc.rn.nt .rx,4. ih.|tl b. .r t..tr.qo.l to I,/2 on ..ch rid. ol rh. norrlaornr.r ti...nd in rvawd.m co.r.iniq rh. nor2l..tir.

Fisurc ll.t6 Limits of reintorcine zone. (Courrely Amgrkon Sociory of rnechonicot Ensine€rs: From Fis.560.,{-l of the ASME Code, V t-2.}

3. Limits parallel to head surface are:(a) For 1007o or required reinforcement area:

X = d or (f, + f" + r) whichever is larger

X=8in. or (4 + 1+ 1.125) = 6.125in.; useX:8in.

(b) For two-thirds required reinforcement area is the larger of:

X' = r ! 0.5 \/ R^t or (T + T, + O.sd)

X' : 4 + 0.5 \,{3S.07sXD = 7.085 in. or 6.125 in.;

use X' : 7.085 in.

rr = o.ltro 0.5.

| ' > rh. tfEer ot r.41 \/A; o. tn

n ) the tz,sr otl.,/E7i6li,z] or lol9oltn

rr ) rtre targe. of I t - JitEil x 1.41 \,6or tl - l0l90,1 x l./21

" = {0' /90)r

0 end0' <45deg.

{.1

Figuro I I . I 7 Nozzlo d6tqil. 60r u3€ of olr€rnorive rul€t. (Courl$v Arnericon Soci€ry of tn€chonicol Engineers'

From Fig. AD-560.IJ of {'s ASME Code. Vlll2.)

T-1.o"

- o.'1a1"

Fisure tl.l8 Detcils o{ 2,1 ellipsoidol haod os givm in exomPl€ ll.9'

375

Page 198: Process Equipment

116 OPININOS, NOZZTES, AND EXTERNAT IOADINOS

4. Linrits nonlul to hcud surlucc, the lurgcr ol'

Y:0.5\/r^h + K or 1.73-r + 2.5rr,+ K.<2.57, and < L + 2.5h

v = o.s r{+s6rttll25) + 0.25 = 1.383 in. or

= 0 + 2.5(1.125) + O.25:3.063 in. <

2.5(l) : 2.5 in. and < 4 + 2.5(1.125) = 6.813 in.;

usel=2.5in.

5. Reinforcement area required for

1ffi7o: A, : dt,F : 8(0.789X1) = 6.312 in.'z

?: A, : ?(6.312) : 4.208 in.2

6. Reinforcement available with 1007o limit is

A1 = (r, - t)(2x - dr: (1.0 - 0.789)(16 - 8) = 1.688 in.'?

7. Reinforcement available in nozzle wall is

Az = 2Y(7" - t^) = 2(2.s)(r.rz5 - 0.132) : 4.965 in.2

8. Total reinforcement available form head and nozzle within 1007o rein-forcement limit is

A, = Ar r,4z = 1.688 + 4.965 = 6.654 in.'? > 6.312 \n.2

9. Reinforcement available with two-thtds limit is

Ay : (7, - Ft)(2X' - d\ : (r - 0.789)(2 x 7.085 - 8)

= 1.3O2 in.2

10. Total reinforcement available from head and nozzle usins two-thirdslimit is

A, = Ar r Az = 1.3o2 + 4.965 = 6.267 in.2 > 4.208 in.'? I

Example 11.10. Detemine the reinforcement requirements for a 12-in. x16-in. rnanway opening. The 12-in. dimension lies along the longitudinal axisof the vessel. The manway cover seals against the outside surface of the man-way. The 1D of the shell is 41 .875 in. The allowable stress of the shell materialis 20.5 ksi and of the manway material 19.4 ksi. The design pressure is 700 psi

I I.4 REIN'ORCEMENT I.IMITS 377

and the design temperature is 500"F. There is no conosion. See Fig. I l 19 tor

details.

Solutian

1. Strength ratio is, = D.a/?-0.5 = 0.946.

2. Using AD-201(a) of the ASME Code, VIII-2, the minimum required

thickness of the shell is

pR 700 x 29.93_8_ - = 0.728 in.. use I in.t = S:ojp 20-500 -T3o00)- - ''''o "'" ""'

3. Using AD-201(a) of the ASME Code, VIII-2, the minimum required

thickness of the nozzle is

Pr ,1oo I 9 =.=, : o.22o\n.: use 1| in.,., = s _ g.5p = lt70d= oJCdO - u.zzu ',r., u5

4. Examination of the longitudinal plane gives limits parallel to shell sur-

face as:(a) For 100% of required reinforcement area:

X = d or (f, + f, + r), whichever is larger

X= l}in. or (6+ 1+ 1.25) = 8.25 in.; useX = 12in'

(b) For two-thirds of required reinforcement area,

X' = r 4 0.5\/R"t or (2, + I" + r) whichever is larger

x' = 6 + 0.5\Cl.438XD = 8.315 in. or 8.25 in.; use

X' = 8.315 in.

ABCD=LirDit ot Rei.nforcemerltFigure 1t.19 Deloih of 12 x 16 monwoy op€ning in exomPle I1.10.

Page 199: Process Equipment

078 OPII{INOS, NOZZLIS, AND EXTERNAI. TOADINGS

(c) For limits normal to shell surface, the larger of

y=05\/VJ+x or

Y = 1.73x + 2.5te + K = Z.ST, and, < L + Z.Stp

y = 0.5\/6.625 x l2s + 0.25 = L698 in. or

Y : 0 + 2.5(1.25) + 0.25 = 3.375 <2.5(l) = 2.5 in. and < 3 + 2.5(1.25) = 6.125 in.

usey=2.5in.

(d) Reinforcement area required for

l0o7o: A,: dt,F + 2t"t,(1 - f)A"=12x0.728x1+2x1.25 x 0.728(1 _ 0.946)

= 8.834 in.,

+ A, = 4$.834) = 5.922 in.2

(e) Reinforcement available with 1007o limit:

A1 = (1 - 0.728)(24 - 12) = 3.264 in.2

(f) Reinforcement available in nozzle wall:

outward: 421 = 2(2.5)(1.25 - O.2n)e.946) = 4.872 in.z

inward: A22 = 2(2.5)(1.25)(0.946) = 5.9t2 in.2

(g) Total reinforcement with l00qo limit is

A, = A1 * Ar + A:z= 3.2& + 4.872 + 5.912 = 14.048 in.,At = 14.M8 > A, = 8.834 in.,

(h) Reinforcement available in shell with two-thftds limit:

A' = (l - 0.728r(2 x 8.315 - 12) = 1.259 in.2

(i) Total reinforcement with two-thftds limit is

At = At + Aa + An = 1.259 + 4.972 + 5.912 = t2.O4O in.z

A, = lz.MO > A, = 5.922 in.2

I I.4 REINFORCEMENT TIMITS 379

5. In examining the circumferential plane, reinforcement area required ac-cording to the ASME Code, VIII-2 is

A,: dt,F : 16 x 0.858 x 0.5 = 6.864 in.2

Using the arc length of 16.4 in., A. = 7.036 in.']Either of thetwo areasis less than 4, in item 4d and do not control. Longitudinal controls. I

Problem

11.10 A 10 in. inside diameter nozzle is attached by a full-penetration weldand comer fillet weld to a 48-in. inside diameter as shown in Figure11. 15b. The shell maierial is 5.4-266 Class 1 carbon steel and,the nozzlematerial is SA-182 F304 stainless steel. The design pressure is 1250 psiat a design temperature of 500'F. What is the required thickness of theshell, nozzle, and pad (if required) to satisfy the reinforcement require-ments?

Answer: shell, { = 2.5 in.

nozzle, To = 0 375 in'

Pad' t" = l'375 in'

I 1.4.4 Reinforcement Rules for ANSI/ASME 83l. I

Ruies for welded, reinforced connections according to ANSVASME 831.1,Power Piping, are similar to the rules for reinforced openings in the ASMECode, I and VIII-I. The following requirements give the basic considerations.

N o Reintorcement C altulalians Re quired

No calculations for reinforcement are required when the following limitsare met:

1. Connections made from fittings that have a standard pressure/temper-ature rating established.

2. d^:2-in. NPS with tn6 > Schedule 160 pipe.

3. d/D < 0.25.4. Standard fittings of extra heavy or Class 3000 rating.

Limitations. Angle between branch and run or nozzle and shell is between 45and 90 deerees.

Page 200: Process Equipment

3t0 optt{r],tot, NoTztlt, aND txrrRNAl loADlNos

Notatlons and Dsnnltlons. (Sce Fig. 11.20)

a = angle between nozzle and shell (degrees)

D, = outside diameter of run or header (in.)

d1 = (D" - 27,) /sin o(in.)dz = horizontal limit of each side of centerline, which is the larger of dy orT, + T, + 0.5/, but not more than D, (in.)1 = perpndicular limit : 2.54 + t, (in.)

Required Area of Reinlorcement

The lotal cross-sectional area of reinforcement required for any plane through thecenter of an opening is given by

A,: l.o7t^hdlz - sin d) (rr.29,

which for a : 90' is

A, = l.o1t*dl (1 1.30)

Avoi.lable Area of Reinforcement

The total area available for reinforcement is the sum ofAl + A2 + A3 + A4 +45 where each area is determined as follows:

Ar=(2dz-d)(7,*t,,t). zl(n - t'h)A1 = ---------1--

sm(I

(11.31)

(rr.32)

A3 = area of fillet welds

Aa : arca of reinforcing rings, pads, and so on.

A5 = area of saddles

Reinlorcement Zone

The limits of reinforcement are formed by a parallelogram with sides of d2 oneach side of the nozzle centerline and an altitude of Z perpendicular to the shellsurface.

Multiple Openings

The following should be applied:

l. Overlapping area shall be counted only one time.

r r.4 RHNFORCIMINI llMlt3 3tl

t, IT;-T

^N F.di6d 6lnro6m..t.r!. i a Ar.! A3 - rilld *ld dll't

N jml[mt a& A4 - ncor In rin!, prd. or Ini.s.lN' a6. at -.rc6wdl l. h.!d. dinro,c.d.nr tNol! {2ll

f Au A2 -.rcF wttl in br.nch l@' ar. 45 - m'ttt in td'!t doc tun

fislr6 I I .20 Dim€nlions ond not'otions for ANSI/ASME B3l l (Coud$v Americon Soci€tv of rn€chonicol

Ensinosru, From Fis. 1O'1.3.1D of ASMBANSI B3l'l )

2. Try to limit centerline spacing to 1 54" with at least 50% of area

between oPenings.

Example 11.11 A steam pipe has a 24-in' inside diameter with a design

oressul of Z5OO psi and an allowable stress of 14,500 psi at the design tem-

pera$re. A branch ptpe wtrn an rnside diameter of 8 in connects at an angle of

Page 201: Process Equipment

980 OPININO!. NOZZ[!S, AND IXTIRNAI toADlNos

Notatlone and Deffnltlons. (See Fig. 11.20)

a = angle between nozzle and shell (degrees)

D" = outside diameter of run or header (in')

dy = (D. - 24,)/sin o(in.)dz = horizontal limit of each side of centedine, which is the larger of d1 or

T, + T, + 0.5d, but not more than D, (in.)

1, : perpendicular limit = 2.5T^ + te (in.)

Required Area of Reinforcement

The total cross-sectional area of reinforcement re4uired for any plane tbrough the

center of an opening is given bY

A, = l.o7t,,hdt(2 - sin d) (1r.29)

which for a = 90o is

A, = l.olt*dr (11.30)

Avaihble Area of Reinforcenent

The total area available for reinforcement is the sum ofAl + A2 + & + ^

+45 where each area is determined as follows:

At=Qlz-d)(T"-t*). zL\T, - t*)Ar = -_---:--- sln a

(11.31)

(rr.32)

A3 = a'.ea of fillet welds

A+ = nrea of reinforcing rings, pads, and so on.

A5 = arca of saddles

Reintorcement Zone

The limits of reinforcement are formed by a parallelogram with sides of d2 on

cach side of the nozzle centerline and an altitude ofl perpendicular to the shell

surl'rce.

Mulliple Openings

Thc folkrwing should be aPPlied:

l. Ovcrlapping area shall be counted only one time'

| 1,4 RflNloRclMlt{T tl,ulTs lu

t,;rI

-T

rNvFr.diDdorntor6n.nr.n!iaa..!43-lilltt'|'!ldm'itlNv 4llD!l!II' eor aa - nrot in ri.s, p.d, or l.t trlN' a6. a1 -.'..sEll i. h..rL dinror.m.nr lNoa {2,1

f aE 42 -.r6.Mlt an bEnch l@' atle a5 _htnt innddttdd!run

Figur. I I.20 Dimaffions ond nolotions for ANSVASME B3l l (Court$y Americon Soci€tv oI tt€chonicol

Ensim€rs. From Fig. 104.3.1D of ASME/ANSI B3l'l )

2. Try to limit centerline spacing to l 54" with at least 5070 of area

between opemngs.

Example 11.11 A steam Plpe has a 24-in' inside diameter with a design

-"r.ui" of 2500 psi and an-ailowable stress of 14,500 psi at the design tem-

;;;;;.; ;;-.fi pipe with an inside diameter of 8 in' connects at an angle of

Page 202: Process Equipment

?82 OPININOS, NOZZITS, AND EXTERNAI. TOADINGS

o = 75'.'l'ho br&nch is &ttached by a lull-penctrutit)n wcld that is radiographedso that E = 1.0. Determine the thickness and reintbrcement requirements.

Solutinn

l. Determine the minimum required thickness of the run pipe as follows:

PR 25oo x trt', = Sf=-06p = 2.308 in.: use 4 : 2.5 in.

2. Determine the minimum required thickness of the branch pipe as follows:

Pr 2500 x 4.0t* = Sn _ oSt, = 0.769 in.: use 4, = 2.0 in.

3. Area required for reinforcement according to Eq. 11.29 is

A,: 1.07(2.308\(8X2 - sin 75') : 29.43s't.z

4, Horizontal limits of reinforcement are the larger of

d=8in. or 4+ nI r = 2.5 + 2.O + 4 = 8.5in.; use8.5in.

5. Perpendicular limit of reinforcement is as follows: Assume a 0.75 in.thick pad is added and attached by full penetration welds that are exam-ined.

L = O'75 in'L = 2.s7i, + t" = 2.5(2) + 0.75 : 5.75 in.

6. Area available for reinforcement is

Ar : (2x8.5 - 8X2.5 - 2.308) = 2.880 in.,

4, = 2(5.75\(2 :-o 7691 = 14.656 n.,

sln /J-

A, = (0.5)'z= 0.250 in.'?

ra = (2x8.5 - 8 - 4)(0.75) : 3.750 in.,A, = At * A2 + A3 + Ac = 21.536 n.' > A, = 20.430 in.2

Shell requirement: 24-:lr.. ID x 2.5 in. thickNozzle requirement: 8-in. ID x 2.0 in. thickFillet weld requirements: 2 with 0.5 in. legs

I I.4 REINFORCEMENT IIMITS 383

Pad requirement: l7-in. OD ring x 0 75 in thick

Nozzle attached to shell and pad by full-penetration welds' I

Problem

ll.lllfthenozzlewereattachedattt=g}",whatthicknessisrequiredforthe pad, if anY?

Answer: I in. thick Pad

I I.4.5 Reinforcemenl Rules for ANSI/ASME 83l '3

The reinforcement requirements for ANSI/ASME B31 3, Chemical Plant and

Petroleum Refinery Piping, are similar to the requirements for ANSVASME

S31. t and for Section Vtri, Dini.ion 1. Rules are given for branch connections'

oi no""l"., which are attached to run piping, or headers' Differing ftom other

,"info.""."nt "ul"ulations

, the minimum requiled thickness of the branch piping

anJ tne tun piping is measured on the outside thickness of the piping' The area

available foi riiniorcement is the remainder of the piping's nominal thickness as

shown in Fig. 11.21.

Limilations of Geomew

The angle between the nozzle and header is restricted to those intersections

where tle acute intersection angle B is equal to 45" or more'

Limitalion When No Reinforcement Calculatians Are Required

1. Standard fittings that have pressure/temperature ratings determined'

2. Standard fittings not exceeding 2-in. NPS that have d/D < O'25 and a

pressure rating of 2000 lb or more.

3. Integrally reinforced connections that have been proved adequate by

tests, calculations, and use.

Nomenclature

4 = opening size in run or header (in')

dz : horizontal limit on one side measured from the centedine of the open-

ing (in.)

l+ : vertical limit perpendicular to header surface (in')

F : acute angle at intersection (degrees)

,,, = required thickness of header (in.)

Page 203: Process Equipment

g--t:-

t;-i.-ie:IaE:;eg'E

*r(t

t2ic6!l

lI

III

fa---{--J_iI

6'o

E

\,3E

'6- 1

12<{9aE'6

E-iE8

96En+is95az6q:

9iii'6

i

I

.l

4 = nominal thickness of header (in.)

t6 = required thickness of branch (in.)

?i = nominal thickness of branch (in.)

D6 = outside diameter of branch (in.)

D,, = outside diameter of header (in.)

384

I L4 RllNrgRcltllllr I Llmlrt

Requireil Area of Reinforcement At

For intemal Pressure,

Ar = ttdrQ - sin F) (1 1.33)

(11.36)

For extemal Pressure'

(11.34)

Horizontal Limits. The horizontal limits on each side of the centerline of the

nozzle is the larger of

d1 or T1+4+05dI

but not more than D1,.

Vertical Limits. The vertical limit measured from the surface of the shell is

the smaller of

2.5T, or 2.57b + 4, where 4 = pad thickness (in')

Areas Available for Reinforcement A2, Aj, and Aa

Excess thickness in header or run ,42 is

A2: (2d2 - d)(Th - th)

Excess thickness in nozzle or branch A3 is

(11.3s)

. thd(z - sin B)ar: -----T-

. 2L4(Tb - tb)a^ =

-

sin P

In other metals available within limits Aa, if reinforcement metal is weaker than

;;r-;i;;,J,,h" area available for rcinforcement is reduced by Sn/Su'

Reinforcement Zone. Excess area within the following is considered accept--iii:, ut " La, wtrl.;e La is measured perpendicular to shell surface'

Muttipte Openings. The following cautionary rules are to be followed:

1. Center-to-center distance of at least 1'5du"'

2. At least 5O9o of the total required area between the openings'

Page 204: Process Equipment

rrc optt{tNot, t{ont|t, AND tXTlRt{Ar toADtNOS

Oxnmplc I l. 12. An tt in. NpS Scherlule g0 bronch (nozzle) is attached at rightangle to a 20-in. NPS Schedule 40 run (header) with a full penetration weld withfillet weld cover. The allowable stress is 13.l ksi. Design pressure is 600 psi ata.design temperature of 900.F. Determine the reinforcin-g requirements and padsize, if required.

Sohrtion

l. Determine actual and minimum required sizes at the branch run inter-section as follows:

4 = (0.s93)(0.875) = 0.519 in.

{, = (0.s00)(0.875) : 0.438 in.

th: PD/2(SE + py) = (600 x 20)/2(13,100 + 0.4 x 600)

= 0.450 in.

b= Pd/2(SE + PY): (600 x 8.625)/2(13,100 + 0.4 x 600)

= 0.194 in.

Fillet weld size is the lesser of 0.7?i or i in.;

0.7(0.438) = 0.306 in.; use fillet weld,ir" = | in.

2. Determine the horizontal limits of reinforcement from the following,whichever is the greater:

d1 = (8 - 2 x 438)/sin 90" = 7.125_in. opening size

dz = (0.519) + (0.433) + 0.5(7.125) : 4.519 in. ord2 = it : 7.125 in.; use d, : 7.125 in.

3. Determine the vertical limits of reinforcement from the following,whichever is less:

L4 : 2.5(0.519) = 1.298 in.

or

Lq = 2.5(0.438) + 0 : 1.095 in.; use Za = 1.095 in,

4. Determine the reinforcing area required according to Eq. 11.33 as fol_lows:

41 = (0.450)(7.125)(2 - sin 90.) = 3.206 in.,

I I.5 TIGAMENT EFFICICNCY OF OPENINGS IN SHCLI.S 3A7

5. Determine the areas of reinforcement as fbllows:Excess in run (header):

Ar : (?.125)t0.519 - 0.450) = 0 492 in'z

Excess in branch (nozzle):

Ar = 2(1.095)(0.438 - 0.194) = 0.534 in '

In fillet welds:

Ao = 2(r()2: 0.063 in.2

Excess area in Azr Az + Ao = 1.939 in'2 This is less than '4r; con-

sequently, a pad shall be provided. Determine the thickness of pad based

on the pid extending to the horizontal limits of reilforcement'

(7.r25)H = 3.206 - 1.089; Il = 0.297 in.

Assuming f, = 5116 in. determine minimum pad width'

(2w - 7'r2s)(0'3125) = 2'117

W = 6.95 in. Use 14 in. x 5/ 16 in. pad.

45 = (14 - 7.125X0.3125) = 2 148in2

Available area of reinforcement in A2 + A3 + A4 + As = 3 '237 in''This is greater than A1 and therefore is satisfactory'

It may be possible to obtain more refinement and a thinner or narrower plate by

reevaiuating the vertical limits by setting T, : 0 312 in and by including the

outer fillet;elds if they lie within the horizontal reinforcement limits' This

recalculation may reduce the pad thickness and/or the pad width However, a

14-in. by 5/16-in. pad is satisfactory. IProblem

11,12 For the construction in Example 11 . 12, what is the maximum allowable

working pressure when the allowable stress is increased to l8'8 ksi?

Ansper.' MAWP = 880 Psi

I 1.5 Ligomenf Efficiency of Openings in Shells

In addition to the method of reinforced openings for compensating for metal

removed at openings in shells, there is the method of ligament efficiency The

Page 205: Process Equipment

318 oP!N|NOS, NOZZUS, AND TXTTRNAL TOAD|NGS

ligoment el'licienoy method considers the loarJ-carrying ability of the area bc-tween two points in relationship to the load-carrying ability of the ligamentreTltlilg when the two points become the centers of two openings. In thcASME Code, only the shell plate is considered; however, Lloyd;s Rulis6 permitsome help from integrally attached nozzles.

The basic method of diagonal ligament efficiency for application in thcASME Code was developed in 1915 by Black and Jones oiihe Babcock &Wilcox Company, which was published in 1920 in the Marine Engineer'sHandbook.T ln 1975. a limit design analysis was used to examine suesses ln aperforated cylindrical shell.8 This limit analysis was further developed forASME Code application and used to update the original code rules. The rulesand curves are still given in several sections of the ASME Code and severalforeign codes that determine the ligament efficiency used in the cylindrical shellformulas.

The ligament efficiency curves apply only to cylindrical pressure vesselswhere the circumferential lension (stress) has twice the inbnsity of the longi-tudinal tension (stress). Once this was established, Rankine's Eilipse of Streiswas used to determine the iniensity of lension and of shear on any diagonalligament. This is shown in Fig. 11.22. The total tension and the total shear areottained by multiplying the intensity of tension and of shear, respectively, bythe diagonal pitch between openings and by the shell thickness, as ixpressed bythe following equations:

Figur. I1.22 Diogonol ligoment!.

I I.5 TIOAMENT EIFICIENCY OT OPENINGS IN SHEITS 389

cos2 0 + Iintensity of tension on any plane

sin d cos d

(11.37)

( l 1.38)

(11.41)

(rr.42)

intensity of shear on any plane :

total rension _ cos, g + l(p,4) (11.39)z

sin A cos A. ,-,rotaf shear: *\p'T,) ( 11.40)

The stress factor for tension for any section of the ligament is obtained by

dividing the total tension by the cross-sectional area of the ligament. The shess

factor for bending for any section of the ligament is obtained by dividing the

bending moment of the section by the modulus of the section. The bending

moment is the product of the total shear multiplied by the distance between the

section considered and the point of contraflexure, which is the plane passing

through the centers of the openings. The distance is Y in Fig. 11 22'

length of ligament : L = P' - \/F=4bending moment = (6161 shear)(I)

section modulus :+:tg-P (11.43)

The stess factor fot tension is determined as follows:

^ cos20+ 1 (p'T,\"' 2 lp'-\/d2-4Y'z)T,

(11.44)

The stess factor for bending is determined as follows:

sin 0 cos 0 (11.45)Sa=

The total stress factor for both tension and bending is the sum of the stress factors

for tension and for bending. When the curve was originally developed for the

ASME Code, the maximum total stress factor was found by tial by calculating

the shess factor at several sections between the sections through the centers ofthe two openings to the plane that is tangent to the edge of the openings. Table

I1.4 shows a sample of this calculation to determine the maximum factor for aparticular angle ;ith the longitudinal axis 0 values of p' /d and a shell plate

thickness I.

Ie' - t/F - +-qv'f la

Page 206: Process Equipment

390 OPININOS, NOZZITS, AND EXTERNAI IOAOINOS

Undcr the sponsorship of the Pressure Vessel Research Committee, an exten-sive limit design analysis of perforated cylindrical shells with uniform patternsofopenings was completed. This limit design analysis was used to determine theupper and lower bounds of limit pressure. A 2 : 1 ratio of stress field wasconsidered and the shell plate curvature was not included. From this analysis,the basic lower bound equation was develooed into

PLqb = 2I + cos2, - d/P\4 +-5io?n

(11.46)1+3cos20

For application in the ASME Code, the equation was rearranged so that thediagonal efficiency term was expressed as p' /d, a number equal to or greaterthan 1.0, and the efficiency was expressed as a whole number. The equation forcode use is

/"-^ a\sec2 o + I - I "':;YI\A + sd2-7

- \P /d|'- 0.015 + 0.005 sec2 0

Calculations of minimum ligament efficiency was determined by examiningvarious planes between openings at different distances of I as shown on Fig-I1.22. An exanple of the calculations based on the original ASME Code workis given below. It has io be repeated for different values ofp ,/d and for variousangles 0:

known data: d= 4 in.; s = 6in.;0= 35.;I = 1in.

calculated dnt^: p': s/cos d = 6/cos 0 = i.32-in.f; =ffi = t.AZ

ToblE | 1.4

(1r.47)

I,engthand Total SectionArea Tension Modulus

Total Bending TensionShear Moment Factor

BendingFactor

TotalFactor

o 3.320.50 3.450.75 3.62

0.90 3.'15

1.00 3.86

1.50 4.68

2.00 7 .32

6.126.126.12

6.12

6.12

6.126-12

1.84

1.98

z.t82.34

2.48

3.65

8.93

l.'t21.72

|.721.72

1.72

t.'72

1.72

0.861ro1.55

1.72

2.58

3.44

r.E4

r.771.69

1.63

1.59

1.31

0.84

o.43

0.59

0.66

0.69

0.'t I0.39

I .84

2.202.28

2.29

2.28

2.O2

1.23

I I.5 TIGAMTNT Eff ICIENCY OF OPENINGS IN SHEIIS 39I

The lowest factor is used to calculate the minimum efficiency for the angle 0

being examined.

efficiency : -l- = O'437 : 43 7vo2.29

Examplell,l3. Determine the minimum required thickness of the shell givenin Example 11.5 using the ligament efficiency rules.

Solution

1. Determine the longitudinal efficiency based on the longitudinal spacingof 4.5 in.:

^'- I A\-2)5E=r '= -:::------:j::: O {0f)

p' 4.5

2. Determine the equivalent longitudinal efficiency from the diagonal effi-ciency using Eq. 11.47 as follows:

0=53.13" d=2.25 l=w sec0:1.667

EVo =

EVo =(1.667)2 + | - (r.667 / r.6T\/t + Q.667f@ = 47 .59?o

Determine the minimum requAed thickness using the equation of UG-27(c)(l) from the ASME Code, VI[-l, as follows:

PR 500 x 18t = sE - oip = C3oo;04i6 -10=.ox-500 : r'164 m'

This thickness of , = 1. 184 in. is based on the shell thickness only withno contribution from the nozzle. I

Problems

11.13 What must the angle d be between two openings for the longitudinal and

diagonal efficiencies to be equal when the longitudinal spacing is 4.5 in.and the opening diameter is 2.25 in.?

3.

sec2 53.13' + 1 - (sec 53.13)/1.67\,6 + s-7 51ly

Answer: Angle with longitudinal axis is 0 = 54.1'

Page 207: Process Equipment

392 OPININOS. NOZZIES, AND EXTERNAI. TOADINGS

ll.l4 ln Problem ll.l3, what is the circumt'erential spacing for the samcconliguration'l

Answer: The circumferential spacing is 3.108 in.

I I.6 FATIGUE EVALUATION OF NOZTES UNDER INTERNALPRESSURE

When a fatigue evaluation is required, it is necessary to determine the peakstesses around the openings. The current methods are the stress index method,experimental 0ests and measurements, or a theoretical analysis procedure suchas a finite element analysis. The stress index method is the easiest method andis allowed by the ASME Code, III-1 and VIII-2. The stress index method wasdeveloped from reviewing a large amount of experimental and analytical datadetermined in a program conducted by the Pressure Vessel Research Committee .

The stress index method pennits easy calculation of peak stresses at thenozzle-shell or nozzle-head intersection without resorting to any complex anal-ysis. The stress index method gives conservative results; and if the exact multi-pliers for a specific geometry are known, they should be used. Essentially, thenominal stress in the shell or head is multiplied by the stress indices and the peakshesses are obtained.

The peak stresses are determined from the following equations where theshess index I is multiplied times the nominal shess.

For spherical shells and formed heads:

.PD. (11.48)

For cylindrical shells:

I I.6 IATIGUE EVAI,UATION Of NOZZTES UNDIR INTERNAI PRISSURI 393

where R = inside radius of shell or head (in)

r = inside radius of nozzle (in)

4 = nominal thickness of shell or head (in)

D. : mean radius of shell or head (in) = 2q * tP = intemal design pressure or pressure range (psi)

I : stress index for various locations (see Table 11'5)

o, = normal stress in plane being examined (psi)

or = tangential stress in plane being examined (psi)

o, = radial stress in plane being examined (psi)

Example 11.14. A cylindrical shell that is 36-in ID by 2'5-in' thick contains

a perpindicutar nozzle that is 4-in. ID by 0 75-in thick' The design pressure is

td00psi at a design temperature of 450'F. The vessel is subjected to cyclic

operation and a faiigue analysis is requircd' Peak stresses and- str-ess concen-

dation factors are noi known for the specific geometry to be used' What method

can be used to evaluate the peak stresses for a fatigue analysis?

Solutian. At the intersection of the nozzle to the shell, peak stresses are

obtained according to Eq' 11.48. The nominal stress is determined as

_ : PD^ _ 1900(36 + 2.5) = 14.630 psi" 2T, 2(2'5)

The peak stresses are determined as follows using the factorc for stress index Ifrom Table 1 1.5:

Longitudinal Plane Transverse Plane

Stress (psi) Inside Outside Inside Outside

+ t4 ,630 +30 ,720

- 2,930 +38,040

- 1,900 0

.PD.o= t n (11.49)

Toble I1.5 Stress lndex /

Hoop stress

lrngitudinal stress

Radial stress

+45,350

- t q10

- 1,900

+ t7 ,560+ 14,630

0

Cylindrical Shells These values are the peak stresses due to intemal pressure only and must be

combined with other peak stresses occurring at the same location on the shell for

a.fatigue evaluation. I

Problem

11,15 A reactor vessel is 5 ft. 0 in. inside diameter with hemispherical heads'

The design pressure is 450 psi at 650'F The allowable stress of the

Spherical Shells andFormed Heads LongitudinalPlane TransversePlane

qr

1.2

1.0

0

a1

z,o

0

2.0 - (r/R) 2.o - (r/R)

-o.2 2.O - (r/R)

-4r"/D^ 0

3.I

-0.2-2r"/D^

1.0

-o.2-27"/D. :

&

Page 208: Process Equipment

OPININCS, NOIZI-TS, AND IXTtRNAt TOADINGS

vcsscl is 17,5(X) psi. l'hc hcatl and shcll rrc nradc ol.rrinirnurn thickncssr)alcritl roundod up to (hc ncxt I in. Thc vessel is operated undcr ircycling conditkrn.so.that a fatigue analysis is n"""r.ury. It is necessaryto place an 8-in. inside diameter by l-in. thick nozzle, in the vessel. Isthe peak stress less in the head or in the shell at the nozzle junction andwhat are the values ofpeak shesses at the maximum location in ttre treaaand shell? Thin-wall equations are used.

Answers: oFar = +48,510 psi in shell

o''.*, = +27,220 psi in head

I I.7 TXTTRNAL IOADINGS

Extcmal loadings cunsidered by W/?Cl arc longitudinal nx)r)lcnt, tr nsvcrser)lorncnt. torsional moment. and axial fbrce. Stresses at various locations on thcinside and outside surfaces are obtained by combining the stresses from variuusoffects. This involves considerable "bookkeeping" that WRC 107 developed t<r

help alleviate. Once the stresses are obtained according to WRC, they must be

combined with intemal pressure stresses to determine the overall stresses.

Bijlaard's original problem was finding the effects of structural supports ona cylindrical shell. This initial work considered the radial loads and momentsover a flexible, rectangular loading surface. The initial treatment of nozzles wasan approximation based on a rigid attachment without the effects of nozzle wallflexibility. Bijlaard extended this work to spherical shells based on a shallowshell theory and considered both solid (rigid) attachments and nozzles withflexibility parameters. Usage of the rules is generally limited to D/, between 10and 200 for cylinders and between l0 and 250 for spheres. Usage is also limitedto d/D oI about 0.33 for cylinders and 0.50 for spheres. However, dependingupon other parameters, the value of d/D nay go as high as 0.60 for somecylinders. A limit of 0.80 is also applied to the value of d/YD^T for bothcylinders and spheres.

The curves in WRC 107 are related to certain parameters at the intersection.The two important parameters are the shell parameter and the attachment param-eter. The different applications on spherical and cylindrical shells follow.

Spherieal Shells

The shell oarameter is

I I.7 EXTERNAT LOADINGS

When extemal loadings are applied to nozzles or branch piping, local saessesare generated at the nozzle-shell intersection. Several typis of ioading may beapplied, such as sustained loadings, transient loadings,- ind thermal

"*paniionflexibility loadings. Sustained loadings are continuorisly applied and combinedwith iniernal pressure, such as dead Ioads. Transient loadings are applied for ashort period of time, such as earthquake and wind loadinls, pressure fluctu_ations, and water hammer loadings. The thermal expansion Ioadlngs are causedby

-the potential axial growth of piping from temperature expansion.

. When external loadings are applied to nozzles, stresses are generated in boththe nozzle and the shell or head. Although the stresses in thJ nozzle are bothmembrane stresses, which are acting upon the entire nozzle cross sectlon, andlocal membrane stresses, which are aciing through the nozzle wall thickness,present analysis procedures are available only for the general stresses withoutresorting to some procedure such as a finite element

-analysis. These general

procedures usually have a way of applying a stress intensihcation facto; (SIF)that predicts the local stresses in the nozzle. The stresses generated in the shellor head adjacent to the nozzle are-focal stresses. A proce-<lure for determiningthe_se local stresses is given in detail in Welding Reseirch Cor,rncji, Bulletin NolttJ7 "

| | .7.1 Locol Stresses in the Shell or Heod

Although a considerable amount of theoretical development work on localstrosses in shells from external loadings was conducted ind reported by p. p.

ff iiJyalff'r in the early 1950s, it was not until rhe Welding Risearch CouncitIlulldinNo. 107 was issued that all the miscellaneous inforriation from Bijlaardand others was put into a concise form for easy use. The range of usige isrcslricted by limitations on various parameters,'but it is infinitily better thananything before WRC 107 was issued. Currently, experimental and theoreticalwork is being conducted to extend its useful ranse.

:t : r0" ..fn;r

For a square attachment, the shell parameter is

It = c1

" o.875\-RJ

t

In the attachment parameter for all solid attachments, no parameter is needed.For a hollow cylinder (nozzle),

(11.s0)

(l1.sl)

(11.52)

(1 1.53)TI

Page 209: Process Equipment

396 OPIN|NOS, NOZZLES,

l.br a hollow squure,

AND EXTERNAI I.OADINGS

0.875t

T't

Cylindrical Shells

The shell parameter is

The attachment parameter for both solid and hollow is for a cylinder

I t.7 EXTERNAT T.OAOINGS 397

proper values must be read carefully because it may be necessary to interPolatenot only from line-to-line but from curve to curve. The values on adjacent charts

do not always increase or decrease in a consistent direction. Computation sheets

are given for:

Figure 11.23. Solid attachment to a spherical shell

p1::

(11.54)

(r 1.ss)

(1 1.56)

(r 1.57)

(1 1.58)

v, ._ to. '- ,/l;r =-

t,/Ri =-

For a square,

For a rectangle

e=o8i:.

= *g where cr

C!

R.

c2

R^

F,

B,

If

u= f' -*(f; -'),' - n)\/e,k 01.5e)

t. r, u = [' - i(' - f;),' - K))\/e,e, (1r 60)

Using these parameters and the curves given in WRC 107, stresses may becalculated at the inside and outside surfaces due to the various loadinss. The

t,,If

Figure 1'1.23 Computotion sh€.t for rigid onochment to.Phericol shell. (Courr.sy Welding Reseorch Council,

WRC Sulloiin lO7. A',s'Et 1965,)

;I

Co}.IOIN,jD S?RESS INTDNSII1 - S

l ) Hhcn r I o, s - I rrI:L-lL!j-$-c--[.!qi it u r" 4f 4ith:r \s - l/2 lox+oy ! llox - ay)2 | at2 Jot r'tax - oyl' ' 4r'

2) r,then t = o, s = largest absolur. ndgnitudc of eithers - dr, oy or (ox - oy)

Page 210: Process Equipment

TFigure 11.24. Hollow attachment to a spherical shell F-igure 11.25. All attachments to a cylinclrical shell

MtMcM"L Appliod Lootir'

Rodiol looC,CirG. l5h. hl,Long. Xolttl,Tonica f,oronl.thocr Lccd,Slcr Lcod,

2. GoaaryVorrrl thicllorr,Arccharat rt,dlur,Yorrol odior.

p =

-15.g.;

-in.fb.|lL:-i6. lb.lr =-_i^.

lb.vc -- lb.VL --lb.

T,

-an.aC g

-rn.Rn:

-

a^.

GF6atfia Pc?omalcra

Rh't T=-P to.orsr*.-

'NOTE: Enrrr cll fcrco volvcr in

cccordoncr rilh aign co'vcition

ov!

ROUNDATTACHMENTl. Appl,cd Loodr'

Rod,ol Lood,Shror Loqd,Shcor Lood,Ovc.terning Mom.nr,OvGrturhrng Moarcnt,lorrronol Momcnt,

3. Gemrtric Poromctcrr

e=-lb. "_

.*vt2_lr. . z : =-v,

-lb'.-

02 r -M,

-

an.lb.. '-i:

-if.lbr: ,'j# =-

CYLINDRICAL SHELL4. 5t.a3r ConcGnt.oiion Focfora

dua lclrncnbrono lcod, ;,, =-bending lood, Kb a-

NOTE: Entc. oll torcc voluor inoccsrdoncc wrth rign convGnlion

Figvre 11.21 Computotion sheet for hollow otiochmenl to sphericol shell. (Courtesy Welding Reseorch

Council, WRC Bullerin 107, August 1965.)

398

Figure I1.25 Computotion sheei for qfiqchmenis to cylindricol shell' (Courtesy Welding Reseqrch Council,

WRC Bullefin 107, August 1965.)

Frcm

fr g.

Rcod <urv

lor

Conpvtc obtolvtc volcer ol

alicrr cnd antar ratull '

STRESSES - il lood ii cpporilG rhor rhown, rcvcrtc tignr rhorn

AU L 8u BL €u CL Ds

5P-l to l0 XrlF *^ (s,')'? =

T *'(ts)' *l= F + + f

5r4- | ro l0 N,rfiiTilt

/ N,r\r/E;T\ r r^'\T/ '' = f +x.r/T;T la.lili \ 6*{,

xb t- i'- =\ M, / r.y'nnl f +

@Ht

/ x,rlr/ffii\ r,\ t 7'ii7ffi= + +

u.y'Ti.'itt

1r-,{ffi \ 6M:I : I

\ rr / fr{R6f + +Add olgcbroicolly lo, .ummol;on of r, r,

lP- I ro l0 + /xvT\ ?\ P / T?

ItT -'(+) ';l ' # + + t3lr-l to l0 xyrr/if

Bl7 xrr,r/-.i\ r,-"\T/'iffi= f .t-

xyrr/EiTr.,

+ f

xrr/F;-ixt

//Nrry'nhr \ r,""\--*l-/.ffi= .l- +

xv1fiiTr 7xyffii \ 6tr*'\;;_/.ffi= f {-

Add olgebroicolly lor rumnofion of rr

Sh.or.t..r. de.ro lod. Yr fr t

=,+I r

Sh.o..tr..r de.ro lood, Yt r, ofr7 {- f

:h.cr !tr.!. d!. li --,7t- :*+- t r + + + + + I

Add ofgrbrorcolly lo' rua^ot,oa ol t . a

COMBINED STRESS I}ITENSITY - S

" 1"1",),* t3; -'", 1",1fifffi;?l'5'll'lli#,Fa2) Hhen t = Or S = largcst .,rbsolute rnagnitudc of either

S .' O-r qv or (o- - g.l .

SfngSSfS - il locd i. cPgotilc rhot ;ho-n, "vc?t'

t'9nr 3hM

Fig lor rlrarr ohd anlar tlagll ' rL Eu 8L Cu CL DL

3c orcc

x6_?/2,a

/Nd\(n t- l\?/ rh /

?

=lnl

lC or2C- I

roF-

/rd\f,b | -

I

6P

=l2 t l- +

!A,.0 _t ta^26 -

-"(""ft)'#= f t-

IArd

-=rc/ tnE

t- t-

taxo

IL,/ tra6l-^(-#)'# = I P

I I orIt-r

r9IL/ trlt

/ 16\t5l-l\nzr-B /

6fLr-Prr - + +

Adi rlgoltiolly |.. .r6droof { rroror.od *

3C orac

-g-? t?,a - .. (*,)' -! r

lc-1or 2C F

rr (3).8 =\ r/ ta + f I

irffiE' *(#)'#?' I t

2Atr

J.c/l,aPt At \ 6l{cxr\;ta,B-'l' itffi =

I +

a! r_E

rL/litp '"("-fo)'IL

;;EF - t +

---{a .,2t-l rllrrp - "(""+-r'#= + +

A- olgrleially f.t D.-tl-

ol | $tott.lCt €

5br lror Joro l*rio, I

' l{trrlr < {rP = 2nc2o' + ? r f + t F t-

lh-r dr.. ar.ro ld, Yc T,+ = "F + F

llorr rtnrr &rr. l-4. YL

Trd = YL;;T

f +

Ala ^halnlollt

f-.*tl6at rb-r rtroaaar,ft

-s1) tJtren 'E I o, s = lar@itudg of eithEl t

s = l/2 fo**o* ! /to* - o0)2 + 4t2 )or r'(ox - o4)d + 4T-

2) Wtren T = O, S = largest absolute magnitude of eitherS = olr oO or (O* - 06)

399

Page 211: Process Equipment

4OO OPTNINOS, NOTZIIS, AND TXTTRNAL IOADINGS

In addition tt) thc linritllions ()n tlrc gcorlrctty in thc anitlysis in MiC, thctcarc othcr lirnitations. 'Ihis analysis detennines only the stresses in the shell orhead due to the extemal loadings and thus those from intemal pressure must bc

added to them. Because no nozzle stresses are determined by this method, theymust be determined by a separate analysis. However, engineers felt that whenthe extemal loadings are applied to a relatively thin-walled nozzle, the higheststresses may be in the nozzle. For thick-walled nozzles, it appears that defor-mation is similar to a solid attachment and maximum stresses will occur in theshell or head adjacent to the nozzle. Bijlaard's method indicated that for a

longitudinal moment, the maximum stress occurs on the longitudinal axis.However, experimental results obtained in PVRC tests indicate that for largernozzles with ad/D = O.5 or larger, the maximum stress may lie somewhat offfrom the longitudinal axis. Thus adjustments have been made to some of thecurves in l\lfiC Bulletin 107. In spite of these shortcomings, a reasonableestimate of the stresses due to the external loadings is obtained by followingwRC lo7 .

Recendy, in considering certain PYRC work to extend the ueful range ofWRC 1O7 , J. L. Mershon concluded that within the range of its applicability, thecurves for loadings on a cylindrical shell could be reduced, for all practicalpurposes, to an easier-to-use set of curves given in Appendix K. This set ofsimplified curves practically eliminates the need to interpolate between variouscurves in WRC 107 to determine the factors used to calculate the stresses. Whenthe simplified curves are used, it will still be necessary to combine the internalpressure stresses and to develop a method of "bookkeeping" for the signs of thevarious stresses due to different loadings.

The sign convention used with the Mershon method is identical to that ofWRC lO7, as shown in Fig. 11.25. The figure shows that stresses may beobtained at the same locations. The relationship of the curves given in WRC and

the Mershon curves given in Appendix K is as follows:

Appendix K Figure WRC 107 Figures

I I.7 IXTERNAL TOADINGS 40I

^: -+L:VD,"T

where d, = diameter of opening in shell (in.)

D^ : rnean diameter of shell (in.)

? = nominal thickness of shell (in.)

Because the ASME Code, VI[-l, has neither an acceptance criterion nor a

rnethod to classify stresses, the designer has to establish a method that is

acceptable to the Authorized Inspector. For guidance, the method in the ASME

Cod;, VU-2, may be followed by considering the differences in stress theory

and allowable stresses between the methods in VIII-I and VIII-2 This method

permits the designer to assign stresses into such categories as primary stresses'

iecondary stres;s, and peak stresses depending upon what loadings are in-

cluded.

Example 11.15, A cylindrical shell that is 84-in. ID by 1'0-in nominal

thicknLss contains a nozzle S-in. ID by 1.0-in. nominal thickness' The design

pressure is 400 psi and the allowable stress of the material is 17.5 ksi' The nozzle

is subjected to an inward radial loading of 12,000 lb and an applied moment in

the longitudinal direction of 150,000 in.lb. What are the combined sttesses on

the lon-gitudinal axis due to these two extemal loadings using the Mershon

metfodand the curves in Appendix K? The vessel is not subjected to cyclic

loadiqg, and therefore no stress concentration factors need be considered'

Solution

1. The shell parameter is

d^ l0A = ----: _--: = r.uoyD^T V(85X1)

Using this parameter, the constants from the radial loading on the longi-

tudinal axis are:

From Fig. K.5 M'/P = 0.127

From Fig. K.6 Mo/P : 0.086

From Fig. K.8 N,I/P = 0.160

From Fig. K.8 N6T/P = 0.176

Using these constants, the stresses due to the radial loading are deter-

mined as follows:

K.1K.2K.3K.4K.5K.6K.7K.8

11-,2A3A, 4A18, 18-1,28,28-l38, 481C, 1C-l2C,zc-l3c(l),4c(1)3C(2),4C(2\

t

tor the simplified method, only one parameter is required in using the curves-the opening-shell parameter of ,\, which is determined as follows: 3.

Page 212: Process Equipment

n

OPTNINOS, NOZZTIS, AND IXTERNAI. TOADINGS

M, rrom p (bending) = 0 rr?[A18gu] : nrro o,'

M6 from p(bending) : 0 0861@5!qE] : oreo n,i

N, rrom p (membrane) = 0.160142!9E] = uzo n,i

N4 from p (membrane) : 0 1?6[%P] = zrro nri

Using the parameter in item (1), the constants from the applied longi-tudinal moment on the longitudinal axis are determined as follows:

From Fig. rc.2 u,ft= o.tto

From Fig. r.z uoft= o.tu

From Fig. K.4 N,H = 0.076

FromFig. K.4 N6H:0.260

Using these constants, the stresses due to the longitudinal moment aredetermined as follows:

M, ftom M2@ending) : o r?o l(ffi#] =,r,r* 0,,

M5from M1(bendins) : 0 r04lqx!ggg] = e:oo n,i

N, ffom M L(membrane) = o.oze f !J!9'0{ll = | lao psi

L (luxrr IN5from M1 (membrane) = o.roof$lqll : :eoo pri

Summaries of membrane stresses, bending shesses, and combinedstresses at various locations for external loadings are given in TablesI1.6. 11.7. and 11.8.

In addition to the stresses from the extemal loadings, the stresses frominternal pressue must b€ combined. These stresses may be determined

u,( = oo, 1.40

o'( = o) 0.80

I t.7 EXTERNAT TOADINOS 403

as shown in Table I I .5. However, exact values may be used if available.

For this geomefy, assume the following values were determined:

Lonsitudinal Axis

Membrane Bending Membrane Bending

+0.20 o"( = a) 0.70 -r-0.35

+o.lo o,( = a4) 0.85 -f 0.55

s =PD^ - 400 x 85' 2T 2xl = l/'wuPsl

E. The total cornbined shesses from htemal pressure and extemal loadings

are grven in Table 11.9. I

Example 11.16. For the cylindrical shell given in Example 11.15, determinethe stresses due to iniemal pressure and applied extemal loading by the methodin WRC Bulletin lO7 .

Solution

1. For the WRC method, the following shell-nozzle parameters are required:

,5B:0.875f;= 0.875 x

a2r= o.roz

R^ 42.5Y=;=i= 42's

The constants below are determined from various figures in ITRC and the

stesses determined as follows:

From Fig. 4C No/e/R^) = l.l * J244- = 2060 psi

From Fig. zc-r M6/P = 0.088 x q#"'q = 6340 psi

From Fig. 38 N6/@L/R,^B) = 4.5 x @#ftffi--= 3630 psi

M6 =or}4sx 6x 150,000 _

(MJR^p) ""'"' (42.sxo.lo3XlFFrom Fig. 1B

= 9250 psi

Page 213: Process Equipment

s"qaRall+f

8833di -i ,.i di++l

:5t516;6

+'++

\o^ \ v1 ..!

+ll

c..l | -! ol

NINI

Eonr

::c-fi:>oA.F

6

o

{,

obo

)q

-gol-

88SI \ct .d

ldui

€98a" +- v1

t$.1

+tl

F:o\+++

t.icjtl

zlaF

s

o

oJ

oo

=o'

oao

fBo

c-oo

=obo

fin

@

o-oqF

405M

Y|56oi ,.i 6+-: I

I

t':+-t-

o\ \o ar

+tl

O\\OF

l++

1 ."1 vltt.:

I

\seeE

&

6

,9oo

t.9q

oo

E

oto

ao

oFq

f

\

-9-ooF

898-..i --t I

O\FF'

REBO\:O..r --i ..ittl

s:8-i -i .ittl

e881o\\t++

t++

:H5oi ..i 'dtll

iO\Q

ttl

o.:I9EAF,.Y

tt

.9ot2oo

oo

oaaoo

-oo

=otct

9o

-o

Page 214: Process Equipment

406 oPlNlNOs, NOZUuS, ANO EXTERNAT tOAD|NOS

From Fig. t" h= 6.6 * -l?41 = l6eo psi

From Fig. tc-t + = 0.12s x ai?rq = e000 psi

FrornFig. 4B Mfu= 1.3 x 150,000(42.5),(0.103X1)

1050 psi

From Fig. 28 M,/(ML/R^O = 0.072 x 6 x 150,000(42.5X0.103X1F

= 14,800 psi

3. Using the intemal pressure stresses determined for Example 11.15 andcombining then with these stresses gives:

Pressure mernbrane

Pressure bendingP membrane

P bendingM1 membrane

M1 bendingTotals

+23,800

-3,400- 1,690

- 9,000

-3,630-9,250

-880

+23,800+ 3,400

- I,690+ 9,000

-3,630+9,250

+37,100

+ 23,800

-3,400- 1,690

-9,000+3,630+9,250

+24,880

+23,800+ 3,400

- l,690+ 9,000+3,630

-9,250+25,860

oO

BLBUA7

or

B1BUALAU

hessure membrane

Pressure bendingP membrane

P bending

Mr. membrane

M1 bending

Totals

+ 13,600

+ 1,700

-2,060-6,340- 1,050

- 14,800

- 11,240

+ 13,600

- I,700

-2,060+6,340

- 1,050

+ 14,800

+32,960

+ 13,600

+ 1,700

-2,060-6,340+ I,050

+ 14,800

+20,4ffi

+ 13,600

- 1,700

-2,060+6,340+ 1,050

- 14,800

+5,460

| 1.7 EXTIRNAI LOADINOS 407

Probhms

11.16 For the same vessel described in Example 11'15, what are the stresses on

the transverse plane when the applied moment is changed from a longi-

tudinal rnoment to a transverse moment M": 150'000 in'lb and the

radial loading remains at 12,000 lb using the method in Appendix F?

Answer: o6: Cu = -8180 Psi

Cr. = +30,460 psi

Du = +33,280 psi

Dt = -6200 Psi

4t Cu = -3550 Psi

Cr' : + 19'970 Psi

Du = +23,030 Psi

Dt = +47O Psi

11.17 What are the same results using WRC l0'l?

Answer: o4:' Cu : -7730 Psi

C. = + 31,150 Psi

Du = +34'670 Psr

Dr. = -7050 Psi

o': Ct) = -2620 Psi

Cr = + 19,240 psi

Du = +21.820 Psi

Dz: +920 psi

I1.7.2 Stresses in ihe Nozzle

The general membrane stresses in the nozzle are calculated using the basic

equaUon

.P,M,,7"_ A_ I _ J

(1 1.61)

Page 215: Process Equipment

4OO OPININOS, NOZILCS, AND EXTIRNAI I.OADINOS

Howcvcr, to utiempt to make some correction fbr local eflbcts, the bendingmoments are adjusted by a stress intensification thctor. For piping thermalexpansion flexibility stresses in both the ANSI B3l.l and ANSI 831.3 Codes,the procedure is as follows:

The sfess range, SE, is calculated by

se - t/il a aP (0r.62)

where S' : M'/22 @si)

Mr = torsional moment (in.-lb)

Z = section modulus of nozzle (in.3)

and 56, the resultant bending moment, is

itM)" + (i"M.)z (11.63)

where i1 : in-plane SIF from Table 11.10

i, = outplane SIF from Table 11.10

Mi : in-plane bending moment, (in-lb)

M, = outplane bending moment (in.Jb)

The allowable shess range 51 is

lo =/(1.255" + 0.255/,) (11.64)

where S" : allowable stress at ambient (cold) temperature (psi)

51 = allowable sfress at design temperature (psi)

/ = reduction factor from Table 11.11 based on number of cycles

The design is acceptable when S5 < 51.lrngitudinal stesses Sa due to sustained loadings, such as pressure and dead

loading, shall not exceed S7,. When 51 ) .[, the difference may be added to theterm 0.2551 in Eq. 11.57. This gives

,So :/[1.255" + 0.255, + (Sr - Sz)]

or

sA =/[1.25(s" + s) _.ir.l

which may be used in place of Eq. 11.64.

(11.6s)

I r.7 txTCRNAt LOADINGS 409

Example 11.17. A l2-in. NPS Schedule 160 branch and run pipe are attached

to oneinother. The design pressure is 2200 psi. The allowable stress at ambient

temperature is & = 17.5 ksi and at design temperature is Sl = 12'0 ksi' Inaddition to the intemal pressure, the branch is subjected to externally applied

forces and moments ftom thermal expansion of connecting piping. These mo-

ments and force are Mi = 600,000 in.-lb; M, = 900,000 in.-lbiMt = 750 '00,0

in.lb; and F*iur = 90,000 lb. The nozzle is designed for 20,000 cycles Using

the design procedure ofthe ASME-ANSI B31 I Code, what is the total applied

stress and what is the allowable stress?

Solution

1. Properties of 12-in. NPS Schedule 160 are D, : 12.75 in.; inside

ard : 80.5 in.2; metal area = 47.14in.z;z = 122.6in.3; t^ = 1'312

ln.

Flexibility {actor'for elbows i = 1.65/iFlexibilitv factor' lor miterc k = 1.52/h5t6

' Stress intensif ication

' lactor i =O.9lh2t3'Stress intensi{ication

'tactor t = O-75/h213.r || l|-Zx N

x r.\

clI I

\tf.

s EE E e q:33 33:.t oo o o oCharacteristic t

.9

t!

100

8060

40

30

20

15

108

3

2

1.5

I

1.00

0.75

0.50o.375

o.25

1 end flanged cr = i]2 ends flanged c1 =i1l3

Page 216: Process Equipment

lF.. tS I1r -1frn-T|

ili@H

rlr sIFH.a',-n

ill,\ilMlIrJ

rir. ,l-ll- | I .!

rF,lsJl{

+-l-

{.-tFr

rr.., I c+It\

rr-,.|s rr-. | {adl\t .n

(.:9o. li o. l{dlt cil\oF. o'lQct l\ ct lt

o\ t{..tF

o, lE<i l!

+

o c]

--&-E EE J{ AE €E E"*ii"Eq"E Ea gSEFe"gE

EtIigEtEEEFf

gd0

-.i ltt

.bvtrl Fr'

c

'r::

e

I

'^c i

<;Esit .E&,

t)t

tLh

r$'-Ill

4ll4r0

rI. 1f-lf't I slmsW

q

F_r|r

rFi I g*lh :l-i- 9l' r,-rsEIN +l <f(,)l *l

=r

.lll ,

rs ,:f F "-1l't I (

N

.RIGIt\ l'>

€'\ l<<i lt

o\ l{e l"t

o\ l{ol\

o. lt o. lQdl\ ctl\o. lE.ctl\qliot{

vr l;i I'q!a l;'€ls9I's

!>r

!- .:E}?3bX61!.'Eo lee STE 35F iF: € €: 9€ ^.,*eE -dsF Fi;-sY HH.t g;Ill

-

B

o

e'tE€o#E

'=llx .!s

d

9Xg.F

!.)

rt)

ooEoo

=o

Ern!o

oo

-oxoE0;-9-o

Page 217: Process Equipment

€t I2-\eltt-,,-->\tRlq+

>-:--€t e

{lrF.--:-\{ la-

+

--=-

h

F"

5B*3Eg9613hF2A

p,B'E}F

gqEE€raE.EtsE--R

E ir-a.9 -EE6 F! o.E *!€>, .z .-' i'E *E €q *; ao .-' >i.i;i E - =-t FF E .l 6t\ 5fi E 3.3d" :H H E Ht -e; fr R 6'E e; a 5 E

€ E9 d o o

"a sg.E ".9; €t s E 6t :€ Ec d: gE E\€I *HE 3.8E E$ €: Er ;€ E E e*,t..tc 3b: s F

E ; EE € 5 !

A;EI iE€I - .eE E E f

EFs€ggg4t3412

il tr Ilr€ EE;3 = 5Ei E { g

Eg E E ;€;E 7 i€r t €9c E

;: i gHE €E; r i.Ex*,+E€ E Z.E.gEE

Es E E.F*€EEE g E:.gCi .Eg.E E ssso;ac E l!";:5sb a g

Eg E 9{>r '{ 5

EE EO Edi >, a.-Jg; ET E

AE€ !E' *E*c c$F ;?EH E:E ;Fei i:€ E g

;BE iE; g i$ig E iE, $*c

igg'EiEiiiE€sE FBa ! L' ll.,l I l. $E

EE€EI Eg.3 FE.E F ?A

.i

eie 'Eq

€6fr;$H;'EE ri.EE BflgESF

>!!P.2'*6E E{OE

-E .s

E95fi

x

.9.9'x

Iat)

oEcoo

oo,Sc.9oll'6co.s

p

t,o

oo,s

5oo)al

o

.gop

Page 218: Process Equipment

1t1 ollt{lt{ol, f{ollt|t, AND rxil${ r KTAD|NO3

Tobb ll,ll Strcr-Rongr RrductlonFocl,oru ( f)

Cycles, rV Factor, /7000 and less

Over 7000 to 14,000

Over 14,000 to 22,000

Over 22,m fi 45,ONOver 45,0m b 100,000

Over 100,000

1.0

0.90.80.70.60.5

2. Data at juncture from Table 11.6:

n=4 __ 1.312 =n,r"nR, 5.719

u:H=z.qon-'-

t = o.75i" + i = o.7s(2.$) + 0.25 = 2.05

Determine torsional stess:

s,=E=ffi=*oo.t4. Determine the bending shess:

Courtgoy American Society of M€chanical En-gioeers.

2.05 x 600,000), + (2.40 x 900,000122.6

5. Determine the stess range:

3.

Sa= : 20,770 psi

s" - !*|14 = \/Ao,nTT4@ - 2t,t7o psi

6. Determine sustained longitudinal stress:

sL: ezu) nl4i: 3760 psi

NO'rltNCtATURt 4lt

7. Determine allowable stress range S,r:

/ = 0.8 for 20,000 cycles

Se = 0.8[1.25(17,500 + 12,000) - 3760] = 26,490 psi

Ss < S,{ design is acceptable.

Problpm

11.1E An 8-in. NPS Schedule 160 branch pipe is attached to a 16-in. NPS

Schedule 160 run pipe. The design pressure is 2000 psi, the allowablestress cold is S, = 17.5 ksi, and the allowable sfress at design tem-perature is 12.0 ksi. The maximum allowable torsional moment is450,000 in.-lb. The pipe is designed for 10,000 cycles. Maximumallowable bending moments are set as equal, ff rounded up to the nexteven 1(X) in.lb, what is the value of M. md Mi2

Answer: M. = Mr = 331,400 in.-lb

(

NOMENCTATURE

Individual nomenclature is used throughout Chapter 11 and usually noted close

to where used. The following gives some general nomenclature:

p, or P = intemal design prcssure or maximum allowable working pressure

(psi)

: extemally applied axial force (lb)

: extemally applied horizontal force (lb)

= extemally applied bending moment (in.-lb)

= total local stess at opening (psi)

: allowable tensile stress (psi)

: inside diameter of shell (in.)

F"

nM6

OT

s

D

Page 219: Process Equipment

,l

d

r,

T^

4 t6 OPTNINOS, NOZZtTS. AND TXTTRNAT I.OADINGS

= insidc dianrctcr ol nozzle (in.)

: inside radius of opening (in.)

= distance from center of opening to point being examined (in.)

: nominal thickness of shell (in.)

= nominal thickness of nozzle (in.)

= minimum required thickness of shell (in.)

= minimum required thickness of nozzle (in.)

REFERENCES

1. 'ASME Boiler and Pressure Vessel Code," ANSVASME BPV, American Society of Me-chanical Enginee$, New York, 1983.

2. 'ANSI/ASME Code for Pressure Piping B3l" ANSI/ASME 831, American Society ofMechanical Engineers, New York, 1980.

3. Harvey, J. F., Theory and Design of Modern Pressure Vessels, 2nd ed., Van NostlandReinhold, hinc€ton, N.J., 1974.

4, Rodabaugh, E. C., and R. C. Gwaltney, "Inside Versus Outside Reinforcing of Nozzles inSpherical Shells with Pressure Loading," Phase Report 117-7, January 1974, Battelle-Columbus Inboratory, Columbus, Ohio.

5. Rodabaugh, E. C., "Proposed Altemate Rules for Use in ASME Codes," Phase Report 117-3,August 1969, Battelle-Columbus Laboratory, Columbus, Ohio,

6, Rules and Regulations for the Classifcatior o/SiDJ, Lloyd's Register of Shipping, Irndon,l98l.

7. Sterling, F. W ,, Marine E gi eers Handbook, McCtraw-Hill, New York, 1920.

E. Porowski, J. S., W, J. O'Donnell, and J. R. Fan, "Limit Design of Perforated CylindricalShells per ASME Code," Jounal of Pressure Vessel Technology, Vol. 99, Sedes J, No. 4,November 197?.

q- Wichman, K. R., A. G. Hopper, and J. L. Mershon, "Local Stresses in Spherical andCylindrical Shells due to Extemal lradings," Welding Research Council, Bulletin No. 107,Ncw York, August 1965.

lll. Bijlaad, P. P., "Shesses from Local Loadings in Cylindrical Pressure Vessels," T/ans.I.\ME, Vol. 77. pp. 805-816. 1955.

ll. _, "Stresses ftom Radial Loads in Cylindrical Pressue Vessels," Welding .loutnal,vol. 33, Research Supplement, pp. 6l5s-623s, 1954.

14.

17.

BIBI.IOGRAPHY 417

-,

"strcsscs liorl Radial Loads aDd Lxlonl l MoDrcnls in Cylintlrical I'r'cssttrc Vcs

scls," Wtltlint: Journal, Vol. 34, Rcsearch Supplcncnt, pp 601ts-617s, 1955

-,

"Computation of the Sbesses ftom Local Loads in Sphcrical Prcssurc Vcsscls or

Pressure vessel Heads," Wewing Research Council, Bulletin No. 34, New York, March

195't.

-,

"Local Stresses irr Spherical Shells from Radial or Moment Loadings," WeklirgJoumal, Vol. 36, Research Supplement, pp. 24ls-243s, 1957.

-,

"Sresses in a Spherical vessel from Radial l,oads Acting on a Pipe," weldinS

Research Council, Bulletin No. 49, New Yo*, April 1959

-,

"Stresses in a Spherical Vessel from Extemal Moments Acting on a Pipe," ibid , pp

3t-62.

-,

"Influence of a Reinforcing Pad on the Stresses in a Spherical Vessel under Local

l-oading," ibid., pp. 63-?3.

-

, "stresses in Spherical Vessels from Local Loads Transfe.red by ^

Pipe," WeditqResearch Council, No,50, pp. 1-9, May 1959.

-

, "Additional Data on Stresses in Cylindrical Shells under Local Loading," ibid., pp.

l0-50.

BIBLIOGRAPHY

Ellyin, F., "An Experimental Study of Elasto-Plastic Response of Branch-Pipe Tee Connections

Subjected to lntemal hessure, Extemal Couples, and Combined lrading," wRC BulletinNo230, Welding Research Council, New York, September 1977.

Ellyin, F., "Elastic Stresses Near a Skewed Hole in a FIat Plate and Applications to Oblique Nozzle

Attachments in Shells," WRC 8llrrerln No. 153, Welding Research Council, New York,August 1970.

Ellyin F., "Experimental Investigation of Limit lnads of Nozzles in Cylinddcal Vessels"' wRcBulletinNo.2lg, welding Research Council, New York, September 1976

Eringen, A. C., A. K. Naghdi, S. S. Mahmood, C. C. Thiel, and T. Ariman, "Stress Concen-

trations in Two Normatly Intersecting Cylindrical Shells Subject to lntemal hessure," WRC

Bulletin No. 139, welding Research Council, New York, April 1969.

Fidler, R., "A Photoelastic Analysis of Oblique Cylinder In&fiections Subjected to IntemalPtesslure," WRC Bulletin No. 153, Welding Research Council, New York, August 1970.

Findlay, G. E. and J. spenc€, "Bending ofPipe Bends with Elliptic Cross Sections," I/Rc B!.rletin

No. 164, Welding Research Council, New York, August 1971.

Gwaltney, R. C., and J. M. Corum, "An Analytical Study of Inside and Outside Compact

Reinforcement for Radial Nozzles in Spherical Sheus," ORNL 4732, June 1974, Oak Ridge

National Laboratory, Oak Ridge, Tenn.

Page 220: Process Equipment

al! oPlNtt{ot, t{ozz[3, aNo rxTaRNAt r,oAotNos

Kruus, H., "A Rcvlcw dnd llvlluution of Computcr Program6 for thc Analysis of Strcsscs inPrcBsun Vc$scls," MtC BulletinNo. 108, Wclding Research Couocil, New York, September1965.

teveD, M. M., "Photoelastic Determination of the Sftesses at Oblique Openings in Plates andShells," WftC Bunettu No. 153, Welding Resea.ch Council, New York, August 1970.

teven, M. M., "Phoioelastic Determination of thc Shesses in Reinforced Openings in hessureVessels," WRC Bulletirr No. ll3, Welding Resea.ch Council, New York, April 1 6.

Lind, N. C., A. N. Sherboume, F. Ellyin, and J. Dainora, "Plastic Tests of Two Branch-pipeConnections," lyRC trrrerir No. 164, Welditrg Research Council, New York, August 1971.

Marwell, R. L., atrd R. W. Holland, 'collaps€ Test of a Thin-Walled Cylin&ical Pressue Vessclwith Radially Attached Nozzle," WRC Bulletin No. 230, Welding Research CouDcil, NewYort, September 1977.

Mershon, J. L. , "Intetpretive Repoit orr Obliqle Nozzle Connections in hessure Vessel Heads andShells udder Ifternal Pres$ur€ t ading," WXC Sarr?rrn No. 153, Welding Research Council,New Yort, August 1970.

Mershon J. L., "Preliminary Evaluation of PVRC Photoelastic Test Data on Reinforced Openingsin Pressur€ Vessels," WRC Bullain No. I13, Welding Research Council, New York, April1966.

Raju, P. P., '"Tbre€-Dimensional Finite Element Analysis of 45" Lateral Model | (tl/D = 0.08,D/T = lO, under External i&Plarc MomeDt lrading," TR-3984-2, Teledyne Engin€edngServices, Waltham. Mass. December 1980.

Raju, P. P,, "Three-Dimensional Finite Element Analysis of 45"I-ateral Modelz(d/D :0.5,D/f : n) under Int€rtral hessur€ and Extemal in-Plane Moment Loading," TR-3984-1,T€lcdyne Engineeriry Services, Waltham, Mass., December 1980.

Raju, P, P., "Tbree-Dimensional Finite Element Analysis of 45" Lareral Model l(d/D = 0.08,D/T = lO) under Internal Pressure and Extemal in-Plane Moment Loadings," TR-3X9-1,revis€d A, Teledyne Engineering Services, Waltham, Mass., January 1980.

Riley, W, F., "Experime al Detennination of Stress Disributioni in Thin-Walled Cylindrical andSpherical Pressure Vess€ls wilh Ciltula. Nozzles," WRC BulletinNo. 108, Welding ResearchCouncil, New York, September 1965.

Rodabaugh, E. C., "Elastic Stesses in Nozzles iD Pressue Vessels with Intemal Pressue Load-itr8," Phas€ Repoft ll7-1, April 1969, Battelle-Colubus Laboratory, Columbus, Ohio.

Rodabaugh, E. C., "Review of Service Experietrc€ atrd Test Data on q)ening$ in Pressure Vesselswith Non-I egral ReiDforcidg," WRC Bulletin No. 166, Weldiog Research Council, NewYork, October 1971.

Rodabaugh, E. C. , and R. C. Gwahiey, 'Additional Data on Elastic Stresses in Nozzles in Pre$sulEVessels with Intemal Pressure loading," Phase Report ll7-2, December 1971, Battelle-Columbus kboratory, Columbus, Ohio.

Rodabaugh, E. C,, aDd R. C. cwaltoey, "Elastic Stsesses at Reinforced Nozzles ir Spherical Shellswith Pressur€ and Moment Loadiog," Phase Report ll?-gR, September 1976, Battelle-Columbus Iaboratory, Columbus, Ohio.

Rodabaugh, E, C,, and S. E. Moore, "Evaluation of the Plastic Characte.istics of Piping hoductsin Relation to ASME Code Cdteiia," NUREC/CR-0261 ORNI-/Sub-2913/8, Oak RidgeNational Inboratory, Oak Ridge, TeIm., July 1978.

Schroeder, J., K. R. Srinivasaiah, and P, Graham, "Analysis of Test Data on Bmnch ConnectionsExpos€d to Intemal Pressure and/or Extemal Coluples," WRC Bulk,n No. 200, WeldingResearch Council. New York. Novemb€r 1974.

Schoeder, t., and P, Tugcu, "Plastic Stability of Pipes and Te€s Exposed to Extemal Couples,"WRC Bullctin No, 238, Welding Research Couucil, New York, June 1978.

BIEIIOORAPHY 4I9

SellcrB. F., "A Note on the Conelation of Photoelestic and Stcel Model Data for Nozzlc Con'

ne.tions in Cylindrical Shells," WRC Blt eri, No l39, Welding Resealch Council, Ncw

Yo!k, April 1969.

Taylor, C. E,, and N. C. Lind, "Photo€lastic Study of the Stresses neat Operdngs in hcssure

Vessels," WRC Burkr,t No. ll3, Welding Resea.ch Council, New York, April 1966'

Tso, F. K. W., J. w. Bryson, R. A weed, and S. E. Moore' "Stress Analysis of Cylindrical

Pressure Vessels with Closely Spaced Nozzles by the Fhit€ Element Melhod"'in Vol l'Stres! Analysis of vessels with Two Closely Spaced Nozzles under Intemlrl Pressure'

oRNL/NUIiEG-18/vl, November 1977, Oak Ridge National Laboratory, oak Ridge, Tenn'

l

Page 221: Process Equipment

CHAPTER 12VESSEL SUPPORTS

420

Ditfereni v$sel supporis. (Courresy of the Noofer Corporotion: St. touir, Mo.)

421

Page 222: Process Equipment

412 VISSfl" SUPPORTS

I2.I INTRODUCTION

Process equipment is normally supported by one of the following methods:

1. Skirts2. Support legs

3. Support lugs

4, Ring girders

5. Saddles

Most vertical vessels are supported by skirts, as shown in Fig. 12.Ic. Skirtsare-economical because they generally transfer the loads from the vessel by shearaction. They also hansfer the loads to the foundation through anchor bolts andbearing plates.

I*g-supported vessels are normally lightweight and the legs provide easyaccess to the bottom of the vessel. An economic design is shown in Fig. 12. lb,where the legs attach directly to the vessel and the loads are transferredby shearaction.

(a) Sklrt

I.'igure 12. lc shows an alternate design where the lcgs irLre attached to lugs that

in tum are welded to the vessel. The bending stiffness of the shell and its abilityto resist the moments adequately, must be considered. The cross-bracing ol the

legs may be needed to minimize lateral and torsional movements.

Vessels supported by ring girders, (Fig. 12.1d), are usually placed within a

structural frame. The ring girder has the advantage of supporting torsional and

bending moments resulting from the transfer of loads from the vessel wall to the

supports.Horizontal vessels, (Fig. l2.le), Ne normally supported by saddles. Stiff-

ening rings may be required if the shell is too thin to transfer the loads to the

saddles. The problem of thermal expansion must also be considered.

I2,2 SKIRT AND BASE RING DESIGN

Design of the skirt consists of first determining the dead weight of the vessel W

and bending moment M due to wind and earthquake forces (see Chapter I 6) . The

stress in the skirt is then determined from

-w(f = ^

In most practical applications, the ratio R/t ) 10. Hence, the area A and the

moment of inertia I is exPressed as

A : 2rRt

I : rR3 t

and the equation for the stress in a skirt becomes

, = #'#, 0z.z)

where o: axial stress in skirt

W = weight of vessel

M = moment due to wind or earthquake forces

R : radius of skirt

r = thickness of skirt

Because the compressive stress is larger than the tensile stress, it usually

controls the skirt design and is kept below the skirt's allowable axial com-pressive stress as given by Eq. 8.15.

I2.2 SKIRT AND BASE RING DESIGN

a;.

Mc-+-I

(r2.r)

(b) Leg (c) L!s

Gl rder (e) Saddtes

Figur€ l2.l Vessel supporrs.

(d) Rins

Page 223: Process Equipment

VESSIt SUPPORTS

Toble 12.2 Bolt Dimensions ond Cleorqnces Bolting DqtdAtlcr the thickncss of the skirt r is determined, the next step is designing the

anchor bolts. For a given number of bolts Nthe total bolt area can be expressedas NA where A is the area of one bolt. The moment of inertia of bolts about thevessel's neutral axis is I = NAR2/2.'fhtts, Eq. 12.1 is

_-w2M, N -NR

Nut Dimensions

Radial EdgeDistance Distance

RE

AcrossFlats

BoltSize

No. of RootThrcads Arca (in.'?)

Across BoltCorners Spacing

B

WrenchDiameter

a,

where P = load/bolt

17 : weight of vessel

' N = number ofbolts

R = radius of bolt chcle

M = bending moment

The maximum load/bolt is based on the allowable stress and conespondingarea given in Table 12.1. The allowable stress depends on the type of bolifumished. Table 12.2 shows various properties and required dimensions forbolts with different diameters.

Example 12.1. Determine the required skirt thickness and the number of boltsneeded in a vessel with an outside radius R = 7 .0 ft. IIJI empty weightWr : 160 kips, weight of contents Wz: l4l;} kips, wind-bending momenrM : 1500 ft-kips and temperature = 300. F. Assume A307 bolts and useFigure 8. 11 for the exiemal pressure chart.

Solution

Skirt design

Lpt t = 0.375 in. From Eq. 12.2,

Tqble 12. I

(r2.3) o.126o.202o.3020.419

0.551

o.728o.9291. 155

1.405

1.608

1.980

2.3042.6523.4234.292

5.2596.3

7 .487

8.'749

10.108

11.566

0.9691.1'7 5

1.383

1.589

t.'7962.0022.2092.4t62.622

2.8283.035

3.449

3.8624.2't54.688

5.102

5.515

5.9286.341

6.755

lil!2

L7

3*l

J;

41!

1Z

On

tt a=

'7L

lE

8"1

tiriz 7F,

L1

L'

zc

J7

4+7

+i

t)a,7

7i8

8j9

.t? r16a!!1

rt t5

zi Lz^ I ^3J-6 ZE

Ji

+i rt.ri ra

z

rr_6

rr_6

ra-

ri32

.16L1

^3-15

Ja-

Ji+i

5

oi

arJd rro1 10

;e18l* 8

li 8

1"1 8

ll 8

lt 8

li 8

1"2 8

282i82i82i8

v3i83i83i848

AllowableBolt TensileType Stress (ksi)

Cross-SectionalArea(in.')

4307

43254449A.490

20

40

40

54

tr /^ 0.9743\'t\" - -7rr-

1Nominal

NominalNominal

'l{' is number of lhrcads/in. 425

Page 224: Process Equipment

lN Vttilt luPlotTt

160 + 1l|40 1500 x 12o= -

From Eq. 8.15,

2 r (84 - 0.37 5 / 2)(0.37 5\

10.28 ksi

r(83.813f(0.375)

0.125A: RJt

= 0.001 I

Hence, from Fig. 8.11, A = 12,100 psi OK

Boh design

Let N = 12 bolts. From Eq. 12.3,

I-oad/tntr: - l@+ 2(15ooxl2)t2 12(84)

: 22.4 kips

Frorn Table 12.1,

22.4area requlre{ : ld-

= | .12 n.2

From Table 12.2 W l|.-lln. diameter bolts (N' =.S). Thus from Table 12.1,

n." ^-- 0.9743."*u=Z1r.sD-1-)-: 1.23 nz > 1.12 OK

7)Aactual shess = J1: : 18.2 ksi

l-25

total furnished area = 12 x 1.23 : 14.8 in.'?

Use l-in. skirt with 12 - l*-in. dianeter bolts. IHaving established the nurnber and size of bolts, the next step is to calculate

thc interaction between the base plate, anchor bolts, and supporting snuchre. Ifthc supporting structure is a steel ftame or foundation, then Eq. 12.3 is all thatis necded for designing anchor bolts. On the other hand, if the foundation is deep

r2,2 tKlnT aND lA$ RINO DIIION all

and/or r,esting on a group of piles, it can be assumed that fte intersction bctwccn

ttt Uots, bie plaie, *d c-on"ret" is similar to that of a reinforced concrotc

U"".. fn t"feoit g to Fig. 12.2, the following assumptions are made:

1. The contribution of the bolts on the compression side is negligible'

2. The bolts on the tension side are assumed to act as a continuous ring of

width r", where r" is calculated from the equation

,,=4zrd

3. The allowable stress of steel /" is taken from Table l2'1'

(t2.4)

tigl!.o 12,2

Page 225: Process Equipment

lrt v||||t turro$t

Tobb 12.3 Concntr Proprrflcr

CompressiveStess (psi)

AllowableCompressiveStress (psi)

Modulusof Flasticity Gsi)

25m3000

3500,1000

f" = o.4sfl1,t251,350

1,575

1,800

E.: 57,WO\/n2,850,000

3,120,000

3,370,000

3,610,000

Ei /8"ltt09

8

"E, = 30 x lf psi.

Concrete on the compression side is assumed to have a width t" that is thesame as the width of the base plate.The allowable complessive stress of concretel is taken from Table 12.3.The ratio of the modulus of elasticity of steel to that of concrete is definedas n.

=f'/e, -f"e"f" e" f"a"

In an elastic analysis, the stains in the concrete and steel at any location are thesame. Hence, e" : e, and

':ti - ,=*Also, from Frg. t2.2c, using similar triangles

4.

6.

.E"n: Ec

From theseobtained:

f, nf.d-kd kd

,1x = 1] 1Jnf" lJ2's)

assumptions afr Fig, 12.2, the following relationships are

I2.2 SKIRT AND IA3: RINO DTSION

1=,t" =W=t-2kThe total force T of the tensile area of the reinforcement can be determined bvsumrning forces on the tensile side of the neuhal axis which gives

/,r\( t ll.,r. \ 'llr = f,t,l;l {r--= | [; * yl sin 7 + cos 7l I\z/ tr -1- sln 7 L\z / J)

o|

, =r,^(1) *,

The disance between I and the neutral axis expressed by 12 is

t"=4l<r/z+nt't+t.st*t" n+o f'' 2L (r/2 * 7) sinT * cosT J

429

(12.6)

(r2.7)

(r2.8)

(12.e)

Similarly, the total force C of the compressive area of the concrete is given by

b=<,,*-{;lls::=;v]

c=(t,+*"r\h*The distance /3 between C and the neuhal axis is

, _ dl(n/2 -z)(sin'zy + l/21 - 1.S(sinycosy)'l

"-216]The relationship between extemal forces M and I7 and the intemal forces I andC are derived from Fig. 12.2c. He,nce

2M"=O

M - w(h + h) - r(h + 4) = 0

Page 226: Process Equipment

alo v|lilt lutFom

0nd

Similarly,

and

^ M-W(\+l)t = 1ra 1,(12. r0)

)r',=o

C:T+W (12. r 1)

The values of 7, h, h, h, Ks and K2 are given in Table 12.4 for various valuesof /c.

Tqble 12.4

2h/d 2t"/d 2h/d Kr Kz

0.01

0.02

0.03

0.040.05

0.06

0.08

0.10

0.15

0.20

o.25

0.300.35

0.400.45

0.500.55

[email protected]

0.70o.75

0.80

0.85

78.52

73.74

70.05

66.93

@.166t.&57.t453.13

44.43

36.87

30.00

23.58

r7.4611.54

5.74

0.00

-5.74-11.54-17.46-23.5E-30.00-36.8'l-44.43

0.980.96o.940.920.900.88

0.840.800.700.600.500.400.30o.200.100.00

-0.10-0.20-0.30-0.,m-0.50-0.60-0.70

1.489

1.477

1.465

1.452

r.4391.426

1.400

1.373

1.3041.233

1.161

1.087

1.013

0.938

0.8620.785

0.709

0.631

0.553

0.475

0.397

0.318

o.239

0.0160,o320.048

0.064

0.080

0.096

o.1280.160

o.2390.318

0.397

o.4750.553

0.631

o.7090.785

0.862

0.938

1.013

1.087

1.161

t.2331.304

3.1 13

3.085

3.059

3.033

3.008

2.9832.9352.887

2.772

2.612.5512.442

2.3332.2U2.1t32.000

1.884

t.7651.ffi1.509

|.3'to1.218

1.049

o.267

0.378

0.4630.535

0.599

0.657

0.160

0.852

1.049

1.218

r.3701.509

1.640

r.7651.884

2.000

2.1132.2U2.3332.4422.5512.6612.772

12,2 SKIRT AND lASl RINO DlllON .ltl

Example 12,2, ln Example 12.1, it was found that l2-lN in. A307 anchorbolts were needed for a vessel with an outside radius R = 7 ft,Wt = 160 kips,M = 1500 ft-kips, and a skht thickness of0.375 in. If/l = 3000 psi, determinethe actual stess in the concrete and bolts.

Sohiion. By referring to Fig. 12.3 and Table 12.2, for le-:ff' bolts, the boltcircle can be calculated as

d = 2(84 + 0.25 + 1.875) = 172.25 in.

Also

,t":2(0.25 +

Frorn Example 12.1,

From Eq. 12.2

1.875 + 1.375) + 0.375 = 7.375 n.

"f, = 18.2 ksi

r2(r.23\,=-'" t(172.25)

= 0.0273 in.

Figirr. 12.3

Page 227: Process Equipment

1t2 Vililt tuttottl

From Tablo 12,3

"f' = 1350 Psi

n=10

and Eq. 12.5 gives K = 0.43.From Table 12.4 wirh K = 0.47 ,

1= o'.,*a

1= o.ssza

1 = o.srra

&: 2.157

& = 1.836

The magnitude of I is obtained ftom Eq. 12.10 as

- _ 1,500,000 x 12 - 160,000 (0.1{ + 0.678) (172.25)- (0.892 + 0.678)(r72.2s)

: 49,750lb

The value ofi is determined ftom Eq. 12.7 as

From Eq. 12.1I

Equation 12.9 gives

49,750(0.027 3)(r7 2.2s / 2) (2. 1 s7),

: 9810 psi

C = 49,750 + 160,000

:2O9,750lb

2@,750f": lo.on3 + (10x7.37st (t72.2s/2) (r.836)

= 18 psi

I2.2 SKIRT AND 8A3I RINO DI3ION

The calculatcd values of/,1 andf, result in a K value of

K=

433

r + 9810/(10xr8): O.O2

which is considerably lower than the assumed value ofl( = 0.43. Hence anothertrial is needed with a K value of 0.02. After recalculating values of 7, /", C, and/", a new value ofK is obtained and compared with the assumed one. ff bothvalues are approximately the same, the analysis is completed. If they axe not, anew analysis is performed. Thus, in this example after a few trials, forK = 0.O75, the following values were obtained:

:1 = 0.8s(t

',L--:1.$7

4 = o.rnd

K(:2.e47K) = 0.734

. T. _ t5 x ld x t2 - 16 x lff (0.85 + 0.120) (172.25)tr -

:35.230

35,230(o.027 3)(t7 2.2s / 2) Q.e 47 )

: 5085 psi

C = t95,230

f"=42psi

and

K: r+(5085/10+42): 0.076

which is apptoximately the same as the assumed value. Hence;[ = 5085 psi andI" = 42 psi is the answer. I

Page 228: Process Equipment

atrt vlSlll tUPPOltl

12,2,I Anchor Cholr Dcrlgn

The base ring is designed both for the effect of the concrete-bearing load on theside of the foundation under compression and for the bblt force on the other sideof the foundation in tension. On the compressive side, the base ring can bcassumed as a cantilever beam subjected tol as shown in Fig. 12.4. The requiredthickness is obtained from

6lj4C= __V t t:

Substituting for M the value

M = r!-

the expression for t becomes

(r2.r2)

wherc t : required base ring thickness on the compressive side of the neufalaxis

/" : actud sftess in concete

I : cantilever length of base ring as defined in Fig. 12.5

o : allowable bending stess of base ring

On the tensile side, the thickness of the base ring is conholled by the amount ofbolt force and dimensions shown in Fig. 12.5. The exact analysis for deter-

__r'

l6It4\/;

tw\/;

Fi$,r. | 2.a

,4r.tll',t!tf!,t;;

r2,2 SKtRt AND lA3! R|NO Dll|ON 4$

---1_r",,DEFLECIION

(,Fisuru 12.5

rnining the maximum bending moment in the base ring is rather complicatedbecause of the nature of the boundary conditions and the hole. However, anapproximate and conservative solution can be obtained by assuming the ring toact as a plate simply supported on three sides and free on the fourth side. Usingthe yield-line theory,l

r]--lls-llrl

PARTIAL VIEWOF

BASE RING

(") (b)

external work = intemal work

F(t) = 21,1016 - dr h + u, (a - fi j

or

Mp=2[2n /a + a /2t - d(2/a + r/21)']

Using. a load factor of 1.7 and a factor of l.l5 to allow for fleld-line comereffect,r the equation

^4M't'

Page 229: Process Equipment

lta w||tt tuDotTl

can bo solvod for tho rcqutrcd thickncss cxpressed as

( 12.13)

where t = required base ring thickness on the tensile side of the neuhal axisF : bolt load

S, : yield shess of base ring

ul a, b, d, and I re as defined in Fig. 12.5b.The load in the shell is tansferred tothe anchor bolts through the gussets. An

approximate free-body diagram of the forces is shown in FIg. lZ.O. Venicattorces are transferred as shown in Fig. l2-6a. The resulting unbalanced bending-^_1T:,1i T the gussets resulting from the vertical forcei requires equal andopposrte horizontal forces as shown in Fig. 12.6b. These horizontal forcesinduco local sfiesses in the shell that are calculated from the equation

G)vqlrcaL_EaSaEs

(!)HoRtzoNTaL FoRcEs

l.5Fb(f = -:-ntzh

(12.r4)

u.c)(b4)'' zzh

S,l2b /a + a /2t - d 12'/a + t/zq'l

Figur. 12.6Figw.12.7

I2.2 SKIRT AND !A3! RINO DISION

whcrc o - allowable sness in shell

, = thickness of shell

F = bolt load

Example 12.3. Design the base ring shown in Fig. 12.7a. Stress in the boltsis 17,500 psi; height of gussets 12 in., and concrete-bearing stress is 100 psi,Allowable stress for base ring is 20,000 psi and yield sfress is 36,000 psi.

Solution. Required base ring thickness due to concrele-bearing stress is ob-tained from F4. 12.12 as

x100x6220,000

0.73 in.

From Table 12.2, tln net area of I l-in. bolts is 1.405 in.'?

. force F in bolts = 17,500 x 1.405

= 24,6M lb

(l2) t.l BOLTS

Page 230: Process Equipment

From thls trblc, cloarancc for wrcnch diametcr is 3.75 in. Allowing for gussetflllct wclds, the distance between gussets is as shown in Fig. 12.7i. froi fq.12.13.

ile- designq I tlis point has a choice to make. One can either use a base ringthickness of 1.07 in., which is controlled by bolt load, or use a base rin!thickness of 0.73 in. with anchor chairs, as shown n Fig. 12.7.

The stess in the shell is obtained from Eq. 12.14 as

1.5x24.600x6"- = -1t x oigt n

: 10,4O0 psi

This sbess is combined with the axial stress and the total must be less than thre€tirnes the allowable stess. I

all vltllr SuPFol?t

I2,3 DESIGN OF SUPPORT IEGS

Support legs are designed to take into consideration axial loads, bendins mo_ments, and shear forces in tlre vessel. Refering so Fig. 12.g we see that at-crosssection A-A all forces are expressed in terms of M, V, and W. The axial forceW.is canie.d uniformly by all columns. Bending moment M is carried by thecolumns away from the neutral axis and the shearing forces v are carried by thecolumns closest to the neutral axis as shown in Fie. 12.g.

Column A in Fig. 12.8 is designed by using Eql I2.3 given by

P =-w * 2tu1

n{ -NR

where P: load per column

W = weight of vessel

iV : number of columns

R = radius of columns' circle

M = noment due to wind or earthquake loads

I t 91 x z4-roo --

v

t2.3 D!3|ON ol luPPoR? t!o! 4tg " ":''''

--+--/F lort-i-7\i-_/

qJtcrta,r

'4-,4

Column B in Fig. 12.8 is designed to carry shear in accordance with the equation

T =VQ-IlrI

The shearihg force f at the top of columns B causes bending mornent in the

column if no cross-bracing is used. With cross-bracing the force T is resolved

irito axial forces as shown in Example 12.4.

Example 12.4. Determine the forces in columns A and B of the vessel shown

in Fig. 12.9.

Sohtlion. Axial force in colurnns A and B due to W is

w 240

N8Axial force in column A due to M is

[Iil-[f[ff]w

ruro,\7V ,,,u,"'r.,

F= :30

_ 2t4.NR

2x20p,0

Page 231: Process Equipment

--"--*-"-ry*"trffiffitrufft

/= 50kM-2aaa8Fr

X= /2.5

(b)

(d)

("):igur. 12.9

total axial load in column A = -50 - 100 = -150 kiptotal axial load in column B = -50 kip

The shearing stnesses transferred to column A are zero. Those transferred tocolumn B are detennined frorn

u=Wh

The moment of inertia I of the whole cross section in Fig. 12.9c is given by

t2.3 DIS|ON Ot SUPPOnT uog

rr3t. I'he quantity p of the crosshatched area in this figure is givcn by

a= wo(?,\\1t /

= 2:r2t

The force Il is then given by

. H- V (2r2t) - v

-2V" (in3t)(zt) nrt A

txSflH :;6 = 0.2653 lb/in.

Horizontal force in column B is

a = (o.z6sr)(:3y /: 12.50 kips

This force Il is normally resolved into two components as shown in Fig. 12.9d'Force U is a r{dial force on the shell and force X is a horizontal force in the plane

of the cross-b\acing.

. u = Hcnt a= 12.5 x 0.414 = 5.18 kips

y = !- = !-L = 13.53 kips'^ sin a 0.924

The force X intoduces additional cornpressive force in column B as shown inFig. 12.9e. The distance between columns is

t=2{ =3.en

The apFoximate height of the colurnns is 20 ft. Hence, angle B is about lldeer€€s and the axial force F in colurnn B is

F : #n:6e.61 kips

force E = "n BA

= 7O.lt fip.

4l

Page 232: Process Equipment

I2,5 RING GIRDTRSvtss suPPokrs

total lirrcc in colunrr A : --l5() kip

total forcc in column B : -50 - 69.61 : 119.61 kio

total force in bracing : 70.91 kips I

If the cross-bracing is eliminated in Example 12.4, the shear force tends tocause a bending moment in column B. Assuming the bottom end of the columnspinned, the horizontal force causes a bending moment at the top of the columnof magnitude 12.5 x 20 ft : 250 k-ft. Thus, without a bracing system, columnB must be designed to withstand a compressive force of 50 kips plus a bendingmoment of 250 k-ft rather than a compressive force of 119.61 kips with a bracingsystem.

Note that the absence of a cross-bracing causes the tops of the columns tosway laterally because of reduced rigidity. This can also cause excessive vi-bration or deformation of the vessel.

I2.4 LUG-SUPPORTED VESSETS

The main design consideration regarding lug-supported vessels is the stressmagnitude in the shell. Bijlaard's method is usually followed in such a design.2It consists of determining the stress in the shell at the vicinity of a support lugof height 2C2 and width 2C1, as shown in Fig. 12.10. The bending moment in

\__

)r-l 1,.,t4 t

lhc shgll duc t() support cccentricity is givcn by

M": Fe ( r2. r5)

and the maximum stress in the shell is calculated from reference 2. Both mem-brane and bending stresses are calculated. Details ofthe required calculations are

well established in reference 2. Further treatment of this topic is unnecessary inthis book.

I2.5 RING GIRDERS

Ring girders (Fig. lz.ld), are common in elevated vessels supported by a

structural frame. An exact analysis of the stresses in a ring girder due to variousloading conditions is very complicated. For a uniform load, the stresses andforces can be determined easily with the following assumptions:

l. Supports are equally spaced.

2. Vertical deflection at supports is zero.

3. Slope of ring girder at supports is zero due to symmetry of loads andsupports.

4. Torsion force at supports is zero. This assumes twisting of the girder dueto flexibility of shell.

Based on these assumptions, t}le moments, shears, and torsion at the supportsand in-between supports are given by

M, = Kzwr2

V, : Ka,wr

r, =0

M^ : Kswrz

v^:oT^:o

(12.16)

where M,, V,, T" = support moment, shear, and torsion, respectively. Positive direction is shown in Fig. 12.11.

M,, V^, T^ = midspan moment, shear and torsion, respectively

K3 = (t = constants obtained from Table 12.5

w : uniform load

r : radius

The maximum torsional moment occurs at the ansles shown in Table I 2 . 5 andis given byFisur€ 12.10

Page 233: Process Equipment

Ifl' Viiiliti,hom

T*" : Kewr2 (r2.r7)

The moment, shear, and torsion expressions for any given location betweensupports are obtained ftom

Me : V,r sin d * M,cos 0 - wr2 (l - cos 01

Ve = V" - wrg (l2.l8)To = V,r(l - cos d) + M" s:rr,e -wr.z (e - sn 0)

whete M6, V6, 76 : mornent shear, and torsion at any location

0 = angle as define.d in Fig. 12.11

Tqble 12.5 Ring Gider Coefficienrs

AngleNumber Between

of SupportsSuppons (degrees) K3 Ka KaKs

Angle ofMaximum

Torsionftom

Support(degrees)

2

J

5

6

8

t0l2l620

180

120

90

72

60

45

36

30

22.5

18

-1.0000 1.5707

-0.3954 1.0471

-0.2146 0.7853

-0.t351 0.6283

-0.0931 0.5235

-0.0519 0.3926

-0.0331 0.3141

-o.o229 0.261'l

-0.0128 0.1963

-0.0082 0.1570

-3.307 x

-8.278 x-3.313 x-1.654 x-9.471 x-3.9q x-2.W x- 1.154 x-3.722 x-2.469 ><

l0-r 39.5510-, 25.80

lo-2 D.2110-2 15.30

l0-3 12.74

10-3 9.53l0-! 7.6210-3 634l0-3 4.72l0-" 3.79

-0.57m-o.2091-0.1107-0.0690-o.M7l-0.0262-0.0166-0.0115-0.@65-0.0042

Figuro l2.l I

f 2,t milo ottDltt 4t

_ In deriving Eqs. 12.16 it is assumed that thc loade and thc rcactions rctthrough the neutal axis ofthe girder. In pressure vessels the loads are tansfcrre.dto the ring girder through the shell. If the ring girder is taken as a channel sectionas in Fig, l2.l3a, tben the loads in the sh-ell cause a bending moment in thegirder because they are not applied through the shear (flexural) center. Thismoment, shown in Frg. l2.l2a, has the magnitude

m=-we

where e is the shear c€nter moment arm, which can be expressed as

b2d2he= 41,

The uniform bending moment m causes tension hoop sbess above the r_axisand compression hoop stress below the.x-axis as shown in Fig. l2.l2b. T\e

\ 'r Tr-'l--zt{-

(b)

Figw. 12,l2

Page 234: Process Equipment

"--*tr*"wffruruilr-momont and corrorponding strcso can be cxproosod ac

(12.19)

where o- = sftess

D = width of flange

d = distance between flanses

ft = flange thickness

I, = rnoment of inertia of girder

r : radius of vessel

r = shell thickness

w = unifonn applied load

. At the supports, the reaction eccentricity tends to produce compressive forcesin the top flange and tensile forces in the bottom one as shown in Fig.. 12.13c.The.top and bottom flanges can be assumed to fansfer the loads as shJwn in Fig,12.13b. TIla forces are derived as

,, -v,rb2d2hM=-mr= 4L

mrya: L

M,:+ ("o,a"otf - 'rr - 3) - t. t .t

.. -H.. (a * i),,= z ---. i-t-z

wb2d2hry

4I?

- roo, (t-i.,)n,=Z---;-ttt

(t2.20)

12.5 RINO OtRDlRt Uf

/.tsev-rr * rt

(bl

At the supports, 0 = 0 and

(c)

Figurc 12.13

M,=+(*,;-i)-Hatt = Zco.a

v,:-H'2and in-between the supports 0 = a/2

f coonrl . "-;\sm;Mr=

?4

Page 235: Process Equipment

H W$tt tupPotll

_ .f,| cos ar, = 7_.ismt

v,: +!:!sa .at-z

The positive directions of M1, F1, and % are shown in Fig. 12. l3c.

Exanp!9 12.5. The ring girder shown in Fig. 12.t4 is supporred at eightpoints. If I7 = 200 kips, find the forces in the ring at the supports and at thepoint of maximum torsional moment.

lxx = 587.4Inl

Flgure 12.14

Solutlon

from Table 12.5, with N = 8,

''''tit'lttlf 2,6 SADDU tUPPOmt 49

= 0.637 k-in.

Kc = 0.3926

K6==3.940x10-3

200wfia (zXl00)

& = -0.0519Ks : -0.02.52

Maximum torsion occurs at 9.53' ftom support.

The forces given by Eqs. 12.16, 12.19, afi 12.?I are detemrined in Table12.6 and illustrated in Fig. 12.15 at the supports and at the point of maximumtorsion.

I2.6 SADDTE SUPPORTS

Horizontal vessels supported by two saddles (Fig; 12. le) act as simply supportedbeams. For vesSels with dished heads (Fig. 12.16a) the equivalent beam lenglhis taken as .L -l 4H 13 where L is the tangent-to-tangent length of the vessel and

.br (,At Support At Point of Maximum Torsion

Eq. 12.16

M", M^v", v^L,T^

Eq. 12.19

MEq. 12.2V

MfFr

u" Ihese equatioas apply at poifis a and D; poirts A and C have opposite signs.

'-. Wk+e'\

_ 200 1.89 + 4812

= 12.'26'

a==z:45o6'

-82.65 k-in.12.50 k

0

-60.05 k-in.

+40.54 k-in.14.80 k-6.13 k

0 k-in.7.20k

6.n k-ln.

-60.05 k-in.

-101.50 k-in.13.58 k-8.50 k

Page 236: Process Equipment

M=60.05 K-in

Fo.f.! or Support. Fotce. tt point ot l rrinr,n

Figur. 12.15

L/,TEI'(.

F=r.w

Fisur. 12.16

450

4tlt2.6 SADD!! SUPPORTI

Il is the depth of the heads. The vertical load on each head is given byV = 2IIw 13 and is assumed to act at the center of gravity of the head. Thchorizontal pfessure on the heads due to liquid heads is resist€d by a horizontalforce F acting as shown n Fig. L2.l6b.It is interesting to note that for hemi-spherical heads where 11 is equal to r, the bending moment at the head{o-shelljunction due to force F and vertical force V is zero. The bending moFent at anypoint in the vessel is obtained from statics as shown nFig. n/f6 lL b

The section modulus of the shell between the saddles is I/c and is expressedas rr2t. At the saddles, the effective section modulus is reduced due to thedqfonnation of the shell which renders the full cross section less effective.Research has shown3 that the length of the effective cross section of the shell isequal to the arc length of the contact angle of the saddle plus one-sixth of theunstiffened shell, as shown in Fig. 12.17. The section modulus of the arc lengththat is in t€nsion is expressed as

Thus the maximum longitudinal stress values can be expressed as

Z: r2t+

[4

01 ,= C1M6 for midspan between supports

o1\ C2M, for unstiffened shells at saddles

or: CrM" for stiffened shells at saddles

(r2.22'

tigur. 12.17

Page 237: Process Equipment

112 Vllln tuPForTl

whorc or - longltudinal bcnding shoss in shell (ksi)

I7 = weight of vessel plus its contents (kips)

t = length of vessel between tangent lines (in.)

r : radius of vessel (in.)

t = thickness of shell (in.)

c,: J-' ,ft't

^-ll sinA/A - cosA I"-r4LA+;inE;I-2Giltlfu)l

at=o+EThe shear sress in tlre shell between the saddles is computed by assuming a

sinusoidal distribution of the shear forces where the maximum value is at iheequator, given by

o' = I 'io 'nn

where @ is measured as shown in Fig. 12.18.

(12.23)

Flgurc 12,18

t2.6 SADDI tUPPOtTt

The shearing stress at the saddle area is influenced by the deformation of thcunstiffened shell above the saddle. Experimental research has shown that theshear near the saddle is distributed along an arc length of

t=2,(!+9\" \z 20)

as shown in Fig. 12.18. The shearing stress can then be calculaied as

4t0

wher€

a, = CtV (12.24)

^ sin dCr : -;- for saddles away from headsn\n-d+srnccos)

- sin 6 / c - sinacosa ) for saddles near headsflI \n- (l + Smdcosc/

where r : radius of vessel

a: 0/2 + F/20

d = ang(e as rneasured in Fig. 12.18\

h : ngle that varies between z - a and r

. o-" = shear sftess

Equation l2.Z is also used to check.the stess in the head. In this case thevalue of t in the expression for C3 is taken as the thickness of head rather thanshell.

The circumferential stress in lhe shell at the saddle area is calculated byassuming the shell above the saddle 0o act as a fixed arch subjected to shearings&ess as illustated in Fig. 12.19. Using the theory of indeterminate stuctures,the moment at any point along the arch can be expressed as

wrf - s IMa = * | cos {(sin'zB - iFsin2F +

79'z cos2 F)anLa L

/1 | \+ dsind(iB'z +

osnzB - sin,9)

I+ jFcosPQF + sin2p)

. lr | | \1-sinp [;B + ; sin 2B + ; gcoszll

I\4 o + ll

Page 238: Process Equipment

#a v||l|taultom

"r 3.#Pi

Fi$rc 12.19

where

llCc=s111.2|-:^P'-=sn2!.'24

The maxirnum value of M6 given by this equation occus at 0: B. Hencethe maximum circumferential bending moment in the shell can be expressed asa

"r= H*, (r2.25)

0.5<:<1.0

w2

where C5 is plotted in Fig. 12.20.

, /, Experimental work has shown that the wjdth of the shell that is effective in, / j/resisting the moment in F4, 12.25 can be taken as four times the radius or" one-half the length of the shell, whichever is smaller.

It has also been showna that Eq. 12.25 is valid whenA/r is eqgg!-Io lf€reaterthan 1.0. For A/r values of 0.5 or less, it is suggEGTll[llvalG-i@1ereduced l tfre neaA. nor in-between values of A/r, a reduction factor (Rf)

* = (;i -',can be used.

V.\

-Ut

\

12.6 SADDtl SUPPOffg .ltt

160

oo6 140o

s1s120

t@

o.ol o.o2 0.o3 0.o4 0.(E 0.06 0.o7 0.G o.os o.t o.2

Cs ond C6

tigw.12,20 Volucr of C5 ond C6 or o tunction oI the loddlo onsl! 0. (R.f. 4, p. 212)

The maximum circumferential force P at the hom of the saddle is determinedfrom

,'= (v)", (12.26)

o

- l|rnA + llcosFQP+ sin2B - ssinp + B cosB)]

where C6 is given by

..= + l*+ifu - "',8] . #*F (cs - c,)

and

t, : frf,r,u(t - | "o,n * ) o"ne - le,)

A plot of the Quantrtt C6 is shown in fi9. 12.20.When the stess in the shell as calculated from Eq. (12.25) nd 92.?,6) is

excessive, stiffening rings are used at the vicinity of the saddles to carry thebending moment.

Page 239: Process Equipment

.t!6 v|llll luttotTl

NOMENCTATUR,E

C = compressive force on concreie foundation

F = bolt load

"f" = allowable compressive stress of concrete

f, : allowable lensile stress of steel bolts

* = constant given by Eq. 12.5

Kr Kz = constants given in Table 12.4

K3 - (u = constants given in Table 12.5

/ = length

h - h = lengths as specified by Fig. 12.2

M = bending moment

Ma : bending moment in a ring girder

N = number of bolts

n: f,/f.R = radius

f : bnsile force on foundation

To = torsion moment in a ring girder

, = thickness

t" : equivalent thickness of anchor bolts

V = shearing force

Ve : shearing force in a ring girder

W : weight

o : shess

REFER,ENCES

Wood, R, H, , Pla.rric aal Elattic Design of Slabs 4nd Prater, Ronald hEss, New York, 196l .

Wichman, K. R. , A. G, Hopper, ad J. L. Mershon, "Local Stiesses ir Spheric€l a|ld Cylin-&ical Shels due to ErteErl lradings," BAC Barr"ri, 107, Welding Res€arch Council, NewYorL. 1965.

Zic}' L. P., "St€ss€s it Large Horizortal Cylitrdrical Pressur€ Vers€ls otr T\a,o SaddleSuppons" in Prr$rr" Vesscl dnd Piphb DesigL, Collected Pqert 1m7-1959, lJreicatSociety of Mechanical Elgircers, New York, 1960.

l.t

illuooRAPHY 1r'

{, Browncll, L. 8., ald E, H, Young, Procr$ Equlpmcnt Datlgn, John Wiloy, Now York,1959.

BIBTIOGRAPHY

Ro8rk, R, J., aodw. C.Yot g, Formulasfor S''ast and Stain,sthed., Mccmw Hill, New York,t915.

Uteful ltdomation ol the Design of Plate Structwes, Steel Plate EnE Bering Data, Vol.2,American lron ad Steel Institute, New York.

Page 240: Process Equipment

PART 4THEORY AND DESIGN

OF SPECIAL EQUIPMENT

459

Page 241: Process Equipment

''"' 'rii tir

CHAPTER I 3FLAT BOTTOM TANKSa

T't

.!E

I5z,l

'b

!

*pg

o

461

Page 242: Process Equipment

462 fl.At toTIoM TANKS

I3.I INTRODUCTION

Flat bottom tanks are normally constructed according to one of the followingfour standards:

1. API 650. Welded steel tanks for oil storage.2, API 620. Recommended rules for design and construction of large,

welded, low-pressure storage tanks.3. ANSI 896.1. American National Standard for welded alumrnum_alloy

storage tanks.4, AWWA D 100. Standard for welded steel elevated tanls, standpipes,

and reservoirs for water storage.

Table 13.1 shows a general comparison between the requirements of the variousstandards. The values in the table serve as a general comparison; however,specific requirements and limitations are obtaiied from the standards them_selves.

I3.2 API 650 TANKS

The requkements of API 6501 are for flat bottom tanks containing liquids withlitde or no surface pressure. The design criteria are based on simpti"fied equationswith a minimum amount of analysis.

| 3.2. I Roof Design

Flat bottom tanks with large diameter and fixed roof normally are designed withcolumn-supported roofs. As the diameter gets smaller, seif_supporting roofsbecome more economical. Dome and cone ioofs -" th" -ort popolar iypes.

^ The following equation for designing self-supporting do-" .ooi. is obtained

from Eq. 9.2b, which is based on a fairor ot saiety (FS) four:

^ 0.0625 EP=-' (n111' (13.1)

The required thickness is obtained by assuming that the maximum pressureconsists ofa live load of 25 psf, which is the assumed maximum snow load, anda dead load of a maximum roof thickness of 0.5 in. as allowed by ApI. Hence

P : 25 psf live load + 20.4 psf dead load

= 0.315 psi

7F llr.rF.=

< ld..l

F*

oZ zzz

z @

< | 42F- - o.l

-i -i

XXX

cl clxxx

a.l\o 9e

'6bEqa- 9-:.: txz

.- q. q.*9.9--t tz

.- Irr ,-

J t-z

zz zzz

\o

E< < txd

*.E5?)XF-<zx-..;

(,)

.+

aa

XXX

XXX

a

^ s E3\ E 8.9E e 8-:EFsEEtrEEtsFEE

Ve,= .9>€

E€.9*EE^EEHv 5t

r.)oo

5 e*ff

E

6

'6

?

:.9ed bERE.E e .<}!'EUF frR g9:-?,6 EE ;290F.E A.{l'H€ ^" 3H.c ; ::

Fe{ifea€EitEErEb::eE r F3::igsEEctg| , , t g s.2

?sEFEfE4 aa6es trtrtrE

F

oao

o

o

(tE(t

cod,

E'o0

an

loo

o-ooF

Page 243: Process Equipment

a6.l ttAt lOnOiit IANK!

tptting f - 29 X lOi psi, expressing R in fcet, and r in inches, Eq. 13.l is

R' 200 (13.2)

(13.3)

which gives the required thickness of a dome roof.

- The roof+o-shell junction has a stiffening ring to provide for the discontinuityforces shown in Fig. 13.1. Force 1l is

"*pr".rJa u,

11 = Ndcos d

PRzcos0

and the required area needed to resist this tensile force is given by

^ _ H(D /2)(13.4)

Fis',.o 13.l

I3.2 API 650 TANKS

/Pncos0\/a\= | -------:- || ^ |\ z / \zo/DR

= 4t/(P "."

o)

API 650 assumes a maxirnum value of o for head-to-shell rings of 15,000 psi.

The value of P can be taken as 0.315 psi. The maximurn value of cos 0 for Ris 0.8D and is equal to 0.909. Expressing R andD in feet andA in square inches,the required area is

.DR^: ux

API uses the equation

DR'- 1500(13.s)

for the required area at dome-to-shell junction.The required thickness of self-supporting conical roofs is based on Eq. 9.19

and is

P" - 2.61(t sin 0/D)25E FS(L /2D)

10..14 /r sin 0\x5= FS(,* g)\ D /

Substituting t = 29 x 106 psi and P" : 0.315 psi in this equation and express-ing D in feet and t in inches results in

. D lcs(tan 0)lo4

'= u" g zza,sq( 13.6)

Figure 13.2 shows a plot of this equation for various factors of safety. A moresimplified equation used by API is

,: -J (13.7)400 sin 0

where 1 : pquired thickness of cone roof (in.)

D : diameter of tank (f0

0 = angle between cone and horizontal base (degrees)

Page 244: Process Equipment

rt,2 Alt $0 rAHKI

A= -3: .2645 sin 0

API uses the simplified expression

D2

Using g: 1.5,000 p€i p = 0.315 psi, and expressing D in feet and.4 inequare inches, the rcquired area is

3000 sin 0(13.9)

for the required area at the cone-to-shell junction where

A = rcquired area (in.2)

D = diameter of tank (ft)

0 : angle between cone surface and horizontal base (degrees)

For tanks with small intemal pressures, the maximum pressure is limited to that

which does not cause the uplift of the tan} in the ernpty condition. Hence ftomFig. 13.3 the upward force due to pressure is equal to the downward forceresulting from weight of shell plus roof:

Pt?2=w.(q)(')4 r. -.2r. /

tlg0re 13.3

%

Flgure | 3.2

_ The required area at the cone roof-to-shell junction is obtained from Eq. 13.4.In this caee, H for a deed load condition is liven Oy

n= PD4sin0

and

A=Dz o8c sin 0 (13.8)

Page 245: Process Equipment

'*""'- *-^ffi**Yffiiffiitnmr

or

rcquired area is

, HDlz(f

P= 4=6w+h'twhere P = intemal pressure (in. of water)

W : weight of shell (lb)

D : diameter of tank (ft)

t/r : thickness of roof plate (in.)

Y - 49o lbttr

The equation for maximum pressure is then

P*":W * t,, (13.10)

The stess level at the head+o-shell junction must also be checked. In re-ferring o Fig. 13.3, vertical force V is given by

., PD ,Dv=__;__\th.l)-;

H =J _tan 6

H: 1 IPD -thrDfta'J9L4 4 l

Dzl\=#4r-to1

^ Mo tan d .r=--jr-+thy

13,2 API 630 TANKT {i60

lrtting a = 20,000 psi and I = 490lbfit3, this equation reduces to thc approx-Imate equation

- 30,8004tan0 ^r'N=--2 + 6th (13.1 1)

where P = intsmal pressure (in. of water)

A = required area at roof-to-shell junction (in.'?)

= angle as defined in Fig. 13.3

D = diameter of tank (ft)

4 = roof thickness (in.)

Equation i3.11 may be rewritten to calculate the required junction area -A as

. Dz(P - 8t,\A : --------:------'-- 30,800 tan 0

(r3.r2)

API 650 assumes failure to occur when the stess in the junction area reaches32,000 psi. This is an increase of 60% over the allowable sness of 20,fi)0 psiused in deriving Eq. 13.11. Hence failure pressure can be expressed as

4: r.6P - 4.8r, (r3. l3)

whete P1 : failure pressure (in. of water)

,P = desigp pressure (in. of water)

A = roof thickness (in.)

The sepond tenn in Eq, 13.13 is an adjustment factor that corrslates this equationwith experimental data.

When the roof-to-shell junction is designed so that failure because of exces-sive surface pressure occurs at the junction rather than the roof or shell, thejunction is called frangible. A frangible joint design equation can be derived bysubstituting Eq. 13.10 into Eq. 13.13, which gives

ryY . Bh, = 1.u, - o.r u

e=ffi+tt,

Page 246: Process Equipment

Sub8titutlng thia oquatlon into Eq, 13.12 givcs

0.153 W30,800 tan 0

where .4 : required tangible roof-to-shell area (in.2)

17 : weight of shell

d : angle of roof with horizontal axis (degrees)

(r3.14)

Note that failure of a frangible roof joint is only possible when the wetding isfrom one side.

13.2.2 Shell Design

API 650 includes two rnethods for the design of shells. The first is called the"one-foot method," which consists of calculiting Ae re4uir"O ttrict<r,"ss of sn"lcourse A in Fig. 13.4 based on the hydrostatic pressure at I ft above point X

Fisure 13,4

It.2 AFI 610 TANKT ilTl

which is the circumferential oeam between courses A and B, This mcthodconsiders that the bottom plate on course B stiffens the next course at point X0nd the maximum stess occurs at a location higher than X. This location isarbiharily set at "one foot."

At point X the hoop stress is given by

.PD-2tor

25

Defining y : 62.4 pcf and adding the corrosion allowance to this expressiongtves

(13. r s)

where CA : corrosion allowance (in.)

D : diameter of tank (ft)

G : specific gravity of liquid

I1 - liquid height (ft)

S = allowable stess (psi)

I = required thickness (in.)

The second method, the 'variable point method," is an extension of theone-footmethod in that it calculates a more exact location of the maximum stressnear the junction of the bottom or shell courses with differing thickness. In thiscase the bottom course is assumed to be hinged at its junction with the bottomplate. Hence the deflection due to intemal pressure at the junction is equal to thedeflection due to an applied shearing force as shown in Fig, 13.5. From Section{t 1

4:6pV PR2

TFo= n

.. ZB3DPR'

'= E-

-_Gy(H-t)D

t:2.6p(H_- r)G + cA

Page 247: Process Equipment

Fieur€ 13,5

The hood stress at any point along the cylinder close to the junction ls given by

Na=pR(l_Ca.)

where.c& is given by F{,. 5.23. Taking the derivalion of this equatlon withrespect to .r and equating it to zero gives the point of maximum Nr.'This occursat

'IAT 'OTTOM ?AI'IKS

and

Hence

t = Ne/S

_ 1.06 pPs "'or using the terminology of ApI 650

3tr4p

lr, = rn(r - "n,to "o"3!)= 1.06 PR

'= rr.oor(a!429)

13.2 APt 650 TANKS 473

'l'osts have shown that this equation is too conservative because the maximunlstrcss can be many feet away from thejunction where the pressure is reduced andthe stiffness ofthe second course becomes signincant. Accordingly, the equatbnlirr the desisn of the bottom course is modified to read

( 13. l6)

The thickness of the second course is determined from the following equations;

.2-

It-=t^ + (t.

-t^\l 7l'4/t -''.L.2-

where t2 : thickness of first course (in.)

/z = thickness of second course (in.)

lz = thickness of second course calculated from the equation for uppercourse (in.)

ftr = height of first course (in.)

r = radius of shell (in.)

Design of the upper courses is based on the equation

t, ir +<r.37sh. -l

h,- ,r*--,1 ir l'375 <;;<2'62s

t,. it L-z.ezs

2.6DlH - x / 1,21Gl : ___- s- + L]A

(t3.r7)

(13.18)

where "r is the variable design point that is a function of the thicknesses of layers,tank radius, and liquid height.

In referring to Fig. 13.6,.r is the minimum value of .r1, -r2, and "r, obtainedfrom the following equations:

q = o.6r{E + 0.32 ch,

x2 = Ch"

xz = l '22lrt"where

t ={.*,(*=-!I + K\/K

Page 248: Process Equipment

--* nr-Tfflffiffiiifrir

VARIAELE \oEstcit Fo[{T

3 OF TASHELL

'"1-:0.3iI

0.61

Gh,

fr/

MDIALGROTITN

Hrr. OF xi /+'1.o;c-o.xr

I 'll'Tn I

,6+j.-lv

0..'ffi\

t D, \ lh,,t1t.-{// --Et-

Figure 13.6 Elo3fic nrov€ment oI rh€ll cour!€. ot girth ioint (R€t. 5).

locATtot{CF TAN(

iflN.WHEl,l

UNRESTRAIT{EDMDIALGROTIT'TH

I *=?

After establishing the shell thickrtowindroadsm'it*.n*d.ri:;lil:J"-Hfr::3*Tilffi if:#,::;as

p = O.00256 V2

where p = wind pressure (psf)

V = wind velocity (mph)

API ,yses

a__100-mph wind velocity for design purposes unless a higher value isspecified. Hence

P = 25.6 Psf

Because the pressure distribution may cause a vacuum on part of the shell, theshell is designed to withstand a yaglum pressure of 25.6 psf. A simplifiedexpression for the buckling of cylindrical s-hells is given Uy fq. O. tZ as

r3.2 Apt 6t0 TANKS 47t

P _ 2.42E ( (t/o)rt 1Fs (r - *zltte \n /o - o.4s \/;lDl

or for long cylinders with E : 30 x 106 psi and p = 0.3,

H =77.e2 " ro.#,l/*)"r" \u/

Substituting P", : 25.6 psf and FS : 2.0, this equation becomes

(13.19)

where Il = length between stiffeners (ft)

t : thickness of shell (in.)

D = tank diameler (ft)

The required section modulus of the stiffening ring necessary for resisting thelateral pressure is obtained from the following classical buckling equation of aring:

^ 3EIR3

- 3EI

" :

Fs(R)

where

Hence

F= PH

PrlilFS)3E

PHD2 FSz=2AE C/D

(r3.20)

Page 249: Process Equipment

1rt illT tonom ?aNl(t

API arsumca that tho rstio of thc outstanding leg of a stiffener to thc diameterof the tank is not lcss than 0.015. Hence, C/D = 0.0075. Usins FS : 2.0.P = 25.6 psf, E = 29 x 106 psi, and expressing D and If in feet,-the equationfor the required section modulus of a stiffening ring is

Z = O.Offit HD2

where z = requirc.d section modulus of stiffening ring (in.3)

II : height between stiffeners (ft)

D : diameter of ta.nk (ft)

| 3.2.3 Annulor Plqtes

(r3.21)

The requircd thickness of the bot8om plate in an ApI 650 tank is given in Table13.1. At the shell-to-bottom plate junction, the ApI standard requires a butt-welded annular plate whose thickness varies between 0.25 and 0.15 in. and isa function of the shess and thickness of the first shell course. The width of theannular plate nust be adequate to support the column of water on top of it in cas€of a foundation settlement. By referring to Fig. 13.7,

*=+Using plastic analysis,

L=

L=

Letring p = 62.4 pcf, a), = 33,000 psi, and expressing H in fe,et and 4 ininches, the equation becomes

. _ 195 tb- \/GH

API 650 uses a factor of safety of two for the length. The length of the annularplate is thus expressed as

4M

RY;t;fr

"l yGH

390 h\/ GH

L= Out not less than 24 in.) (r3.22)

!;rlll.rr{jwlillirfrs

I3,2 APt 650 TANKT 4ll

( al

lM

,

(b)

tisut 13.7

where tr : length of annular plate (in.)

/a : thickness of annular pla0e (in.)

1l: height of liquid (ft)

G : specific gravity of liquid

Exarnple 13.1. The steel tank in Fig. 13.8a contains a liquid at the roof-to-shell junction level. Eesign the various tank components if G = 1.1, CA =0.0, S = 15,000 psi. Use the "one-foot" method for shell design.

Sohtian, For the roof design, Eq. l3.l gives

' = 0.40 in. Use t : 7116 in. for the dome roof

For the shell design the required thickness for the bottom course is given by Eq.

n80' 2M -' 2n

Page 250: Process Equipment

ata 'ltt

torTors ?A]{t(l

(.)

(b)

Fisur6 | 3.8

13. 15 as

. 2.6(80\Qo - txl.t)' 15,m0

= 0.29 in. Use r = 5/16 in. for the

For the top course

. _2.6(80X10-1x1.1)- 15,000

= 0.14 in. Use t - 1/4 in. for the top course

bottom course

Angl€ 4r4xt

according to Table 13.1

':.!1].:, ., ]''' ',]i!,!r

lV'r3,2 APt 6!0 ?ANK3

The required inteffiediale stiffener spacing is obtained from Eq. 13'19 ae

I/ = 6(100t)

Usins a conservative value of t : 0.25 in.,

I1 :6(100 x 0.25)

= 26.20 ft

Zroo t o:sVv\s"/Because this is larger than the height of the tank, no intermediate stiffeners are

needed.The required area of the roof-to-shell junction from Eq. 13.5 is

,DR" 1500

_ (80x80) ,

1500

: 4.27 n.2 Use 4 x 4 x 5/8 in. angle with A = 4.61 n.2

For the bottom plate use t = ll4 in. according to Table 13.1.

Assume the annular plate is 1/4 in. thick. Then the width of the armular plate

from Eq. 13.22 is

. 39ohL = ------_

YGH390 x 0.25-:ffi

L : 2JJ79 in.; Use a 24-in. wide annular plate

The above details of construction are shown in Fig. 13.8b. I

Example 13.2. In Example 13.1, determine (a) the maximum allowable inter-nal pressure and the maximum failure pressure, (b) the required roof-to-shellarea if a ftangible joint is required, and (c) the thickness of the shell using the

design conditions of Example 13.1 and the variable point method.

Solation

(a) The maximum pressure that does not cause uplift of the shell is obtained

ftom Eq. 13.10:

Page 251: Process Equipment

-'. -*-ry--'fil?Yffiii irrxr

wctght of eholl = (a0.82)(a)(EO)(tl)(s/16 + U4)

= 57,800 tb

. _ 0.245 x 57,800 ^r'*=--lo-+Ex0.437s

= 5.71 in. of water

0.t53 W^ - 3oSoo t"" d

_ 0.153 x 57,80030,800 x 0.577

A = 0.50 in.,

(c) The thickness of the bottom course is calcrilated from

,=(t.*-: 0.30 in.

0.463 x 80

m

For the top cowse, the quantity

15,m0

h1

Yrtr

r3,2 APr 630 IANKS 4tl

-10l0x12v(40 x 12x0.3)

indicates that tz : t2! as given by Eq. 13.17.Equation 13.18 is based on an iterative process that is initiated by assuming avalue of f2, which can be obtained from the approximate equation

: 0.21 psi

The maximum pressure that does not cause excessive stess ai the head-to-shelljunction is giveo by Eq. 13.11 as

^ (30,800x4.61x0.s77)

: 16.3 in. of water

= 0.59 psi

Thus, maximum intemal pressure = 0.21 psi.The failure pressure from Eq. 13.13 is

Pr: 1.6 P - 4.8 A

= (1.6)(s.71) _ 4.s(0.437s): 7.04 in. of water

p1 = 0.25 psi

(b) The frangible joint arca given by Eq. 13.14 is

r. O1nK=-=1':-;=2.14t" u. t4

C : 0,59

.r, : 0.6tV@l-iZXo5 + 0.32(0.5eX10 x 12)

:29.98

rz: 0.59(10 x 12)

= 70.80

2.6H- t) DGt": '-' 15,000

_2.6x9x80x1.115,000

: 0.14 in.

From Eq.13.19,

=10

Hence -r : l0 controls and

xc = 1.22Y(40 x l2)(0.14)

Eq. 13.16 as

2.6D@ - x /r2\Gtz= a,-2.6(80X10 - ro/r2)(r.D

15,000

= 6.1a f.Because this value is the same as the assumed one, the analysis is complete,

and no additional iteration is needed. Hence. use

h: 5/16 in. for the bottom course

tz: l/4 n. for the top course as govemed by Table 13.1 I

6x20x80x1.

Page 252: Process Equipment

-' -.---ru-*ryffiffiiuffiTtliii

I3,3 API 620 TANKS

API 620 tanks2 tend to be more complicated in geometry and are generally

:llJ9:Id g hiekr-ilptt^pressu'e than Apr 650 tank;. Accordingly, trr!r€quirements of API 620 differ significantly fiom those of ApI 650 because themrckn€ss of the components is obtained from shess analysis that considers thebiaxial shess state rather than a set of simplified formulas.

_ The shess analysis procedure in Apl 6t0 is based on Eqs. 6.10 and 6.11.Equation 6. I I for /Vd can be determined- for any shell configuration by using thesummation of forces obtained from a free-body diagram.-The advantage of afree-body diagram is that forces other than pressure cair be accountedlor withoutC:inF tryugh T inregration process. Once Nd is determined, the value of ly'e isobtained ftom Eq. 6.l0 as

l&*&=oR2 Rr

where Ne = X of forces at a given cross section.

(r3.23)

Example 13.3 illustrates the application of \. 13.23 ro ApI 620 tanks.

Example 13.3. The rower shown in Fig. 13.9 is filled with a liquid whosespecific gravity- is 1,9 rlp to point d. Above point a the tower is subject€d to agas pr9sswe of 5 psi. Determine the forces in the various components of thetower disrcgarding the dead weight of the tower.

Solutian

Roof Forces

The maximum force in the roof is obtained from Fig. 13.10a. Below section a_o,a 5-psi pressure is needed to balance the pressurJabove sectjon a_a. Force lVuin the roofhas a vertical component V around the perimeter of the roof. Sum_mauon ot torces in the vertical direction eives

av - ,o,ll o

v=!=s"ff= 600 lb/in.

Hcnce

-=ff;;%

. ..2iL$tua

r3,3 APt 620 TANKI 4ts

'l .62,4 pct

and fron 84. 13.23 with R1 : Rz = 48 ft,

5x576

: 1440 lb/in.

and the unbalanced force 11. : 1309 lb/in. (inwards).

40-Ft Shell

The maximum force in the shell is at section b-D as shown in Fig. 13.10r. Totalweight of liquid at section D-b is

w

=:rr^;*:X,:,o,Total pressure at r-, is 5 + (62.4/144)(35).

P = 20.17 psi

Sum of the forces at b-b is equal to zero. Hence,

2,744,s00 - (2O.17)GiQaD' + v1ay480; : 3

V = 600 lb/in.

^, _PR_t\o - 2 -

Figur6 13.9

Page 253: Process Equipment

' -- " - ffi **ff IYI#iiiSii'ilirr

b- - -

(e)

.-b

v

o)

b"-

and

iV' = 600 lb/in'

In a cylindrical shell R, = oo and Rz = R. Hence Eq. 13.23 becomes

Ne_pR=(n.n)(?/io)= zt84l lbiin.

Conical Trawition

At section b-b force V in the zl0-ft shell rnust equal force V in the cone due tocontinuity, as shown in Fig. l3.l0}.

lV:i

Tfr-{-tT

Figuro 13.10

r3.3

\,4)"1'nr'

API 620 TANKS 4T5

(c)

c- +-

c- _c

----d

Figurc 13.10 (Continvod)

V: 600 lb/in.

-. 600wo = di6

: 849 lb/in.

= co and iz = R/sin L Hence Eq. 13.23 becomes

(d)

and

In a conical shell R'

Page 254: Process Equipment

'"" -" --ilffi*-"""Tiiftl6ffii'iinn

&=g =uo?o:!!)srn 0 -- 0.707

= 6847 lb/in.

The horizontal force at trnint b is Ho = 600 lb/in. (inwards) !Figure 13.10c shows the forc€s at point c. The weight of tiquid in conical

section is

*=4rl+R,R,+n3)

_nx62.4 x 10..^" .^-3 -(Iy+

l0 xzo+202)

: 457.2100 lb

Total liquid weight is

W : 2,744jffi + 457 ,4n = 3,201,900 lb

Pressure at section c-c is 5 + (62.4/ A0@S\.

p = ?A.5 psi

Sumrning forces at section c-c gives

('24.s)Gr|(r2o)2 - 3,201,900 - (v)Giea\ = oV = -2777 tbtin.

- The negative sign indicates that the vertical component of iy', is opposite tothat assrrmed in Fig. l3.l0c and is in cornpression Ltner man 6nsion. This iscaused by the^column of liquid above the cone whose weight is greater than thenet pressue force at section c-c.

-.t11''- 0.707

: -39271blin. (compressive)

l/o = RPlsin 0= tZOx 24'5' 0.707

: 4158 lb/in.

H. : 3927 lb/in. (inwards)

13,3 APt 620 TANKS 4tt

20-Ft Shell

At section c-c the value of V in the 20-ft shell is the same as V in the cone ducto continuity. Thus

N1 = lt : -2777 lbli'..'

,'1llol,ff^",,,',

At section d-d the liquid weight is given by

W: j,?rr,9oo + (62.4)(n)(r0)2(zs)

= 3,692,000 lb

and the pressure is calculated as

/6) A\P=s+l#l(70): 35.3 psi

From Fig. l3.l0d the summation of forces about d-d is

3,692,W - 35.3(r)(r2o)2 + v(r)(2$): a

N6 : l/ = -2177 lblin'

which is the same as that at point c.

No: PR = (35.3X120)

:4236lblin. I

13.3.1 Allowqble Stress Criterio

The required thicknrcss of API 620 components in iension is d€termined from thelarger of the values obtained from these two exDressions:

, =N'-sE.rt{"' ,tE

(13.24)

Page 255: Process Equipment

488 FIAT SOTTOM TANKS

whorc t : rcquircd thickncss ol'componcnt (in.)

Ne = hoop force (lb/in.)

No : meridional force (lbs/in.)

J = allowable tensile stress (psi)

E = joint efficiency similar to discussion in Section 8.1

The API criteria for components in compression are as follows.

Compressive Stress in the Axial Direction wilh No Stress in the Circum-ferential Directian

The rules for this case are based on the axial buckling of a cylindrical shell asgiven by Eq. 5.28. With E = 30,000,000 psi and a factor of safety 10, thisequation becomes

( 13.2s)

13.3 API 620 TANKS 489

Compressive Stress with Equal Magniludc in the Meridional and Circum-lerentinl Dbections

The goveming equation is obtained from Eq. 6.35 for the buckling of a sphericalshell with a factor of safety of four. Using E : 30,000,000 psi, the equationbecomes

a= srz,soo(*)

which is approximated in API as

/.\r,ooo.oool;l

\^/(13.26)

,=,.,,,o'(f)This value is 1.8 times smaller than the value given by Eq. 13.25. Accordingly,the limit ofEq. 13.26 is established as 15,000/1.8 = 8340 psi. Thus oDElc inFig . I 3 . I 1 is the criteria used for components having compressive stress of equalmagnitude in the meridional and circumferential directions.

Compressive Stress with Unequal Magnitude in the Meridional and Circum-terential Directions

The criteria for this case are based on the following equations:

(larger stress) + 0.8(smaller stress) < 1.0 (13.27a)shess determined fuom OABC tn

Fig. 13.11 using R for the larger force

1.8(smaller stress)

To prevent the stress in Eq. 13.25 from exceeding the allowable tensile stressof the material, an arbihary value of 15,000 psi is established as the upper limitof the allowable compressive stress. This is shown in Fig. 13.11 as line OABCwhere 4-B is a transition line between Eq. l3.ZS and the upper limit of 15,000psi.

at

Ethooo

o

shess determined from OABC inFig. 13.11 using R for the smaller force

< 1.0 (13.27b)

Compressive Stress in One Directinn and TensiJe Stress in the Other Direction

The criteria are based on the assumption that the capability of a component toresist compressive force in a given direction is reduced as the tensile force in theother direction increases. The goveming relationship is derived as follows. Let

, - actual comoressive stressrrr --ii_------:-i--------------

allowaDle comDresslve sresstuom OABC of fin. t:.tt

tE

Figure l3.ll (Coortesy of the Anericon Perrol€um Inlritute.)

Page 256: Process Equipment

fLAt lotTot TANKS

und

^, _ actual tensile stress,r - r-i-----_:-i_--- -allowaDle tenslle stress

The interaction of this equation with Eq. 13.25 is shown in Fis. 13.12.

13,3.2 Compression Rings

As shovn in Example 13.3 there are unbaranced horizontal forces at the roof-to-shell and cone-to+hell junctions. These forces must be carried by a com_p_ression ring region at that location. The region can be in tension or compressiondepending on the direction of the discontiriuity as well as the troop torces. apt620 as-sumes that portions of the roof, shell, and cone shown in He. 13.13 are

t*^.,.l_T :*pt":tioT ring region._ Th9 total force given Uy tt-e torro*ingequaron ls assumed to be supported by the ring region:

Then

M2+MN+N2=1.0 (13.28)

l" *r'o

6

I

6

!3

\t:

iB

Flgura 13. | 2 Sioxiol stress chon for combinod retuion ond comprelsion 3O.Om p3i ro 38,OOO pst yietd srr$srt.oh. (Courrory of rh6 Am6ricon petrol€sm tmrirute.l

(r3.30)

I3,3 API 620 TANKS 491

Rool ol l8nk

Fisur€ 13.13 Compr€ssion rins rasion. (Courtosy of rhe Americon Pelroleum Inslitute.)

Q=Na,Wn+N1'"W"+HR (r3.2e)

where Q : total force at ring region (lb)

Nr. : meridional force in roof or cone (lbiin.)

N0, : circumferential force in shell (lb/in.)

I7r, = effective length of roof or cone as determined from Fig. 13.13(in.)

W" = effective length of shell as determined from Fig. 13.13, (in.)

11 : unbalanced horizontal force at junction (lb/in.)

R : radius of tank at junction (in.)

The total required area at the junction is determined from

: is,ooo--L when Q is compressive

= # when Q is tensile

Page 257: Process Equipment

'.' --*""*'ffi **TffiTffi f irmr

whorc A - roqulrtd a,rpa (in,2)

S = Allowabie t€n6ils stress (psi)

E = joint efficiency

Details of various ring attachments are shown in Fig. 13.14.

Example 13.4. Deterrnine the required thicknesses of the 20_ft shell and theconical reducer in Example 13.3. Also detemine the required stiffening ringarca at point c. I,et S : 20,000 psi, E = 1.0, and CA :0.O.

Sohttian

20-Ft Shell

From Example 13.3 the forces at point c are

No : -2777 lVn'ffd = 2940lblin.

and the forces at point / are

Nt : -2177 lbln.Nd = 4236 lblin.

Thus forces at point d control. From Eq. 13.24,

4236'- 2o"ooo x lo

= 0.21 in.

. 9.t=i6-'

f.: o.oo+z

actual tensile r*rr = ffi = 7530 psi

kt

Then

P..niisibl. wh.r. rEf (ft bor+.E)pldl! thi.tn... i5 nor 6v.tiir.z4t, tf-

Y-JNot P.rh'.3rbrc

Figurol3.14 som€ Fmi.libl. qnd noip6rml$lble d.lcik ot compr€$ioo'ringFiuicturo conJ?udioi. (cour-

!,6!y of {|. Amlricon Peholcum lnrtituL.)

493

Page 258: Process Equipment

actuel compressive sress = ffi = +S+O Vsi

allowable compressive stess from Eq. 13.25 = l.g x 106 10.5625\8zl40psi \-m-)=From Eq. 13.28,

.91 IIAT IOTTOM TANK!

7530 : 0.3820,000

M 4940=

,Ooo = O.SS

0.38'? + 0.38 x 0.59 + 0.592 =0.72 < 1.0 or user=9/16in. shell.

Conical Transition Section

From Example 13.3, forces at point , are

N, = 849 lb/in.

Ne = 6847 tb/in.

and from Eq. 13.24

' = 6847

20,000

: 0.34 in.

Forces at point c are given by

N, : -3927 lblin.

l/a : 4158 lb/in.

L€t

t = 11/16 n.

, 0.6875R= 120 = 0.0057

actual rensile rt "rr = ffi = 6o5o psi

Then

13.3 APr 620 TANKS 495

actual compressive ,o"r. = o%- = 5710 Psiu.t)6 /)

allowable compressive stress from Eq. 13.25 - l'8 x 1q10 6875 = 7290 psi

ru=ffi=0.:o

n =W: o.ts7290

0.302 + 0.30 x 0.78 + 0.78'? = 0.91 0K

use t = 11/16 in. for conical hansition section

Compression Ring

From Example 13.3 the discontinuity force at point c is

H = -3927 lb/in. (inwards)

w. = 0.6 (120X0.s625)

= 4.93 in.

/ rtn \Wt' = O'6 {;+ | (0.6875)" \u. /u// '

= 6.48 in.

Na : 2940 lb/in.

No, = -3927 lblin'

Q: C3927)(6.48) + 2940(4.93) + (-3927)(r2o)

: -482,190 lb

From Eq. 13.30,

, _ 482,190" 15,000

= 32.15 n.2 required area

available area = (0.6875X6.48) + (0.5625X4.93)

= t.25 |It.-

needed area = 31.25 - 7 .23 = 24.O2 in.2

Use 2 in. x 12 in. ti"g. I

Page 259: Process Equipment

.9O ILAT IO'TOM TANKS

I3.4 ANSI 896.I ALUMINUM TANKS

The rules for ANSI 896.1 Tanksr follow the same general criteria as ApI 650rules. Differences in various requirements between ai-uminum anJ sieet tants aregiven in Table 13.1.

| 3.4. I Design Rules

The design of dome roofs is obtained from Eq. 9.2b and is based on a factor ofsafety of 4.0. Hence,

o.06258

\R/t)'

Using E = 8,000,000 psi at 400T, this equation reduces to

R-t = ToiYP

where r = thickness of dome roof

R = radius of roof (ft)

p = dead and live loads (psf)

The required area at the roof-to_shell junction is obtained from Eq. 13.4:

O_DRpcos04o

A conservative value of cos 0 is taken as 1.0. Hence,

(13.33)

(13.31)

(r3.32)

^ _ PRD

4o

where A = required area at dome roof_to_shell junction (in.z)P = dead and live loads (psf)

4 = spherical radius of dome roof (ft)

D = diameter of shell (ft)

o = allowable tensile shess of roof, shell, or junction area, whicheveris less (psi)

The required thickness of a self-supporting conical roof is obtained flom the

I3.4 ANS 896.I AI.UMINUM TANKS 497

lilllowing expression, which is similar to Eq. 13.5:

, = r"oo Y:-,e)I (13.34)- 897 sin 0

ANSI 896.1 uses an approximate equation which, for the design of conicallrxrf.s, is given by

D \/Ft=-- 1414 sin 0

( 13.35)

where r = required thickness of cone roof (in.)

D = diameter of tank (ft)

P = dead plus live loads (psf)

0 : angle between cone surface and horizontal base (degrees)

The required area at the cone roof-to-shell junction is obtained from Eq . 1 3 . 8its

PD2-- 8o sin d(13.36)

where A = required area (in.')

P = dead and live loads (psf)

D = diameter of tank (ft)

o : allowable tensile stress (psi)

0 = angle between cone surface and horizontal base (degrees)

The design of aluminum shells is based on Eq. 13.15, which is based on the"one-foot" method given by

2.6D (H - tt GI:_----.4

where r: shell thickness (in.)

D = tank diameter (ft)

11 = height of liquid (ft)

G = specific gavity

(r3.37)

Page 260: Process Equipment

498 FLAT IOTTOM TANKS

/ : ulkrwablc tcnsile stress ol'alurninum (psi)

- _ PHD, (FS)48 E Q/D)

In an elastic body,

f = Ee ( 13.3e)

and for a stiffener in bending, the relationship between strain and curvarure r

e = joint efticiency

ANSI B96.1 does not contain mles for intermediate stiffening rings. For opentop tanks, a stiffening ring is required, *hich is basJ;; a. 'iilio.

i" *,, ""*,Il is defined as the overall height of the t"* ,J-E{I.'liio;;";;".

tt= 2R

Hence, from Eqs. 13.39 and 13.40

(13.38)

(13.40)

(13.4r)

t =f2D 2E

Substituting-this expression into Eq. 13.3g and using a factor of safety 2.0, theexpression for the required section modulus Z becoires

z = 0.084 PHD'

fwhere Z = required section modulus (in.3)

P : wind pressure on tank (ps|Il = height of tank (ft)

D = diameter of tank (ft)

/ : allowable stress of stiffening ring (psi)

I3.5 AWWA STANDARD DIOO

Most water tanks are built in accordance with the ..American Water WorksAs.sociation Standard for Welded Steel Elevated Tankr, Si_Jpio".,'_o n"r"._voirs for water Storage.'a The standard gt";, f"* ;;";#" ;;";ons rbr the

BIETIOGRAPHY

dcsign of components. Instead it outlines the general requirements associatc(l

with design loads, earthquakes, allowable compressive stress in columns, radio-graphic examination, and so on. Most of the requirements in API 650 can bc

applied to AWWA tanks. Some exceptions are given in Table 13.1.

REFERCNCES

l. Weldcd Steel Tanks for Oil StoraSe, 7th ed., API Standard 650, American Petroleum Institute,Washiqton, D.C., 1980.

2. Recommended Rules for Design and Construction of Large, welded, Lout-Pressure StorageTanks, 7th ed., API Standard 620, American Petroleum lnstitute, washington, D.C., 1982.

1. American Nation^l Standard for welled Aluminum-Allo! Storage fdt tJ, ANSI 896.1-1981,America[ National Standards Institute. New York. 1981.

4. AwwA Standotd fot Welded Steel Elev.tted Tanks, Standpipes, and Resen'oirs for waterStoraS?, AWWA Dl00-73, Afterican Water Works Association, New York, 1973.

5. Zick, L. P., and R. V. Mcclath, "Design of Large-Diameter Cylindrical Shells," presented

at the 33rd Midyear Meeting of the American Pekoleum Institute, 1968.

6, Karcher, G. G., "Stresses at the Shell-to-Bottom Junction of Elevated-Temperature Tanks" inl98l Proceedings-Refning Department, 46th Midyear Meeting, American Petroleum Insti-tute, May 1981.

BIBTIOGRAPHY

Steel Tanks for Liquid Storase-Steel Plate Engineering Data, Vol. l, Americao hon and Steel

Institute, Washington, D,C,, 197 6.

Page 261: Process Equipment

Rod bdffle h.or €x.honsers. (Courr$y of ihe Noorer corpororion, Sr. touis.)

501

CHAPTER 14HEAT TRANSFER EQUIPMENT

Page 262: Process Equipment

HEAT TRANSFER IOUIPMENT

Heet transt'er cquipment is used in many applications such as boilers in powerplants, heat exchangers in the petrochemical industry, and condensers and evap-orators in heating and refrigerating systems. Heat transferequipment varies fromminiature heat exchangers a few inches in diameter to power boilers over 100ft long. This chapter presents the theoretical background and design equationsof heat exchangers and boilers.

14.I TYPES OF HEAT EXCHANGERS

Heat exchangers in the United States are normally designed according to theStandards of Tubular Exchanger Manufacturers Association (TEMA)I and theASME Code, VI[. In general, TEMA requirements are a supplement to theASME requirements, for they tend to include areas not discussed in the ASME.Most of the TEMA design e.quations relate to tubesheet design when affected bydifferential pressure and temperature, expansion joints, bustles, and so on.

TEMA uses alphabetical designation to differentiate between vadous types offrequendy used components. This is illustrated in Fig. 14.1. The componentscan be interchanged to form a wide variety of heat exchanger configurations, asshown in Fig. 14.2.

Their rules, which apply to thft€ different classes of construction dependingon the severity of service, are referred to as R, C, or B. A summarv of thedifferences between these classes is given in Table 14.1.

Tqble 14.l Some TEMA Requiremenfs of Closses R, C, qnd B Exchongers

Paragaph

Service

Corrosion allowance(cafton steel)

Shell diameter

Minimum thickness oflongitudinal baffle

Minimum tie roddiameter

Prefened gasketcontact surfacetolerance

Minimum bolt size

Severe Moderate

i rn. * in.

8-60 in. 6-60 in.

i h. I in. carbonste€l

I in. atloys

; in. i io.

!+ None

t.l21.15

3.3

4.42

4.71

6.32

l0. t

General

-l in.

6-60 in.

I in. carbonsteel

"1

in. alloys

i in.

None

t in.?n. s j in.

503

.'AT|oNARY I{€AO TY?II

A

a

-Jl llrla-!ii!r

BONNET (NftCRAI

III

c

N

CIIANNEL II

D

SPECIAL TiIGH PICSSUR€ CTOSUNE

atiEu tYPl5

E

ONE PA3s SHETL

F

TWO PrSs SHEI!WITTI TONGITIJDINAL AAfRC

G

H

J

K

KETILf TYPE RE'OILEN

x

Figurs l,(.1 Vorio{rs IEMA component6. (Courtesy of the Tutulor Exchong€r Monufo€turoi! Alsociotion, Inc.)

raat aNo

L

'1t'-ii'----tlll!-i l,-tn

-lL---,?'-"-'---'JUflxlo Tuscs8fEr

LIKE 'A" STATIONARY H(AO

ll,l

-_ !i i:

---{11=i l-\

-tL---.>fIXED TUBESHEI

LIKt "8" STATIONARY IIIAD

N

ftxED TutEska6tIIKT 'N" STAT|oNARY I]EAO

p

OI,i'!;IDE PACKCD FLOATING 'IEAO

s

+J11------

----Lfn\ \.---LI $.=.!a_(n===

FLOATING HEADWTH

'ACKNG DEVICE

IPUTI THROIJOh fLOATING HEAO

u

o_-'1-1-------------\\| | ,lfu-

IJ-IIJBf SUNOLE

w__'ii', __

--r-€:++:.,:zlTT6---r=--l \ lu-----t=:E-+€xrERft^trY slatEDFIOAIINC TUBTSHEEI

Page 263: Process Equipment

:'l*: ].o ,

_ typicol h6ot er(chons.r confisurorion5. (Court€r), of rho tvbolor Exchonser /$dnurodurers

5(M

AJWFis'lrc l,{.2 (conrinued)

I4.2 TEMA DESIGN OF TUBESHEETS IN U-TUBE EXCHANGERS

The basic equation for the design of heat exchangers is obtained from Examples

7 .l and 7 .2 ^s

|.'APaz" = T for simply supported Plate

0.7 5Pa2o = -7= for fixed plare

Letting G = 2a and solving for the required thickness gives

, =ttE {', rornxedprate

50s

Page 264: Process Equipment

5OO HIAT TRANS;IR IOUIPMTNT

whcrc Cr is a constent that is based-on such parameters as ligament efficiency,tubc.stiffening effect, and method of edge suiport. n" fiV"e

"q""tion for therequired thickness of a tubesheet in bending is based on a t^t6i C, _ g.77.

Hence.

t,Vs

e,= cr( -e)

PA

-_FG'-7where I = required thickness of tubesheet

G = diameter

P = applied pressure

S = ASME allowable tensile stress

F = factor equal to I . 25 for simply supported plate and I . 00 for a fixedplate.

- Tle $earing stress in the tubesheet at the outer tube perimeter must also bechecked and kept below an allowable stess. The tota force W aue io press*ein the tubesheet of Fig. l4.3is

W=PA

The shear area A" through the outer perimeter is obtained from Fig. 14.3 and is

Hence the shearing shess o ls expressed as

wA" Cr(l - d,/p)

The allowable shearing s[ess in the ASME Code, VIII-I, is given by

a = 0.8S

Thus Eq. 14.2 becomes

T _ 0.3tDL lP\0 - dJpt\i)

w\erc DL = 4Af C

A = area of tubesheet within outer tube perimeter

(14.1)

(14.2)

I4.2 TEMA OESION OF TUBESHETTS IN U-TUBE EXCHANOTNS 507

: perimeter of outer tubes, as defined in Fig. 14.3

= outside diameter of tube

= distance between tubes

Example 14.1. A tubesheet for U-tube exchanger has a 12-in. diameter and is

subjected to a design pressure of 100 psi. If the tube layout is as shown in Fig.14.4 and S : 17,000 psi, what is the required thickness? Assume the edge tobe simply supported.

C

d"

p

Fisurs l,{.3

(14.3)

Figuro l,{,,(

Page 265: Process Equipment

IOI HIAT IRAN3IIR IOUIPAATNT

Solullon, F'ronr Lq. 14. l,

- _ (r.2s)\r2)2

= 0.58 in.

From Eq. 14.3 with

A = rR2 : 98.17 in.2

and

C = 34.97 in.

= 0.08 in.

Thus f,*, = 0.58 in. I

r4.9 THEORETTCAI ANArySts oF TUBESHEETS tN U_TUBEEXCHANGERS

Gardner in 1959 published a papef that explained the interaction between thetubes and tubesheet in U-rube ireit exchangers. Gardner assumeJthe interactionto be represenr€d by Fig. 14.5. Hence thJ bending in th";1;.;-

,r= -nTt

- _ 0.31(4 x 98.17 /34.97, / too \(1 - 0.7s/r) \17,000/

(r4.4)

F'sur6 la.5 (R€f. 2)

I4.3 THTORffICAI ANALYSI5 OT TUBISHEITS IN U-TUBE EXCHANGTRS

where M7 : bending moment of tube

Er : modulus of elasticity of tubes

11 = moh€nt of inertia of tube

I = baffle spacing as shown in Fig. 14.6

0 : rotation of tube at tubesheet junction

4 = factor relating effect of baffles on tube-end bending momentgiven by Fig. 14.6

Similarly, the radial bending moment in the tubesheet is given by

,. NErlrF,a,rM, = __:,- ( 14.))

TA'l

M, : ndial bending moment in tubesheet

N = number of tube holes

Ar = radius increment as shown in Fig. 14.5

a = radius of tubesheet

509

DXFn

1 2 3OrMore

o 4.OO 400o.2 3.83 3a3

OA 3.69 3.70

o.6 359 3.60

o8 3.52 3.53

1.O 3.OO 3.43 3.46

Figure 1,t.6 (RcI. 2)

Page 266: Process Equipment

I)clining

'= cry#)"'where D* is the modified flexural rigidity of the tubesheet and ly' is the totalnumber of tubes. The differential eEq. 7.7 becomes rquation of the bending ofa plate as given by

dlt d (.dw\l _ e .,/d,u\drlr dr| El ] - o.' ,\d,)

(14.6)

(14.7)

(14.8)

(r4.9)

This equation can be solved in terms ofBessel functions. For a uniformly loadedplate, the solution can be expressed as

. =uJ-{1g1_!1_ Afto@") _ r"(U)t}dw pa3 / -I\ _

dr= o.\zu2)LU-Alt(utl

w = deflection

P = applied pressure

U.= (au=trA = constant of integration

10, 1r = modified Bessel function of zero and first order, respectively

D*=

.E'* = effective modulus of elasticity of perforated tubesneerZ = thickness of tubesheet

t,r = effective poisson,s ratio of perforated tubesheeta = radius of tubesheet

r = radius of a given point on tubesheet

d : tube diameter

p = tube pitch

For fixed tubesheets, the rohti,solved forA,: on at the edge is zero and Eq. 14.9 can be

E*73

I4.3 THEORETICAT ANALYSIS OI TUSTSHETTS IN U.TUBI TXCHANGTRS 5l I

for fixed edge ( 14. r0)IIU")

For simply supported tubesheets, the moment at the edge is not zero because theouter tubes have a bending moment that is transferred to the tubesheet. For thisboundary condition, the value ofAl is given by

for simply supported edge (14.1l)

A1

With the value ofA; established for the two boundary conditions, the values ofM,, M,, and Q can be obtained from Eqs. 7.3a, 7.3b and 7.10 as follows:

u,: r*fi{o + p+y - alro14 - 5Or,<rr]}a,= r' fir{o + p.t - elsaul +9nP4u,]} t'0 "'9 = rafir,<u)

The maximum value of M, can be obtained from Eq. 14.12 for variousboundary conditions and U values. Hence,

M'* = Pa2 F.

where F. : coefficient obtained from Fig. 14.7.The maximum bending stress is given by

(14.13)

' =e!e\ (14.14)lt \T/where r; = ligament efficiency of perforated tubesheet in bending

:p - dp

Also the maximum value of Mr in the tubes can be expressed as

maxMT = i(#),", (l4.ls)

Page 267: Process Equipment

,22

.20

.18

.16

74

12

.10

.oa

.ou I

""1.o2 |

u .t , "

Or-U 6 7 8 9 10

Fisurs ra.; Ger. 2l

*lY€ . 4 = coefficient obtained from Fig. 14.8.

, The interaction between the tubeshe"t ttii"t n"r. _O tt e pressure is illustratedoy combining Eq. 14.6 with Il" = !a: Etvng

(:)=h

t r-zts - T

AA (14.16)

where

^=ftztl=il4f.Nr,lt/tL l E+ Iasl

Also Eq. 14.13 can be expressed as

/l\= ^'\qo/ 6F^U2n

or

ff: ar.utu5t2

(14.17)

234567

rigurc 1,1.8 (ReI.2)

Equations 14.16 and 14.17 arc combined in a plot, as shown in Fig. 14.9.

Example 14.2. Find the thickness of the tubesheet in Example 14.1 if

E* : 9.0 x 106 psi lt* : 0.3

N= 88 Ir = O'0166

Er=30x 106 psi n= 3.46

l= 12 in.

1a\

Fisurg 1,{.9 (Ref. 2)

Page 268: Process Equipment

drAr la srlR laulPMlNT

Solullon. tct ?.= 0.24 in. Then

^* _ (9.0 x 106X0.24)r

12(1 _ 031) 11,390

U.:(a=18.78

From Fig. 14.7,

and from Eq. 14.14,

f. = 0.008 (conservative)

,=10--9'7s=0.r,

o_ (6)(0.008)(100)/ 6 Y0.2s \o.z+)o = 12,000 psi OK I

r4.4_-.BACKGROUND OF THE-li_t4E DESTGN EQUATTONS FORTUBESHEETS IN U-TUBE EXCHANGERS

The ASME Code, VII_I, uses the method in- Section 14.3 for designing tube-sheets. The tigament efficiencv 4^obtained from o',D#Jiii.Jrk, is sum_manzed in Figs. 14. t0 and 14. il . Because the diamet , oiti" ouirt" tuu. ,o*ls normally less than the tubesheet dlameter, an adjustment is made to Gardner,st4. t4.t3. The tubesheet is assumed ," "r"riri.ii" iirilr"i"Tllj,. , r"or,a and an outside ring of outer radius ,. Accordingly, Fig. 14.9 must be modified

::.J.j:., ft"-y,io_ot b/a. A sample of the curves developed by the ASMEruSgr_o_up on Heat Exchan8ers is shown in nigs. r+. r z anJi+ifr rlr. ^

, .r I .os.r,xpressing Eqs. t4.16 and 14.17 in rerm's oi r;;;;;;;;;;". g,"".

, = ",e.J (14.18)

where f = 6F^

c,=+s

I4,4 BACKGROUNO OF THE ASMT DESIGN TQUATIONS FOR IUBCSHTETS 515

< 0.6

6 o.s(,> o.4

H o.sUI

Also Eqs. 14.16 and 14.17 can be expressed as

o.1 02 03 04LtcaMENT EFFrcrEt{cY, ?

TAIANGULAB PITCH

Figure 14.10 (Ref. 3)

T2 P ,".)t2 a2 )t'rlo'" '

r, : otl(f)110

05 06=+cq

08 1.o

T=THIcKNESS Or PERFORAIED PIAIE

(14.19a)

Page 269: Process Equipment

6 HIAT TRANSITR IQUIPMINT

SIII'AFE P|ICII ROTATED

T-THICX ESS OF PERFORATED PLATE

SOI'ARE PITCH

2

2oo

uI

1.O

09

o8

o:l

o.6

05

OA

o3

a2

o.l

oo rtlo.2 0:i o4 05 05 oaLGAmENT EFFrcrENcy , - PFd'

SQTJAFE PITCH

Fisure l4.l I (Ref. 3)

Expressing

D

a

Ga

K'

and

r*: li'" 2K'

I4.4 BACKOROUND OT THT ASME DISION TQUATIONS FOR TUBESHETTS 517

C6

6.00

4.00

3.00

2.OO

1.00

0.80

0.600.50

0.40

0.30

0.20

-0.1\

\

0.r0

0.04

0.06

0.05

0.04

0.03

o.o2

o.2 0.3 0.40.s 0.6 0.8 1.0 2.O 3.0 4.0 5.0T/ c^

Triangular pitch

F4.

Figvre 14.12 (Coud6s), ot ihe Amsricon Sociaty of Mechonicol Engineers.)

14.19a becomes

,: of rlZ,,

(l4. r9b)

where /* is obtained from Figs. 14.14 and 14.15.

Example 14.3. Determine the thickness of the tubesheet of Example 14.2using ASME's Eq. 14.l9b.

Page 270: Process Equipment

IAT TTANIIII IOUIPMINT

TlarSOUARE PIrcH

Figure l,l.l3 (Court .y ot rh€ Arn.ricon So<ie, of riG.honicol Engin.er3)

Soluti^oy._ From Fig. 14.4, a : 5.0 and D = 6.0. Hence K, = t.? andq = o.25.From Fig. 14.15,

f+ : o.sz

From Eq. l4.l9b with G - 3.0,

r = 3.0(0.s2)

= O.2A in.

t tl

I(0.25X17,000)

R = bolt circle

I4.5 THEORETICAT ANATYSIS OF FIXCD TUBESHEETS 519

t 66 (,) FfiF (2AAeA /I*AE /ile\ \ er=6o"\7

TRIANGUTARPlTCH

(.Ya K: bA

Fisur. l,l,l/a Fis'rra l,(.15(Court sy of th6 Am6ricon Soci€ty oI ntechoni.ol Enginsers.)

I4.5 THEORETICAT ANATYSIS OF FIXED TUBESHEETS

The shess analysis of fixed tubesheets in heat exchangers is very complex dueto the large number of variables that affect the analysis such as difference in tubeand shell strain, the ratio of shell and tubeshe€t stiffnesses, effective appliedpressure, and relative thermal expansion of shell and tubes. The development ofthe simplified TEMA design equations for determining fixed tubesheet tlicknessis based parfly on the theoretical work done by Gardnel'5 and Miller.6 From Eq.7.9 the differential equation for the bending of circular plate is given by

(r4.20a)

The next s€ction shows that in a fixed tubesheet the quantity q, which is thelocal pressure at radius r, is not a constant. Rather it is a function oftll given by

Q:Cz'rKlm-2w)where g: local pressure

C2 = constant

Kr = tube bundle stiffness = Nt(d!;-t)Er

SOUARLP]TCH

ROIATTD SOUARIP TCH

I d [,d lt d (.a\ll =

gr drl'drlr dr\ dr/l) D

;; \,

Fis'rra l,(.15

Page 271: Process Equipment

!20 HIAT IRANSFIR TQUIPMENT

L : lcngth ol tubcs

4 : outside diameter of tube

r = thickness of tube wall

,,? = distance tubesheet edges move with respect to each other.}1, = deflection of tubesheet

Equation 14.20a can be written for perforated tubesheets subjected to 4 pressure

*ffi*2,'fi-*#*,ff**oo=owhere

, = (4\*\D *,/

(r) = Br

and

(r4.20b)

(14.20c)

(14.zod)

", :

ft {1", . (*)'r-,1 -,f,,<,t - (*1,*111(14.20e)

whcre the Z functions are as defined in Chapter 7 and C and II are consranm tobe det^ermined from the boundary condidons.Definrng P as the average pressure acdng on the fubesheet, its total value is

p* = E*7312(l - p*21

This equation can be solved in terms of Bessel functions. For symmetnc loads,the solution can be taken as

q=C2[27@)+HZ2@)]

. = ffiV,<ol - Z1@) + HLzze) - z+(x)l|

e=ffifzX,l+Hz!(x)l

, = # I" *o * = r,z&)lt - rffi] (14.21)

I4.5 THIORTTICAL ANATYSIS OT FIXTD TUSESHEETS

l'he valuc ol C2 can then be deternlinctl liorn this cqualittn as

521

Now define

Q" = FqP

where qo : local pressure at radius a.Then from Eqs. 14.20b and 14.21,

a,: "f-----"----=tt-lfzzi,,rfr - r'#ll

Z,(x.) ,,h6) - "

_ BD* zl(x") + Hzte")\14.25)

zl(x)

ZL@.)

(14.26')

The value of 11 is based on the edge condition of the tubesheet. For fixed

tubesheet, 4 : 0 and Eq. 14.26 gives

f rr-,r\ I | (l- ttt Ilzz6.) + vzltr;l - alz'G) -::------r!'zt9a)lL-- x4 I L xa I

,=-t#Similarly, for simply supported tubesheet M" : O and E9. 14.25 becomes

.. [zzb) + l0 - ttt/x"Vt,- r\, = -\ffi] "t simply supported hrhesheets

04.28\

\t4.22)

(14.23)

(r4.24)

(14.27)

and from Eqs. I

H=-

^ x. Zz@.),a =---, 2 zi&"\

4.20e and 14.2Of

1-IJ'-"'' " zl?.)

for fixed tubesheets

M"0"

or

Page 272: Process Equipment

i|IAI IiAII'IIR IQUIPMINT

f1t^u.uiu"n vuluc or',r,,, the H constants can be carculated from Eqs. 14.27 and14.2[1. Constanr C2 c{rn then be determi""d f.o_fi.'il.;j.",i"i? *a C, ar"known, the -magnitude

of the benolng moment at any rocation in the tubesheetis obtained from F4. l4.2oe. The maximum uAu" oi tf,l.M. ui url g,u"n ,. ,,obtained from 84. l4.ZOe and normally "*p."r."a

u, ---- "" *'*t

M^ = pazF^

where fi is obrained from Fis. 14.16.The maximum bending str6ss is

(14.29)

(14.30)" =T (1)'"

For large values of -r, the Z val.uls can be approximated by those gtven inTable 7.1 and rhe quantities Fo and F^."n u" "ili..r"J ^i "' "'"

IF = 7{l + t/-X.l for fixed tubesheets

t/i (14.3 t)F^ = =-:IX"

and

F : ;O + 2\/-2x) for simply supported tubesheets

-,-n/4 (14.32)F-''' 2x"

Example 14.4. Determine the stoess at the edge of a fixed tubesheet of thick_ness ? = 0.50 in. if the eeometry L u, ,to*n? n!:'il;;?: = 52,800lb/in.3. E* = 9 x 106 psr, p* =-0..1. -a p = icrii-pri.

Solution

D.=q;#H#=103,020

o = (^\r'_ /2 x 52.800\o,s"-\o-) -\ ro3"oro-/ =I'0062

xa: 9(6) = 6.037

1234567A9

Fieur€ 14.16

I"rom Fig. 14.16, F. = 0.059 and T : 0.25. From Eq. 14.30,

": ,+P(ort)ro o'nr

a : 20,390 psi I

I4.6 TEMA FIXED TUBESHEET DESIGN

Development of the TEMA simplified equations are based on Eq. 14.23 and cangenerdly$e<fi.r'idedinto.thraseparateieps-..The first is determining an equiv-alent local pressure on any given tube. The second step is establishing anequivalent general pressure on an equivalent tubesheet. The third is incorpo-rating the first two steps into the differential equation of the tubesheet that isconsidered as a plate on elastic foundation. These three steps discussed in thenext three sections are based on th work of Gardner. ? The notations used are thesame as those given by TEMA.I

I4.6.1. locol Equivoleni Pressure

One of the main assumptions made by TEMA in the analysis of tubesheets is thatthe tubes are uniformly distributed tbroughout the tubesheet. Referring to Fig.

Page 273: Process Equipment

524 HIAT TNANS;ER IOUIPI,ITNT

14.17, it is seen that the total tbrce 4 in one tube due to a tubeside pressure liacting on the face of the tubesheet iS dxpressed as

o = rl# - r(d' i "D'z1 = r#1, - i(+n

n = nAf' (14.33)

where A = ra2/Na : inside radius of tubesheet

4 = outside diameter of tubes

4 = force in tube due to pressure ,q acdng on face of tubesheet

Actual Contiguration

Equlvalent Confl gurafl onFieuf.e 11.17

'ti_il ||ttttli Ps

wrl

14.6 TTMA FIXED TUBESHITT DESION

tt /d. - ztYr,:r-Z\ " /

N : number of tubes

4 : tubeside pressure

t = thickness of tube

Similarly, the total force 4 in one tube due to shellside pressure P, is expressed

o:*l#-ry1=*+l'-i(*il4: nAf, (14.34)

where [ = force in tube due to pressure P, acting on face of tubesheet

4 : shellside pressure

Besides forces 4 and 4 a third force F" also acts on the tubes of Fig. 14.3 that

is caused by such factors as thermal stresses, restraint due to other tubesheet, orother unbalanced forces in the heat exchanger. This force is expressed as

F*= nt(d. - t)on ( r4.3s)

where F- : tube force

or = longitudinal stress in tubes

The total summation of Eqs. 14.33,14-34, and 14.35 is equal to an assumed

equivalent force q acting on an equivalent tubesheet of radius r. Hence,

4na2 = E- n+ F*N

or

s=@f,-u)+\u,-ttot,

The axial stress dr in F4. 14 -37 can be written as

,,=!,6,- u,,",)

(14.36\

(t4.37)

( 14.38)

Page 274: Process Equipment

iIiIO HIAT TRANSIIR IOUIPMINT

whcrc Ii, [x)dulus ol.clasticity ol.tubcs€i = longitudinal strain of tubes

pr : poisson's ratio of tubes

oc, = clrcumferential stress of tube

a1, = longitudinal stress of tube

The circumferential shess due to 4 and i can be expressed by

"'=(#),'(*)-Thus Eq. 14.38 becomes

oh: E,eh. "[(#), - (*)-]

T"^I1r",9t * * Eq. 14.39 can be.obtained lrom Fig. 14.18. The strain of atube at a distance r from the centerline .r ,r,. r,."i i_ir,_g". i,j*L*"o

",a,=a-!t-L-o,r,

(r4.39)

(14.40)

Figur6 14.18 (14.4s)

I4.6 TEMA FIXTD TUBESHTET DCSIGN

wlrcrc L : length of tube

w : deflection of tubesheet

c, : coefficient of thermal expansion of tube

AI, = "1tunt"

in tube length

0r : temperature change in tube

suhstituting Eq. 14.40 into 14.39 gives

q: @t- P,n ++(d.- rl"(Y- ",4]. "l(ry)'-(*)-l

(r4.41)

lluation 14.41 has three unknown quantities: q, w, and LL..

14.6.2 Generol Equivolent Pressure

'l he total longitudinal force W1 in the bonnet due to tubeside pressure f is shownin Fig. 14.19 and is expressed as

Wn : ta'P, (14.42)

where W1 = longitudinal force in bonnet.

If the tubesheet is assumed as an equivalent solid plate subjected to a general

cquivalent pressure P, then the total load on the tubesheet is

Wp = ra'P (r4.43)

where P = general equivalent pressure

Wo = total load on tubesheet due to pressure P

Because W|, is not necessarily equal to w', the unbalanced force transmittedthrough the shell is

W: 1ra'(n - P) (14.44)

where ll{ = unbalanced force on tubesheet.The longitudinal shess in the shell can be expressed as

wnt!(Do - ts)

Page 275: Process Equipment

where D, - outside diameter of shell

r" = thickness of shell

ob = longitudinal stress in shell

and the longitudinal snain is given by

,*=!6r- 1",o*'1

where d, : modulus of elasticity of shell

e6 = longitudinal sfrain of.shell

tr " = Iroisson's ratio of shell

o" : circumferential sness of shell

(r4.46)

FigurE l,t.l9

.,.,6r$g.t,.rr:t,r^tr1rtii4t;ti.

14.6 ilMA flxlD luBllllllr DttloN lt9

Flnally, the value of €,r can be written as

+ = ^! - ",e, (4,47)

whcre d" : coefficient of thermal expansion in shell

AZ, = change in shell lengtrh

4 = temPerature change in shell

And the value of 4", is

ot=*o.m-ee;ln (14.49)

Equation 14.49 has two unknowns, Atr" and P. It is also based on Eq' 14.47

which does not take into consideration the strain due to an expansion joint.

When the dhell has an expansion joint, E4. 14.47 must be modified accord-

ingly. In Fig. 14.20a the expansionjoint can be approximated as shown. The flatplite aD in Fig. 14.?-Ob is assumed fixed at points a and b' The total deflection

of the shell is given by

Substituting Eqs. 14.44, 14.46, 14.47 , and 14.48 into Eq. 14.45 gives

LL"= 1" + La"Q * 6

where 6 = deflection of expansion joint.

(14.s0)

The expansion joint deflection 6 can be expressed in terms of two components

as

*,=o#*

a": {rw

+ w,"l

(14.48)

(14.51)6=t"+6,

where 6. : deflection due to mechanical load

6p = deflection due to pressure load

Furthermore, the deflection due to mechanical load 6, can be written as

(14.52)

Page 276: Process Equipment

Figur. I ,1.2O

where 51 : spring constant of expansion joint

l7r, = load on shell from expansion joint= 1rt,(D" - t,)P"

Substituting Eqs. 14.45, 14.46,14.51, and 14.52 flta 14.50 gives

L!"= w -t&- t/ ^\L - E"r,t,@;4--il* 4,4 +E(r + X)W + wF) (r4.s3)

*..Tf:ilTl5^l1l:.f 9: gy,iq g/6" can be derived from Fig. r4.2r byassumrng me expansionjoint to be subjested to the forces shown. Thi deflectionoue Io priessurc torce Woy end forceW" + Wpj + Wo", and end moment M0 can beobtained from stucturii analvsis as

,.n.rnier'_lrti,iirllilrw, ]lt

14,6 TIMA ftXNO TUBrSl{ilT DllION tOl

Fisur. 14.21

- lMol"2 EIr

(r4.54)s =Lyra-!(w+w+wet)t32n 8 EIi 3 EjIi

Similarly, the slope is

(14.55)

where D; : outside diamet€r of expansion joint as defined in Fig. 14.19

Ei = modulus of elasticity of expansion joint

/i = mornent of inertia of expansion joint= 4,24(Dt + D)tj

I - lengtlt of expansion joint

n : number of convolutions in expansion joint

4 = thickness of bxpansion joint

l7e; = pressure force in expansion joint

=4tp?- o?tp.4'-

Letting 0 : 0 and substituting Eq. 14.54 into 14.55 gives

e :!w,il2 -L(w+w" +w)lz +MoI"' 6 EiL 2 EiIi Ey'i

u=ffi,w+w^rfr+#@l

Page 277: Process Equipment

Conpulng thlr oquatlon wlth thc last tom of Eq. 14.53 shows that

('.*) =r+---at-Equation 14.54 has two unknowns,l, and P. It is also idontical to Eq' 14.49

lor hcat exchangers without expansion joints, that is, for Si '-+ o.

14.6.3 Relstionship Between Locol ond Equivolent Pregsure

Tho TEMA design equation for fixed tubesheets is based on F4s. 14.23,14.41,rnd 14.49. At r : 4 it is assumed that the quantity 2w in Eq. 14.41 is negligible.

Substituting Eq. 14.23 into Eq. 14.41 and equating the latter with Eq. 14.49

. tlsult,in the following expression:

P=Pr'-P!+Pa (14.60)

and

(14.56)

(r4.57)

(14.58)

2nl3IISj r2Ey'i

^ 968,L,); = "' 2n(D1 - D")3

.t:ii:tflTri HL r4'4' 14'48' 14 sc and the expressions ror w* afr woi

+=ffi_w*,,,"*

$1",<n - P) + rt"(Do - ,sa + [<o? - Dhp"]

This equation can be simplifed by letting

Ir+"@"-t"t*t"1LZ4JHence,

LL' a2.-:_ =L E"tn(D. - t,\

frc - "l1 * <4 - oztn 1r -L-' 8"t-\t -

/t \ p*|.i-t/r-**a

IJ

1) - #r(D" - 2t)(D. -

PPi =

-t + xrolr + 0.,UK(l.s +/)l

,JP,]

(r4.se)t,(D. - t) h(D.-2 z (D"-3t",

": :T*n{o.*lrsp* I + r(r.5 +/r]

_(:)(j#)1,.,ffi])o _ un,r, (o--rt'fu!__g!f\'- 1p"- a\ u )\-r +.nq /.. E,t,(D" - t)n=Effi@"

1s

Fe:0.2s+ tr - o.ol1e%&(ql]'A

E = modulus of elasticity of tubesheet material

The values P,', P:, P:, Pi can be simplified by letting

d"-t . d.-tr .......:- - ld-2t - d,

D"-t"-tu:G D"'2t"-2a=G

Page 278: Process Equipment

.,--_-_.*@"*,1r7@qrr'!l[t|ttEr|Eu|'mnr1*

Honco,

U =ffi;n + o.dr(r.s +nl

"' =t*4{o'*Irr's + K(1'5 +Dr (+)('"5)t,,-(#+)(w\

3:Httf "ti..L.iftrlate

the stress in the tubesheet of the heat exchanger

E : n x ld psi for tubesheet material and shelld" = 0.5 x 10-6 in./in."FIength of tubes = 144 in.thickness of tubes = 0.065 fu.f

.= !,ZS (assurne a simply supported plare)

tubeside plessule = 75 psiconcruTent shellside pressure = 15 osiE, = 30 x 106 psid, = 6.5 x 10-6 in./in.gFoperating temperature of shell = l87Toperating tempexature of tubes = ll9?ambient temperature : 70.F

Solution. From Eq. 14.57 of

tt = f;1n + 36xo.2sf = o.l6e8 in.a

a _ O6)Q7 x 106X0.1698)"i -

-@Xlxl?l)47=6t-- = 165,300 lb/in.

j =, * s(ry?E#H:1]q = 32 85

J = 0.0304

OI

= 0.8750

,,,r..sr.tRtitrrttll]]]{{44e1

14.6 TIMA llxlD TUllSHllT DllloN ctt

rrzo-*borueeson'lt"tnntout-lR pttct-t.

(b)

tigor'11.22

From Se.tion 14.6.3

K: Q7 x rO\(O.2s)(36 - 0.25)(27 x 101(0.06s)(0.75 - 0.06s)

= 2N.73

0.75 - 2 x 0.065

35.5

Fq = o 2s + (, 2s _, .,|#_qa#ft#% (#;l]'"Fq : l '8752

and from Section 14.6.1

t:t-i(*, 1rr2o I=l- ,l+\

: 0.9146

Page 279: Process Equipment

!36 HIAT TRANSfTN IQUIPMfNT

llcncc,

1 + (0.0304x200.73)(1.s7 s'

= nTarr<s.trst - 0.36s0)

= 6.57

1 + (0.0304X200. 73)(1.87 s'x [1 + 0.4(0.0304)(200.73)(l.s + 0.9146'

/f,= _ 16 RO?7r

12.4428.- ""' ': 41.55

15

t {o.oro.orooltr.

s + 200.73(1.5+ 0.s75)l

= 1.48

From Eq. 14.58

From Eq. 14.I

_ rr.0 - 9.0304)/ot,; ll r,).I\ 2 /\ 3s.52 lJ

l5

x [9.5 x 10 6(187 - 70) - (6.5 x 10-6)(119 _ 70)12.4428

P=41.55-6.57+1.48= 36.46

. F2G2 P47"

(1.2r2Q5.r24

t

36.46

: 8686 psi OK

NOMENCTATURE

I4.7 EXPANSION JOINTS

'fhe two most common types of expansion joints are the flanged-and-flued andthe bellows, shown in Fig. 14.23. The flanged-and-flued expansion joints areused where the deflection between the tubes and the shell is not very large. Themost frequently used method of analysis is that of Kopp and Sayre.E It treats thejoint as an equivalent rectangular structural frame with some modifications toaccount for the inside and outside radii. Many experimental investigations havebeen performed to verify Kopp and Sayre's method. The results have shown thattbr most applications this method is satisfactory.

Bellows are used for large deformations of the shell. The analysis based ona NASA researche is similar to that of Kopp and Sayre in that the bellows aretreated as a structural frame with hoop stresses resisted by rings or equivalentplate-and-shell segments of the bellows. A frequently used standard in theunited states is that of EJMA.I0

NOMENCTATURE

a = radius of tubesheet

b = G/2: outside diameier of tube

: modulus of elasticity of shell

: modulus of elasticity of tube

= diameter of tubesheet

/r'\Itll7-) \:r-=

FLANOED 1I FLUED EXPANSION JOIN'I

n.lnnilil||tl

___-/uuu\F._______l-.-------1EELLOWS EXPANSION JOINT

Fisur€ 1,t.23

D.F

E,r

G

Page 280: Process Equipment

530 HIAI TRANSTTR IQUIP/IITNI

/I, i: poisroo's r.ittio ol tubcshcct ntatcrial

/r* : poisson's ratio of perforated plate

o = allowable bending stress

K' = b/a

M, = radial bending moment in a tubesheet

Mr = tangentizl bending moment in a tubesheet

N : number of tubes

P = pressure

P, = shell side pressure

4 = tubeside pressure

p = rube pitch

g : local pressure

J = ASME allowable tensile stess

Z = thickness of tubesheet

t = thickness

t" = thickness of shell

t, = thickness of tube

a" = coefficient of thermal expansion of shell

a, = coefficient of thermal expansion of tubes

n =(p-d)/d.

REFERENCES

Standads of Tubular Erchonper Manufecturers Association,6th ed., Tubular ExchangerManufacuers Associarion. Niw york, 1978.Gardner, K. A., "Hear-Exchanser Tube-she€t D€sign_3. U_Tube and Bayonet_Tube Sheers,..Jourrnl ol Applied Meclranics, American Soc",y lf ,r4""_-Lat"*'i1r".", ,'S#:O'Donrell, W. J., and T. Slot, ..Effective

Elastic Constants fo. Thiciperforatea plates wrttrSquares and Triangular penet ation panerns,.. A S!4! J*r;i ;I ;;;;;;;Ir'#"r'l*^o",Noverbber 197t. American Society of Mechanical Ensineers.

9**, I A., ..Heat Exchanger Tube_Sheer Design.,. Journal of Apptied Mechanics,Amencar Society of Mechanical Engineers, Decembei tgag

Gatdner. K. A.. "Heat Exchanser Tube-Sheet Design_2 Fixed Ttbe Sheets,,, Jounat ofApplied Mechanics, American s;iety of Mechani.je nginee.., i;;; trr."' "-

BIBLIOGRAPHY 539

(r. Milfcr, K. A. G., "fhc Dcsign of l'ubc Pla(cs in Hc.rl Exchrngcrs," in l'r(!$ut? V(tii,l MlP4ing Design Colletted Pape^ 1927 1959, Amcrican Socicty ol Mcchanical lirgirrccrs,1960, p. 6'72.

7, Mcmo from G- P. Byme, Jr., Secretary ofthe Tubular Exchanger Manufacturcrs Associatk)nto Members of the Technical Commiftee, dated January 3, 1964 regarding Standards Back-ground Data prepared by Karl Gardner.

8. Kopp, S. and M. F. Sayre, "Expansion Joints fo. Heat Exchangers," Contributed by the HeatTransfer Division and presented at the Annual Meeting of the American Society of Mechan-ical Engitreers, New York, November 27th, 1950.

't. Analysis of Stresses in Bellorrs, Design Criteria and Test Resubs, Part l, Atomics Inter-national Repon NAA-SR-4527.

10, Standads of the Exponsion Joint Manufacturers Association,4th ed., Expansion JointManufacturers Association, New York, l9?5.

BIBTIOGRAPHY

Rubin, F. L., "What's lhe Difference Between TEMA Exchatrger Cl^sses,"? Hydroca/bon Prc-ce$in8, June 1980.

Rubin, F. L. and N. R. Gainsboro, "Latest TEMA Standards for Shell-and-Tube Exchangers,"Chemical Engineering, September 24, 1979.

Yokell, S., "Heat-Exchanger Tube-to-Tubesheet Connections," Cr"nical Engineering, Feh aty8, 1982.

Page 281: Process Equipment

A thick-woll loyercd vsss€t (Courres), of rhe Nooter corpororion, Sr. touis.)

540 ot = P'

CHAPTER t5VESSELS FOR HIGH

PRESSURES

I5.I BASIC EQUATIONS

This chapter presents some design aspects of solid and layered vessels withpressures in the range of 10,000 to 100,000 psi and higher. In these highpressures prestressing, or autofrettaging, becomes an important consideration inthe design.

It was shown in Eq. 8.1 that

t=. PR. ,,,

sE - 0.6P

is the design equation for vessel shells. As the quantity (,SE - 0.6P) approacheszero, the thickness approaches infinity. In other words, as the pressure increases,the allowable stress of the shell material must be increased higher than 607o ofthe design pressure for the equation to be valid. This increase in allowable stressrequires materials of high tensile and yield properties. The limitations ofEq. 8.1for high pressures are usually overcome by using a different equation that isbased on the theory of plasticity as discussed later in this chapter.

Equation 8. 1 is shown in Fig. 5.6 as being very similar to Lame's Eq. 5.9 forthick vessels. Disregarding extemal pressures, Eqs. 5.9 and 5.10 become

/ ,2\o,=P'lt-41\ r-l

(1s.1)

541

Page 282: Process Equipment

512 vt33!13 foR HtoH PRtssulEs

whcrc

* = \!t<r, - oz)2 * (sz - o), * (o3 - c1)21 (1s.2)

.L

Figu.e 15.t

/,?\P' = Pl ,!! "l\r; - rfl

. The shess distribution given by Eq. l5.l is shown in Fig. 15. 1 for a vesselwith rJ 11 = 2.2. The max-imum stress is in the hoop direction and is at the innersurface where r = ri. As the pressure is increased, the stesses increase untilthey reach a maximum limiting stress where rainre is assumJ ti oc-cur. r,o. trrinvessels the ASME Code assrirnes that failure occurs *f,"oG-ii"ra poin, l,reached. This failure criterion is conveni*t *a t

""lf"i tir"'rni*iriut pnocipatsfess tleory. In thick vessels the crirerion usually ;p;Iil f;;;i" mareriatsis the energy of dislortion theory. This trr""q, .lt"Jil;i tl,;lrrii.o" ""uor, ",TI,I)oi", in a body under any

-combination of sfesses begins only when the

^s:11 *oCy .I

Sstorrion per unit volume absorbed at trrefiiit is Squar to tfrestain energy of distortion absorbed per unit volume at any poi* in u i* .,r"rr"Oto the elastic limit under a state of.umaxral stress as occurs in a simple t€nsiontest. The equation that expresses this theory i, giu"n iV-- "'* """,

r5.2 PRESTRESSTNG Ot WAU"S

whcre W = strain energy

t, : poisson's ratio

E = modulus of elasticity

or, cz, 03 : principal shess

F-or a bar stressed to the elastic limit in simple tension, 02: a3 : 0 and the

cncrgy of distortion expression becomes

0 I u\olw:--6-lror a pressure vessel with the tbree principal stresses given by Eq. 15.1, thecnergy of distortion expression is

/t + p\",f ,'; .f1tY= \- l \r;- ri/ \r/Itecause Ws, : l4lr, the maximum pressure at which yield is assumed to occur atthe inner surface is given by

'.:($(T)Gl (15.3)

It is interesting to nole that when the axial strain is assumed to be zero, theaxial stress becomes

o1 : p,(21t)

and the maximum pressure given by Eq. 15.3 becomes

(1s.4)

In most applications the difference between Eqs. 15.3 and 15.4 is negligible.

I5.2 PR,ESTRESSING OF SOLID WALL VESSELS

As the pressure in Eq. 15.3 is exceeded, the inner part of the shell becomesplastic, whereas the outer part remains elastic, as illustrated in Fig. 15.2. Thederivation of the relationship between dle elastic and plastic regions is beyond

or\/3

rl - r?f ri , \r - 21t'fl-t/z--l-Ll - 3 I

-o + De), (#

Page 283: Process Equipment

the s9ory of this book. However, it suffices to say that the derivation is basedon plastic analysis of an incompressible ."r"c-i *irl, *." "*i"i'.nn.. rr,"resultant equations are as follows:

Elastic region:

,4 vtt!!t! fot HtoH PnlssuRrs

Plastic region:

Fisurc 15.2

('.!)(t -'4\

(+)H

@)6@e)

(#X'*1*znt)(#J(-' * 4.* znt)

@(5"*z'n!)

(15.5)

(15.6)

*:trfl':H[X ?iween the applied pressure and the elasric-plastic interrace

- 4 - zr,L\f; p/#('

.," o'r"sr'c Rrc,o, 't'

(r5.7)

15.2 PRESTRTSSTNG OF WAU.S 545

wlrrrc or, o,, a1 = hoop, radial, and longitudinal stress, respectively (psi)

or, = yield stress of material (psi)

r, = outside radius of shell (in.)

ri : inside radius of shell (in.)

r = radius at any point in the shell (in.)

p = elastic-plastic interface radius (in.)

lklrution 15.7 may be used to determine the lower bound pressure P* at whichytrl(ling occurs by letting p : 4. Hence

(15.8)

l'his equation gives results very close to those given by Eq. 15.4. Equation 15.7lnn also be used to determine the upper bound pressure P+ at which totalyicfding occurs by letting p = ro. Hence

lnr (15.9)

Itlxnmple 15.1. A pressure vessel with a solid wall has an 4 of 8 in., r, ofl?.6 in., and o,, : 80,000 psi. Plot o6 and o, when P = P* and when P =({).000 psi.

Solution. From Eo. 15.3.

".=#( -1)

e+ _ 80,000 /17.6, - 8'z. V5\ 3'

= 36,650 psi

-2o"\r5

rrnd from Eq. 15.1,

o, = ss+o(r. !g\\ ,,-/

o,=rsno(r -ry)'l'hese two values are shown in Fig. 15.3.

From Eq. 15.7 with P = 60,ffi0 psi and o, :calculation gives p : 11.50 in. Hence from Eq.

)(-''J

80,000 psi, a trial-and-errort5 5

Page 284: Process Equipment

t46 Ytlstt3 foR HtoH PRISSUnES

RaDrus , lNcH

Fisurc 15.3

and from Eq. 15.6

qe=rs.72o(t*!g)\ r'/

o,=rs,72o(t-!g)\ r"/

a,= 46,Do(1.427 + 2rn;3)/-

o; = +e,loo(-o sz: + z rn ;)A plot of these equations is shown in Fig. 15.3.

^. ,1.^.y:-p_t"g i" Fig . I 5 . 3 are significait because they show the redistriburionor the stress pattem as the inner region of the cylinder beco_"a ptu"ti". ato not"the reduction of rhe stress at ttre inner surfactrrrd;;il;;;,i'?iL" ,o"r, u,the elastic-plastic boundary as the pressure i, ln"."u."Ji"yoro ri. f

Example 15.2. plot the circumferential residual stress a, when the auto_frettaging-pressure j: !f-pl: rs r. i, ."o""ic iJr"r, ;i; irlT o, *r,"n uoeslgn pressure of 45,000 psi is applied.

I5,3 I.AYERED VESSEIS 547

Solution. The maximum autofrettaging pressure of 60 ksi is less than fwice thelower bound pressure P*. Accordingly, the stress distribution resulting from apressure drop of 60 ksi is in the elastic fange, as shown in Fig. 15.4. FromEq.t5.1.

"'= -t,*t(rrr, - s.---g-)

P' = - 15,625 psi

oa= -rs,ezs(r .ry)The stress distribution given by this equation is superimposed with that in Fig.15.3 for a6 at P = 60 ksi. The resultant residual stress is shown in Fig. 15.5.

The internal pressure of 45,000 psi gives a stress of

oe: rr.tzo(r.ry)

and the total stress distribution due to this and residual stress is eiven in Fie.15.5.

I5.3 TAYERED VESSETS

Layered vessels were developed in the United States and Germany at about thesame time during World War II. In Germany they were used in ammonia plantsas well as for producing gasoline from coal. In the United States they were usedfor ammonia-synthesis processes for the ultimate production of nitrates. Since

Figlro'15.4

Page 285: Process Equipment

vlssg.s Fon HtoH PRESSURTS

c(

oof

'?iiLi;i*

Wodd War II the technology of building layered vessels has improved substan-tialty..Today layered vesseJi are used ii'",i,ia"i"re" ;i[nfT"."ru." "pp,,""-tions in the penochemical industry

-such as heat exchangers, urea reactors,ammonia conven€rs, autoclaves. and coal gasificati;; ,#il. -

Layered vessels consist of a multitude of layers wrapped tightly around aninner shell to form a pressure-retarnlng envelope, as shown in Fig. 15.6. Thevent hole system is a safety feature incorporateainio ttre iay"iJu"."sel "on.t

o"_hon. It consists of a mulritude of small holes drilled radiity lntoit "

fuy"., _aextending from the ouiermost layer to and including tfr. i'uy", uj1'u""nt to tfr"inner shell. The holes are sized and spaced so that they do not affect thestructural integrity of the vessel. The venting ,yrt"- uJt, u. u'rnonitor ofpotential problems such as erosion and "orrosioritt

at -ay oc"urln ti" inner rt "ttduring the operation of the vesset.

- Layered vessels are constructed by various methods. The difference betweenthese methods is in the thickness of inoiuiaua Uyeri *.ap-piig !.-o""ou.", "nAI:l1ilg-r."ryiqy In^ general, layered-vesset construction can be divided inrothree categories. The first is the colcentric_ or spiral_wrapped method where thelayers.consist of segments welded together in i spiral ;;;;;; fashion to

ItT ft::"guld ftickness, as shown in Fig. 15.6a andb. The second methodis the shrink fit method wherebv layers ."'inOiuiOuutty for_"Jiito "yfmO"r,and shrunk on each other to form thl reguired total ,r,t'L"*'ii]g.'is.orl. rr,"

ItlO to. ft: coil-wrapped method whereby a .rrti"u""r-J""t i. it ip i, *ounOrn a spiral or helical fashion to form a cylinder as in Fig. 15.4:'

od ar P=45Ksl

I5.3 LAYERID VESSTTS

i,:)SBRINK Fr-r (d) ColL WRAP Figure 15.6

The earliest reference to layered vessels was made in the 1951 API-ASME( bde. In later years when the API Standard and the ASME Code were separated,

llre layered-vessel criterion was deleted from both. It was not until Jan'tary 1979

that layered vessels were included in the ASME Code. In establishing the new

llyered-vessel rules, consideration was given to the state of the art as well as the

"iperience and research accumulated by the industry in the past 50 years. An

c l ibrt was also made to provide rules to accommodate all types of known

l:ryered-vessel construction.Today most layered vessels are constructed in accordance with the ASME

('ode, VI[-1, Division 2. The majority of the design equations given in the code

lor solid wall vessels are applicable to layered vessels. For fabrication, the

ASME Code, VI[-1, Division 2, gives additional rules for layered-vessel con-

struction. One criterion for controlling wrapping tightness of layered shells is

rhat the area of any gap between two adjacent layers, as measured from the end

of a shell section, must not exceed the thickness of a layer expressed in square

inches. This is illustrated in Fig. 15.7.Another criterion used occasionally to measure the tightness of layered shells

is limiting the circumferential expansion of the outer layer during hydrostatic

testing to a value not less than one-half that ofan equivalent solid wall thickness'

tlencJ the stress at the outer layer due to internal pressure P as given by Eqs.

5.9 and 5.10 is

2Prlco = --;--"--r;- ri

C,=0Pr?' r;- ri

Page 286: Process Equipment

wtt|tt tot HtoH PR!33UR!3

GAp AREA a=f r,.n

AREA OF GAP < TH ICKNESS tFigurc 15.7

and from Eq. 2.1,

ex pnesseo rN nl

*: |b, - p(o, + o)l

e, = 9.--DP'J' E(rz. - r?)

The circumferential growth can be expressed as

,

=,#ii _ ,*,-Ee=A-Lt n-tr', defined as the mean radius. Then

11 =P--!-2

,.=n"+|and the circumferential growth is given by

e _ t.71rp(Z?.^ - t)2(?R^ + t)SERnt (15.10)

15.3 t/aYIRED VISSILS 55t

'l'hc uctusl measurcd growth must not be less than one-half the value given byl!. r5.10.

A third criterion for determining the maximum permissible gap in layeredrhclls is by relating the gap height to a given shess level. Referring to Fig. 15.8End Eq. 5.12 and assuming the end to be fixed against rotation, it can be shownlhd the gap /, can be related to the bending moment by the expressron

Mo

,F; (15. 11)

(1s.12)

!l u bstituting

into Eq. 15.1l gives

6Mocb = -- .)-

B=

,:d+- O.55ro,h=

E

(b)

Figur6 15.8

Page 287: Process Equipment

5!2 V!!t!ts toR t{toH PRESSURIS

Equati0n 15.12 cannot be used directly becau-se the quantity o, is not readilyknown. This. quantity, however, can be related to un uiio*udr"-Jt "..

uy "ut"u.lating the principal stresses at a layer as

oo: S + pab

a,= -P

ot=tyt+)

where o6, cr., ar = principal stresses

,S = hoop stress

;r, = poisson's ratio

o6 = bending stress due to gap l,p = intemal pressure

The maximum stress intensity is given by

ah=ob+r+p

The maximum stress inrensiry o; is limited by the ASME Code, VIL[, Section2, to 3S,. Or in general terms

oo+]+p<KS^

where K = 3 for indefinite number of cycles.. _Ircases where aa is greater than 35, Lut less than 3rn,S,, the rules of theASME Code, V I, para-sraoh q_rce .q," apiti i"r

" s.pilfr!a""ir"'rr,"_pr"rri"analysis. In this case

(15.13)

(1s.14)

(15.15)

t": *Z

z^\-

^where & = alternating stress as defined in the ASME Code, VIII, and K is

( 15.19)

r 5.3 TAYTRED VESSfl.S 553

llv('I by

1-n / o,.K= I + --:--- - l:i--,?(m - l) \JJ6

wlrcrc m : 3.0 for carbon steel

= 2.0 for low-alloy steel

: 1.7 for austenitic stainless steel

' n: 0.2 for carbon and low-alloy steels

= 0.3 for austenitic stainless steels

( 15. r 6)

S. : allowable stress:

lrluation 15.16 can be expressed in terms of S" by substituting Eq. 15. 15 for o6uxl letting m = 3.0 and n = 0.2, which yields

')

K: -!- ,[!-!t"t'Va-5s.li(luations 15.13 and 15.15 can be expressed as

",o+f,+"=#r.

(1s. r 7)

( 15. 18)

or assuming S = S. and

u:T".' KS^

liquation 15.18 becomes

o6=NS.-+-P

and Eq. 15.12 can be written as

' o'ss/s" fN - 0.5 - :lo= E L J..l

where N = 25"/KS^

: 3 for indefinite number of cycles

Page 288: Process Equipment

vtttttt tot HtoH PnrssuRES

K=-+.,,"[**& = maximum allowable alternating stressS. = allowable stress

E = modulus of elasticity

r = radius where gap is measured

P : design pressure

l::10L" t:.r, . A layered vessel with a 42_in.. inner d.iameter is constructed ofcarbon sleet with E = 29,000.000 psi. D.,.r*in. ,ir" ni"iriorn iito*uor" g"pi:r:*ifff:'' s' = 20,000 psi,i"d th".;i;;"y;;'iiiii'h"

".,,"r 'i

f31#fl' iffi il:IlTr1 of the ASME code, vrr, Fis. 5-r10.r, & =

IK=-:+

: l.2l

^r- 2 x 4o,ooo1.21 x 2O,nO

= 3.31

_ 0.55 x 21 x 20.00029,000,000

= 0.021 in.

_ 0.5 _ 4000 \20,Oo0/

tEquadon 15. 19 determines then"t'"l wh"r. tl,".Jil;ffi;""1TlTYl uulue of anv one gap in a lavered

n"eteo to tar.e uc"u,nui"##;:1""91t rn a given cross secdon' a criterion is

prished by ;;il;;;; ilJ'#:,li1 91,p' tT9 account' rhis can be accom-

st uin i, tr,eo zu--'J""; ilij};T,=fffifj ffif:T,: ..X*nsap. rhe toar

rn gettrng the strain required to close one gap, refer to fig. iJ.S ,1,"r"

x6 + yE: R?

xE+(Yo-a)2=Rtr

and

r5.3 |AYERED VrSSfl.S

Fisur€ 15.9

( irmbining these two equations gives

RZ - R?: a2 - ?aYs

Also from Fig. 15.9

rnd

RyI h= R2 Ia

Ys : ,R1 cos d

Substituting Eqs. 15.21 and 15.22 inoo Eq. 15.20 gives

h(h + 2R.)2(&+h-R'cosc)

'l'he circumferential saain determined from Fig. 15.9 is expressed as

(1s.20)

(15.21)

(ls.22)

(1s.23)

(rs.24)

Substituting

2RzB - 2Rra- ZrRr

t= B- d

c'Rz

asinaR2

Page 289: Process Equipment

The total snain required to close one gap is obtained by substituting Eqs. 15.21and 15.23 into 15.25, which gives

,=fre+4sin-tc

l!6 VttSlt! foR HtoH PRTSSURES

into Lq. 15.24 yields

where

C:

Rr | _, /c sin a\'l q'="'&1"*""'\ & /l ;

A=l- 2+ h/Rl2(l-cosa+h/R)h (2 + h/R)(h/R)4: I rRr 2(l -cos d+h/R)

2(1 + h/R)(r - cos d + h/R) - (2 + h/R)(h/R)

(r5.25)

(rs.26,

A plot of Fq. 15.26 will show that the lines are a linear function of strainversus /r/R1. Hence, the ASME Code, VItr, Division 2, approximated 84. 15.26by the quantity

e = 0.109(2a)3/(1

or in terms of Fig. 15.7 terminology

. < 0.r0er4)\/-/

(rs.27)

Equation 15.27 calculates the strain needed to close any given gap. The totalstain required to close all the gaps is determined by summiig all

-the individual

shains given by Eq. 15.27. The hoop stress in a layir due o all accumulated gapstains is approximated by

ue =;l ,)et- lL--

The total hoop stress due to gap shains and intemal pressure can be expressedas

15.3 TAYERED VESSIL3

r1 + -2o, ='rr, _j,P * l* p,-- ) .

The maximum radial stress is given by

o,= -P

Hence the maximum stress inlensity is

co,: oo- o.

'1*'1r, + =l----). e + P < NS,ri- ri r- lL--

and

(15.28)

Example 15.4. The following gaps were measured after forming a layered

vessel of 11 = zl0 in. and rz = 55 in.

Gap lrngth Height At Radius

0.008 in.0.005 in.0.010 in.

0.009 in.

Determine if these gaps are acceptable 1f E = 3O x 106 psi, P = 6000 psi'

/, = 0.3, S. = 20,000 psi, and N : 3.

Solutian. Frcm 84. 15.27 ,

.,:o.loefi# =2.33x10-6

., = o.roeff# :2.62 x 1o-6

.,=o.loe*#:3.25x10-6

y.=!d(rs. =)

I 5 in.2 9 in.3 7 in.4 6llr.

43.25 in.43.25 in.

48.50 in.53.00 in.

Page 290: Process Equipment

vlttl|.s foR HtOH PRTSSURtS

s=kw (Is.29)where s = transverse shrintage rn welds

ft = coefficient of transverse shrinkase

w = width of seam weld

- Refe'ing to Fig. 15.10, the total radiar deflection due to transverse shrinkageot a number of seams in one layer rs

(15.30),ns

2twhere d = radial deflection

n = number of welded seams in a layer

Weld shrinkage decreases the diameter- of a welded layer. This causes apressure between the welded laver

"ompatibitity equai;;'ffi; ;?::;:"trh€ ravers undemeath it' rhe deflection

eo = 9 1"^ 6(o o09tUYJJII = 2. l0 x tO-o

rotal€=10.30x10,6

From Eq. 15.28,

| - u2/ ,.?D \-;t ("t - f+,) = rr,. *-,r,- (, x 2o.ooo - H#)= 1O.47 x 10-6

Because total e is less than 10.47 x 1g-d, gaps are safisfactory. f

I5.4 PRESTRESSING OF IAYERED VESSETS

fn tfe gniral or concentric method,of fabrication, the transverse weld shrinkagem me rongitudinat seams causes prestressing .f ,h. ;;r;;i6#: Such weldsnnnkage is influenced bv manv t

r,.ut input, unJ niiiiil;"',ffiI ff:"iffilr:'"X.ll,ii,X#ill1ffi:J.T ;i

d-dt=4"( 15.31) Fisure 15.10

I5.4 PRESTRESSING OF LAYTRED VESSII.S 559

whcrc r/, : radial dellection of layer l, shown in Fig. 15.7, duc to intcrlaccpressure ffa1

d. = radial deflection of all layers beneath layer i due to interlaccpressure fl11

Substituting Eq. 15.30 into Eq. 15.31 gives

'l'he deflection of layer i and all layers beneath I due to pressure 4+r can beolrtained from Eq. 5.8 by substituting ar = 0 and disregarding the term p'z. Thecxpressions for the deflection, using the terminology of Fig. 15.10, becomes

NSa.-4,: Z

, - 4*'R,*, /Ri*r + ni - n.\E \Rl+,-rR? "-l, 4*rRi*r /Ri,r * tRi., , ^ ,\o'= r \n,t,-ni-,-"''/

^ nsE (Ri. | - RiXR:-2 - Rr'?- r),i-,: 4.IrRr-j

____lRL _ R?)

'lhe stress in layer i can be expressed as

.4*tRi*to': ---J

( 1s.32)

/15 ?1\

(1s.34)

(1s.35)

(15.36)

Substituting Eqs. 15.33 and 15.34 into Eq. 15.32 and reanangingyields

Page 291: Process Equipment

560 vt3$tE toR t{toH PRtssuR[s

Substituting Eqs. 15.29 antl 15.35 into Eq. t5.36 gives

nkwE (RIt - 4.iR!*z - R!.)o' = v'nR'n-' lRi'z - Ri)

Stress in the layers below I due to welding i is

-i.,,Ri*r /. R?\"'= il:;r-1t *;,7

Stress in any layer due to welding other layers around it is

,,= -(t * {\ r !-,Ri,.- \ x'/ 1R?,,-nlSubstituting Eqs. 15.29 and 15.35 inio Eq. 15.3g resulrs in

(rs.37)

(r5.38)

(1s.39)

(15.40)

(15.41)

Equations 15.37 and 15.39 are necessary to determine the precompressivesress in a layered vessel due to wrapping Uy *,"

"on""oG" oiri-ira.etnoA offabrication.

In the shrink fit rnethod, the orecompression equations are the same as Eqs.15.37 and 15.39 except that the'qaanniy n*w/2iir"pfuJJy-Jrn. n"*"

, ='#,' r' ra,(i!'!Liul

*r,

"'::!f('\.#) + ry#::t

.. In the coil-wrapped method, the initial stress in the outer layer i is known.Hence the applied pressure for Eq. 15.lg is

n-r=#and the total sbess in the outer layer is

oi= o" Figur€ 15.l I

I5,4 PRISTRCSSINO OF TAYERED VTSSEIS !6I

und the stress in inner layers is given by

/- R?\ - 4*rR?-'* = -\t **) 4 Ril:EItxample 15.5. Determine the wrapping stress in the-vessel shown in Fig'

l5.11lf n =2,k=o.1',8= 30 x 106 psi, w = 0'375 in'

Solution. From Eq. 15.37, stress in layer one due to wrapping of layer one is

= 8733 psi

Stress in layer two due to wrapping of layer two is

2.25 x tO6 (21'z - 2r\(21.52 - 21'z\or:4igffi@= 11,365 psi

Stress in layer three due to wrapping of layer three is

2.25 x tO6 (2t.52 - 202\(222 - 2l.5'z1ot = 4o(o.s)er.sf

= 12,487 ps|

Page 292: Process Equipment

362 vt33!ts Fon HtoH PRESSURIS

From Eq. 15.39, stress in inner shell due to wrapping all three layers is

o,, = :??l l_]ou (, . #) (ffir- 21.52 - 212 , 22, _ 21.52 \- 2tetF=6\* n6=65)-(179,049)(1.97s)(0.0247 + 0.0163 + 0.0120)

-18,737 psi

Stress in layer one due to wrapping layers two and three is

/ lnz \d' = -17e,04e(l * ffis,)to.otos + 0.0t20)

: -9774 psi

Stress in layer two due to wrapping layer three is

o,= -tls,rNs(t + ff)ollllt: _4052 psi

Total stress in inner shell : -1g,737 psiTotal stess in layer one = g733 - 9744 = _1041 osiTotal stress in layer two = I I ,365 - 4052 = 7313 osiTotal srress in layer three = 12.4g7 psi f

NOMENCTATURE

ITtlD = tr-T,E = modulus of elasticity

e = circumferential growth

h = gap

K = weld shrinkage

Mo = longitudinal bending rnoment

n = number of seams in a layer

P = pressure

SIBTIOO[APHY

l{ = inside radius as defined by ASME

llm : mean radius

r = radius

rr = inside radius

r,, = outside radius

J = shess

,1. : allowable sfress given in ASME

t : thickness

w = width of weld seam

rr = coefficient of thermal expansion

pn

A.r

c

p

I

.,1

(fr

(ft

(f,

U0

= change in temperature

= strain

= proisson's ratio

: radius at interface between elastic and plastic zones

: bending stress

: stess at layer i

= longitudinal seess

= radial stress

: stress at layer .r

: yield stress

= hoop shess

BIBTIOGRAPHY

Armstrong, W. P., and M. H. Jawad, "Evaluation of Thermal Conductivity in Layercd Vessels,"ASME Jounal Prcssure Vessel Technology, November 1981.

Brownell, L. W., 8trd E, H. \onnl, Process Equipme t Deiqn, John Wiley, New York, 1959.

Jawad, M. H., "Wrapping Stress and lts Effect on Strenglh of Concentrically Formed Plywalls,"NME Publication 72-pvp-7, Seprcmber l9?2.

Prager, W., andP. G. Hodge, Theory of Perfectb Pkstic Sortrb, John Wiley, l'{e\t York, 1 5.

Page 293: Process Equipment

t6CHAPTER

TALL VESSELS

564

Tollve$el. (Co',rtesy oI rhe Noorer Corpororion, Sr. touj3 Mo.)

565

Page 294: Process Equipment

566 TAtt vtssfl.s

I6.I DESIGN CONSIDERATIONS

Special design considerations are required for tall vessels that are installed in thevertical position. These vessels may utilize support skirts, sffirt nngs, ringgirders, lugs, and other forms of support attachments as describid in Chapter 12.However, the vessel itselfrequires special design considerations in setecting theproper thicknesses and stiffening rings, if neided, to adequately support thevessel and to resist the applied loadings.

. In addition to loadings from intemal and external pressures, tall vessets mustDe capaDle ot.wlthstanding additional loadings from the dead load of the vessel,the

9onte.nt1 inlgmal parts, insulation, piping-, and externA equipment, anA tiom

earthquake loading and wind loading. Thi tall vessel, as we as'most otner typesof vessels, T9y also be subjected to applied forces and morneni, fro- tt errna

expansion of the piping. The niost critical combination of loadings that cause thehighest stresses may not occur when all of the loads are appii.j u? ttr" .a-e ti-e.Certain loads may cause critical stresses during the time of

".""tion of t" u".r"t,

whereas other combinations of loadings ma! cuuse critical stre;ses when thevessel is filled with its contents. The propei design of the veJmay requireexamining several different loading conditions to Jstablish the proper thicknessand other requirements for a safe desien.

Some of the cornbinations of loadirigs requiring careful consideration are:

l. Vessel. installed in place but not operating (no contents, internals, orinsulation) and not under an applied earth{uake or *inJiouotng.

2. Vessel under intemal pressure with contents and other dead loads with orwithout earthquake or wind loading.3. Vessel under external pressure with contents and other dead loads with

or without earthquake or wind loading.

^t;*:::::,b,:l!:y: for a specific vessel, may be a worse combination than any

or me condltons listed above. The designer must be certain that all conditionsaretxamined for determining the controlling condition.

The required thicknesses and other desigi requirements vary somewhat de_pending upon the design theory chosen. Thi .*i-u, ,o".r ,fi.o* is used forIne oeslgn ot most tall vessels. This theory is used in the ASME Code. VI[_I,and the API 620t and 6502 design rules. Tie effects of using other theori"s a.ediscussed later.

The two-external loadings that are important in the design are those due toe:mnquake toadrngs and wind loadings. AJthough the ASME Code, VI[_ | , doesnot specify design methods or design codes th-at are considered, application of*^y: :"lryPt used design ruGs is discussed. nememUer,'ii'ile specincrocauon where tie tall vessel is to be_ installed, as given il the design specifica_tion or purchase order, the design rules may be so-mewhat oimere# tom eitrrer()1 me two rules described here. Local requirements are always considered.

Once the extemal loadings and overtuming moments are determined, they are

16.2 IARTHQUAKI LOADING 567

cornbined with the internal and external pressurcs and any other kradings that arc

lpplicable to the tall vessel. The following sections describe dift'erent methods

lor establishing the forces, moments, and overturning moments from extcrnal

kradings. In addition, methods are given regarding how to combine those load-

ings with other loadings in order to determine the highest stresses and to satisfy

tid-22 of the ASME Code, VI[-1. Included also are methods ofconsidering the

rlynamics effects of the wind loading and wind velocity on vortex shedding and

ovalling vibrations.

I6.2 EARTHQUAKE LOADING

ln the design of tall, vertical vessels, one cause of stresses in the v-essel wall is

lhe overhr;ing moment from the lateral force of an earthquake loading' Al-though most disign standards require vessels to withstand earthquakes, usually

no sfecific applicible rules are given. The purchase order or design specification

,hould list thi applicable code to be used for earthquake design, such as the

ANSI A58.1, "suilaing Code."r the Ilniform Building Code,a ot some otlerapplicable building cod;. Additionally, the location ofthe installation is required

t; ^determine

the appropriate earthquake factor. Figure 16.1 shows a typical

oarthquake "one -up aicording to the Uniform Building Code (UBC)' Earth-

quakj zones given in other building standards may be different. The procedure

lbr determining the lateral earthquake loading is similar in most building stan-

dards and is G same in both the UBC and ANSI standards Some coefficients

in the formulas and the zones on the earthquake zone map may differ in various

standards.For both the UBC and the ANSI standards, the total lateral earthquake force

is calculated by the following formuia:

V : ZIKCSW (16.1)

where Z = coefficient depending upon the earthquake for the location ofinstallation. For ANSI A58. I for zone O' Z = | /8 ' For both the

UBC and the ANSI 458.1, the following apply: for zone 1'

Z = 3 /16 for zone 2, Z : 3/8; for zone 3, Z : 3/4; and forzone 4. Z: 1.0.

Iv = total dead load of vessel and contents above plane being consid-

ered 0b)

I : importance factor; assume I = 1'0 for vessel

K = arrangement factor; assume K : 2.0 for vessel

C : base shear factor = 1/15\/7 = 0.12

? = fundamental period of vibration of the vessel assuming a uni-

formly loaded cantilever beam fixed at the base by the following:

Page 295: Process Equipment

'hdrdhh|'b.dlol

Figuro I 6. I Rirl zorc mop ot rhc Uniied $or€t" (Reproducld tro,n thc Unifrofih Building Code, I 9g2 Edirion,CoPy'iglt 1982, wifi pcrminion oI th. p!bti3h6r, Thc Inr,arnotionot Confera"* J g;tdr;Offt.uL.f

s68

16,2 IARTHOUAKE IOADINO

^ zn t;n"' 3.52 \ EI,s

Substituting I = 386.4 in./sec2 gives

r = o.osos.g.

569

(16.2)

(16.3)

h = sfraight length of shell from tangent to tangent of shell-to-head

lines (in.)

w = W/h = average unit weight of shell (lb/in') of straight shell

length

E = modulus of elasticity of vessel material at design temperature (Psi)

/* = moment of inertia of shell cross section (in.4)

1,: (v/8)(tl + t)3t when (d + t)/t < 20

L = O.Oa9@2 - dt when (d + t)/t > 20 (in.)

r = nominal thickness of shell (in.)

4 = outside diameter of shell (in.)

d = inside diameter of shell (in.)

S = site-sFucture resonance: assume S = 1.5 unless an exact value is

known.

O.l2 < KC s 0.25 for UBC.

O.l2 < KC < O.29 for ANSI, zones 0, l, and 2.

O.l2 = KC < 0.23 for ANSI, zones 3 and 4.

CS < 0.14 for UBC and for ANSI in zones 0, 1, and 2.

CS = 0.11 for ANSI in zones 3 and 4 when.l = 1.5.

KCS need not exceed 0.3.

When KCS = 0.3 is substituted into @. 16.1, the total lateral earthquake

force becomes

V = O.3O Zw (16.4)

When the vessel is rnade from shell sections with different dianieters and

thicknesses, the lateral earthquake force is determined for each cylindrical shell

section above the plane being examined. However, for a cylindrical shell ofuniform diameoer and thickness, the total lateral earthquake force V is distributed

as follows:

Page 296: Process Equipment

570 lAt I vrlslt 3

1. At the.upper head-to-shell tangent line, apply a concentrated horizontalforce determined as follows;

4 = 0.07 TV, except n shall not exceed O.Z5V and Flshall be considered zero for ? = 0.7 or less (f6.5)

- where ? is given in Eq. 16.3 and V is given in Eq. 16.1.2. Along the straight length of shell,

^ (V - hw.h.n,=--;f,

__ For a shell of uniform diameter and thickness, this gives a triangular loaddisnibution with the

_apex pointing downward. fo.

"ul1ufutirg tie momenr,

assume a concentrated loadine of (V _ fl applied at the centroijof the nianglethat is equal to 2/3 tr from the-lower he"j_t,i'rr,"rr arg"riiiJJri Jio*n rn nig.t6.2.Ongg A9 values of d and .{ are determined and the moment arms to therespective forces are known, the overtuming moment is determinel as

(16.6)

(16.7)M": 4(h). n(!^)

Example 16.1. A vertical vessel with a cylindrical shell and hemisphericalheads is installed inside a building in Boston. fhe sheU is i ftlnril aiurn"t"r,0. 5 in. noninal thickness , and 30 h from t"rg"nitl i-t"r,t. ft

" uiJ."r

"ontuio,a fluid at 35- lb/ft3. The purchase order speclfies tf,"t tfi" UsC b" i"llowed forearthquake design. what are the lateral earthquake ro.", ur"a ro. t "

c"rigor

Solwion. The UBC specifies that the total lateral earthquake force is calcu_lated from Eq. 16.1 by the followrng:

v = zIKCSw

Z = earthquake factor depending upon site location. Boston is located inearthquake zone 2

where Z = 3/8

1= 1.0

K=2.0W = total dead load of vessel and contents is

shell weight = n(30.52 - 30\(360)(490/1728): g7gs16

weight of heads = (4/3)n(30.53 _ 3O?)(4gO/ |TZS\: 1630 lb

I6.2 EARTHQUAKETOADINO

fluid in shell = 7r(30F(360)(35 /1728) = 20,620 lb

fluid in heads = (4/3)n(30)3(35 /ltzt1 = 229916

w = total weight : 34,240lb

/r = 360 in.

w = Wlh:34240/360 = 95.1 lb-in.

E:30x106psid+t 60 + 0.5

' U.J

571

-fI

I

I

I

-+Figure 16.2 Eonlquoks lood distribulion on o toll vos!€|.

Page 297: Process Equipment

312 tAtt vrlstts

/, = 9.949161r - = 43,400 in.a

r = 0.0908

- 600)

(95.lx360f(3d-i06x43/00 = o lo06

" =r = 0.2102;maximum is C = 0.12

KC = (2.0)(0.12): 0.24; maximun is r(C = 0.25CS = (0.12)(1.5) = 0.18; maxrmum is CJ = 0.14KCS = (2)(O.M) = 0.28; maximum rCS = 0.3

yis determined by using Eq. t6.l and KCS : 0.2g as follows:

v = (3/s)(t)(0.28)(34,24o) _ 3600 tb

4 = 0 when ? is less than 0.7 (T :0.1006). Therefore, V = 3600 lb and4=0. IExample 16.2. The tall vessel described in Example 16.l is to be supportedat the lower head-to-shell iunction. Dete-rmin" ,fr" i"""".frg'iro-"n, u, *"support line from the lateril earthquake forces.

- -'i-'i''|b 'n

Sotution. previous calculations show that the period of vibration places all of&e horizontal earthquake force to-be applie; ;t;r-""',,#;;i#loaoing. Forthe vessel in Example 16.1, this grves

M" = (3600)(20 x rZ) = 864,000 in.{b IProblems

16.1 What is the total lateral earthquake force using the ANSI A5g.l Code forthe following vessel? A vertiial vess"t *irh ;-;;;l;;.il-o.on"o o, *"lower head. The shell is a seaml"r, pip" *i;h ;_i;: inrialtii.am","., ,.0in. thick,.and 40 ft. long wirh 3_in.-ih'i.k ri;;;J#;. rd"uJrlr"r "ont"tn.gas at ambient temperature. The vesset is instJleJin --.*mqo"k" ,on"4 where Z = l.O.

Answer: Lateral earthquake force is 3910 lb.16.2 Consider the exact same vessel given in problem 16.1. What is &e totallateral earthquake force using tri'" u.ii"""-i",rar"!'C"iJ.ll"r,

Ansu,er: Latel-3l earthquake force is 4970 lb;

16.3 WIND IOADING 573

16.3 What is the equivalent earthquake force in terms of g for the vessel in

Problem 16.1?

Azswer.' Earthquake force is 0.229.

16,4 What is the equivalent earthquake force in terms of g for the vessel in

Problem 16.2?

Answer: Eafihquake force is 0.289.

16.3 WIND TOADING

Two distinctly different kinds of design considerations are generated from wind

Ioading. First, the static force from the wind-loading pressure against the vessel

"our"a'- ou".to-ing moment that must be considered in designing tall vessels

installed in the vertic-al position' The second consideration is the dynamic effect

from vorlex shedding of wind passing arcund the vessel'

16.3.1 Externol Forces from Wind Looding

As with earthquake loading, many different design lnocedures determine the

wind loading and its applica:tion to i vessel. The two most widely used standards

are the ANSI A58.1 Code and the Uniform Building Code'

Although there are differences in tle procedure for determinilg the wind

loads betieen the ANSI A58'1 Code and the Uniform Building code' both

methods use the same rnap for determining the wind velocity at the location site'

as shown in Fig. 16.3 for the Uniform Building Code'

When the ailst A58.1 Code is used, the basic equation for determining the

velocity pressure q, at various heights z is calculated from

q" = 0.OO256 K,(tv)2 (a)

where q, = veloclty pressure (Psf)

1 = importance factor; assume 1 = 1'0

y = design wind velocity (mph) from Fig' 16'3

K, : veloc8 Pressure coefficient

In addition, it is necessary to modify Eq.a by the force coefficient C1' which is

0.6 for a cylinder, and by the gust factor G, for the height of the vessel above

ground bv!I. Once the -basic

wind speed is determined from Fig' 16'3' ttte

ielocity pressure for a cylinder is obtained from Table 16' 1a' To determine the

Page 298: Process Equipment

HN-.r

d6uI|: 9{E ET: FTd -0HE €I5 *,JE 5?=:!> trr5 E +li*i 95E6' FTE::E €FfrE; ; $

=:a sE

9rE I li*EFE -E€Ei=s i:::5 b5A*g gE

: 6rI +'tE !aiE !8g .e:; i-eq -*r." 6d

iE

g !E! g.a? r;i t;

i- F!,!aAq gi

a:- ieE Ii!;rb8iEFI!t: p:gEg

\-,

N*k)

| :F| 'Eil _ir-,| :at

;

*8i'-9 i

tr

574

16.3 WlNo toADlNG 515

Tqble l6'lo velocitv Pressure for cylinder' (q x Q) ucing ANSI A58'l codr'

P"t

Basic Wind Speed (mph) frorn Fig 16'3I r.,:-rr1 alr^i,aI lcight Above(;round (ft) 100 t20110

l,css than 30

30-6060-100

100-140

l40-200

200-300

100-400

7 g 11 13 16 19 23

911 14 17 21 25 29

10 13 16 20 2s 29 34

11 15 rg 23 28 33 39

12 16 20 25 30 36 42

14 18 23 2E 34 41 48

15 20 26 31 38 45 s2

where (g x Cy) is ftom Table 16.1a and G, is ftom Table 16'1b'

for instatlations above ground level, G is based on the total height of shell

and supports. Depending on the total height, there may be several different

tlesign ^wind pr"riu.". f6r different height zones. For {.sig1 purposes, wind

toaoi ure appiieC at the center of each height zone Gee Fig' 16'4)'

Wfren tdi 1982 Ilniform Buitding Code is used for determining the design

wind oressure in the horizontal direction, the basic formula is

tlesign wind pressurep, the velocity pressure is modified by G, from Table 16' 1b

uccordins to

p=(qxc)(G) ( 16.8)

P = C,C"q'l (16.9)

Toble 16.lb Gusl Foclor for €ylinder ot Vorious Heights

Height aboveground (ft)Gust factorHeight aboveground (ft)

Gust factor

50 60 '10 80 90

1.21 1.20 1.19 1.18 1.17

2N 250 300 350 /100

1.11 1.10 1.09 1.08 1.07

15 20 25 30

1.32 1.29 1.27 1.26

100 Dn AO 160

1.16 1.15 1.14 1.13

40

1.23

180

1.12

Page 299: Process Equipment

T t"t wtl .l

Figrrr. 16.,t Wind lood disiriburion on o rollwr!€|.

where p = design wind pressure (psf)

C" = coefficient for combined height, exposure, and gustCq = pressue factor = 0.g for cylinders

4, = wind stagnation pressure at 30-ft level1 = importance factor = 1.0 for pressure vessel

The Uniform Building Code basic. wind speed map is shown in Fig. 16.3. The1"11T

*._dg::rry_p for a cylinder for vari9";r,!r!itz"i", "ilou?

tn" grouoors glven in Table 16.2. Aeain- there may be sevlral aifferent jesign winCpressure Ioads for different-height zones. The height zones for the Uniform

I

I-f

16.3 WIND LOADING 577

Tqblc 16.2 Derign Wind Pressure pfor o Cylinder Uslng the Unlform Bulldlng€odo (psf)

Basic Wind Speed (mph) from Fig. 16.3llcight above(ltound (ft) 120ll0100

lrss than 20

;10-40

40..{0l,{l -10O

t(x) 150

110-200

t(x) 300

){) 400

t2t416

t'7

t920

22

23

l618

20

22

u26

29

30

36

38

44

47

53

56

62

65

20

22

25

n30

32

35

3'l

z)27

31

33

,10

44

30

37

40

45

47

52

55

42.to

53

JO

63

6't'14

't't

Ituilding Code are different from those given in the ANSI standard. A typicalrlistribution of wind loads at various elevations for a tall vessel is shown in Fig.t6.4.

16.3.2 Dynomic Anolysis from Wind Effecfs

When a laminar wind flows by a circular pressure vessel, the air stream or wakebchind the vessel is no longer smooth. There is a region of pressure instabilityin which vortices are shed in a regular pattem. These vorlices cause an alternat-ing force perpendicular to the wind direction that could make the vessel vibrate.When the frequency of the vortex shedding coincides with the natural frequencyol the vessel, a resonance is caused with increasing amplitude. To prevent thiscondition, the natural frequency of the vessel is set higher than the vortexslrcdding frequency determined by the maximum velocity of laminar wind at thevcssel location.5 Resonant wind velocity is related to the heighfto-diameter ratiool a cylindrical vessel, as shown in Fig. 16.5.

The natural frequency of the vessel/, is greater than the frequency of vortexsheddingJ, using the following equations:

If, = i = natural frequency of vessel (cps)

^ o.2vf, = -t; = frequency of vortex shedding (cps)

1 = period of vibration from Eq. 16.3

I{ = maximum velocity of laminar wind or resonantvelocity (fVsec), (see Fig. 16.5)

(16.10)

(16.1 1)

Page 300: Process Equipment

rAu. vlll .l

r60

140

,- 15,106.7

120

110

100

90

;l

;l

a

.8.

3

.sE!

IE

,E

=

12 t4 16 la 20 E--24---iHeight to diameter rario, ltD

Figl|rre t6.5 Relononr wind velocir,, V,, v€rcus H/D.

D = outside diameter of vessel (ft)

In addition to the vorrex sheddins. l" y,:.:.1 is examined for ovalling vrbrationas a dng. The ovalling frequenc-v

frequeniyf, ",i"s;;i;itil;;:,fi#11,f

at least twice the vonei shedding

f' = # = ovalling frequency (cps)

r = nominal thickness of shell (in.)

I{i.l_!.. ,\*.T: ed a stiffening ring within 24 in. ofboth shelt-to_headJunctlons, and additional stiffeninmaxrmum of g0 ft. g nngs are evenly spaced to keep the span a

f,>L

f. > 2f,

(16.12)

(16.13)

(16.14)Example 16.3, A vertical ves1l. m3de with a cylindrical shell and hemi_spherical heads is to be installed our ol doors near Corpus Christi. Texas. The

16.3 W|NO LOADINO

shell is 5 ft.0 in. inside diameter, 1.0 in. nominal wall thickness, and 100 tl.0 in. from tangent to tangent. The contract specification requires the vessel to

be designed according to the Uniform Building Code requirements What are the

ltteral wind forces to be used for design?

Solution, The UBC map shows that Corpus Christi, Texas, is located in a

100-mph wind zone. Therefore, the wind forces at various locations are calcu-

lated usins Table 16.2 as follows:

0-30 ft ri = Qs)(2o)(62/12) = 2,580 lb

20-40 ft Fz = (n)Qo)(62/r2) = 2,790 rb

40-60 ft 4 = ODQO)(62/L2) : 3,200 lb

60-100 ft Fq = (n)@o)(62/12) = 6,820 lb. r0.5)( zrY3l Y(45) -Upper Head- - \r?r,

470 lb

Total 15,860 lb I

Exampte 16,4. What is the overtuming moment due to the lateral wind forces

assuming that the vessel is supported at the lower shell-to-head junction for the

vessel in Example 16.3?

Solution

Load Arm

0-20 ft 2,580 x 10 = 25,800 ft-lb

2040 ft 2,790 x 30 : 83,700 ft-lb4}-ffi ft 3,2N x 50 = 160,000 ft-lb

60-100 ft 6,820 x 80 = 545,600 ftlbUpper head 470 x 101* : 47,470 ft-lb

Mo : 862,570 ft-lb a

Example 16.5. Determine if the vessel described in Example 16.3 is adequate

to resist vortex shedding and ovalling vibration.

Solution

1. Determine the total dead load weight of the vessel:

Shell = z(31'? - 301$200)@90/ 1728) = 65,219 16

Heads = 4/3 r(313 - 3or(49o / 1728) = 3,320 lb

Total weight = w:68,530 lb

i,100 + 0.4 x 2.5 : l0l.

Page 301: Process Equipment

!to.,

rAu. vlll|lt

Dctcrminc these properties:

w 68.530.= n= 1200 = 57.1 lb/in.

E:30xl06psiI = 0.049(62a - 604) = 89,000 in.a

.1

r = 0.0e08. /- (5ZJ.lg?99I_' ""'""Yt:o xloS<as"ooo) =0'6047

I= 0"604? = 1.65 cps

H 000x12)D= ii; = te.3s

V : 40.33 ftlsec

s =0.2V _(0.2)(40.331'" D - --51? = I.56cps

f, > f, 1.65 > 1.56 oK- 683(1)

J. = .o;i = 25.55 cps

f' > 2k 25.55 > 3.12 oK

Problems

16.5 A tall vessel conshucted with a- cylindrical shell and flat closure ends i8to be installed near Denver, Coloiado. Th" ffi;;#;;.or tlre cyfin_drical shell is 8 ft, the nominal *rl.rhi"k;;j, i.6't.l'Joo ,r," ,o"igr,,length from head weld seam b head *aJl""- i, izJ n.-rir" nut t"ua,are 6.0-in. nominal thickness. Wt at is tf,e totA fa*J*ioO io."" u."O fo.design of the vesset fouowing rh" *d;irh";;i;rltili ""a"rAnswer: Lateral wind force = 14,060 lb.

16.6 What is the total lateral wiusing the Uniform Buildinf,%tff;

* the vessel given in hoblem 16'5

Ansu'er: Laterul wind force = 21,100 lb.

16'7 Many_design specifications requirea-minimum design wind speed of r00mph. What is the total lateral^wlnd torce on the vessel in problem 16.5based on a wind speed of 100 mph?

Answer: Lateral wind force = 21,390lb.

I6,4 VESSEI. UNDER INTERNAT PRESSURE ONIY 58I

10.11 lJused on a support line at the lower head, what is the overturning momsntliom the lateral wind force for the vessel in Problem 16.5'l

Answer: Mo = I1,682,400 in.-lb.

10,0 A pressure vessel is 10-ft inside diameier by 2.O-in. thick and 150-ft tall.l)etermine if the vessel design is adequate to resist ovalling vibration.

Answer: Tl:,e design is not adequate because the "f, = 0.11 and

f. : 0.09i consequently, t does not equal or exceed 2f,.

I6.4 VESSET UNDER INTERNAL PRESSURE ONLY

l,or tall vessel under internal pressure only, the primary additional consid-F|rli(nr to the intemal pressure is the effect of fluid pressure head and the dead['rrl. 'lhis is especially important at the bottom of a vessel where the effects mayr rrrubine. The fluid pressure head may occur only during hydrostatic testing oflh{' vcssel or it may be a continuing load occurring during operation ofthe vessel,lh' additional pressure caused by the ffuid head is calculated as follows:

(16.ls)

wlrt lc PJ = additional internal pressure effect from fluid pressure head (psi)

Il = height of fluid column above point (ft)

7 : density of fluid. lb/ftl

|l the fluid head exists in the vessel during operation, the value ofP7is addedt' ' lhe intemal pressure when the minimum required thicknesses are set. At thelr(,ttom of tlte vessel, the stresses and minimum required thickness are set by thetirtrl pressure. It may be possible to decrease the thickness when the fluid headrllcct is decreased in a vessel where a variation in plate thicknesses is accept-rrblc.

If the fluid head exists in the vessel only during the hydrostatic testing, theplirnary membrane stress frorn the combination of the hydrostatic test pressurerrrrtl the fluid head pressure may go as high as the yield strength of the vesselt|r terial at the 0est temperature. However, if the resulting minimum requiredtlrickness from the combination is indicated as more than that thickness requiredlrrr the normal design conditions, substitution of a pneumatic iest or a combina-tion of hydrostatic/pneumatic test should be considered. In general, the min-irnum required thickness of a vessel should never be set by the requirements ofthc hydrostatic head unless it is impossible to test it any other way. Also,rcrnember tJlat a hydrostatic test may use fluids other than water if water causesrr rrroblem such as corrosion.

",=W

Page 302: Process Equipment

..7 TAtl Vt!!!ts

. F'or u vcssel untjcr intcrnal pres

iffi:i;:lJ:,.:ji,# ffi #*'#liilT":lji ;iilliJi,l,,lj, ;ii il.;",l:ll,lWhether the ,t .ir", "uur.J.Un",t-,w

vslrcr uur also lts weight to be consi(pressive sresses a"p""a,

"r# ,ii:e -addttronal.loadings cause tensile or

sKrn tocation. : locatton of the extemal supports or s[

. In th€ actual design, the minincircumrerentiaLsnesi;ffi il #l}1T3ffi:*|"**' is initiallv set by

or=PR_ t (16.1

From the equation in IJG_Z7tct(lter-s or sr', tte 'e;;#;"i:')

of the ASME code, vltr-I, expressed

sE=P(4+o'

where ,S = allowable tensile shess (psi)E = weld joint efficiency (E = I.0 for seamless)P = intemal design pressure (psi)R = inside radius (in.)

t : rninimum required thickness (in.)

Using this equation, a lentative m.circumferential .*;.. Wil;;;"f"rmum

required thickness is set based on thobe necessary ro inci;" d;;f;:litequ.ired thickness is determined, it maypressure. Based

";;;;;;:r ^the-

tluid head.as well as the intemal desigirdetermined f.;; il;;iil#; l"nili,ill"t'""''

the total lonsitudinal stress'is

wrD^t

,PR2t

wnere ot: tatal longitudinal sress (psi)W = total dead load of

examined(rb).rhl,;.h:#X,,:?lf :*;r.TdLJr"""D" = mean diameter of shell (in.) _ 211 * ,

From the equafion in uG_27(c\et.:lg: 1tM-E.-C"de, VI[_ | , with rhe rermsrearranged and the dead load term added, the following equation is grven:

,,=+p(!-o.z)t w\zr / rD^t (16.19)

16.4 VESSCL UNDTR INTTRNAI PRESSURT ONIY 583

lrr hoth Eqs. 16.18 and 16.19, the dead load term may be either tension orq'orrrpression depending upon the plane being examined. In general, above the

rrrpport line, this term is compressive and the total longitudinal stress is the

rllllcrence between the intemal pressure effect and the dead load effect. Whenllris is below the support line, the terms are both tensile. For some arangements,thc condition without inlemal pressure may be more critical than when intemalprcssure is considered.

ll .rr is positive, the actual stress is positive and the allowable stress is

rlctcrmined from the allowable tensile stress tables. If the value of or is negative,

lht: allowable stress is determined by the method that establishes the maximumrrllowable axial compressive stress in a cylindrical shell.

l{xample 16,6. For the vessel described in Example 16.1, determine the totalkngitudinal stress in the cylindrical shell above and below the support line that

lN at the lower shell-to-head junction. The value of SE : 15,000 psi.

,l{rrtttion. Assume the intemal pressure is set by Eq. 16.17 for a value ofJr, = 15,000 psi. Reananging the terms gives

p.= sEt _ (t5,000)(0.5) = )45 nci' R + 0.6r (30) + 0.6(0.5)

'l'he dead load of vessel above the support line is

(r6.1

(16.18)

being

ShellUpper head

9,700815

10,515 lb

'l'he longitudinal stress using Eq. 16.19 is

oL: +Q45)( _n"\ - (lo.sls)"'- I a(60.5X0.5)

30

2x0.5ot: *730O - 110 psi

ot = 7190 psi tension with intemal pressure

ot : ll0 psi compression without internal pressure

'lhe dead load of vessel and contents below the support line is

Lower head 815

Shell fluid 20,620

Head fluid 2,290

23,725 tb

Page 303: Process Equipment

tta TAtt wr!![3

The longitudinal $tress usinS Eq. 16.19 is

/ 30 \ oe:'<roy: + (245)l ;-- - O.2l + \'r'tzr)\z ^u.r / r(60.5X0.5)

a1 : I 73C0 + 250 = 7550 psi tension with intemal pressure

Example l6J. For the vessel described in Example 16. 1, determine the

l"TlT !Trftri".'tainingnuidat35rb/ft t;;*r;ivo'l.,jii'L,r"e,

l(#t. ^r,ff *f **.:: is-nee_ded

lt both the lower sheu-to-head tansenrline^ and at the lowest point of the lower head.

At the lower shell+o_head tanrJZ.s ft. .jent line. rhe fluid height is

Problcms

16.10 What is rhe circumferential syss bgeO_o1_tfre ASME Code, VIII-I, atthe bottom of a tall vessel rh"t contains nuiC at sO tUTdJj an intemaldesign pressure of 400 osi? .The. ,"r."i; ;;:;. "#al'ta_eter uy0.5-in. minimum wan uv +s ft 0 i".;;;;l ,."e,i,, *iii"i_il.

".* n*heads on each end. E = l.U and the vessel is supported at the bottom.

Answer: c6 = 15,200 psi16.11 What is the naximum shess in the shell of the vessel in problem 16.10during a standard hydrostatlc test of 1.5p?

30ft+2.5ft=

For fluid P7 : 7.9 psi

For water e, = GZ.$(Q.D = 14.1 psi

At the bottom of the lower head, the fluid height is 30 ft + 5 ft : 35 ft.

Forfluid P"= (3.5)(35) = e {------ 't (1441 -orPst

For water P, = = 15.2 psi

Answer: o, : 22,700 psi

16.5 VESSEI. UNDER INTCRNAT PRISSUR€ AND EXTERNAI IOADINO 585

16,12 What is the maximum longitudinal stress in the vessel in Problem 16.10

with and without considering the internal design pressure?

Answersz ot = TllO psi tension with intemal pressure considered.

ot: l7O psi compression without considering intemalpressure.

I6.5 VESSEL UNDER INTERNAL PRESSURE AND EXTERNAT TOADING

When a tall vessel supported in the vertical position is subjected to internal

|rcssure and extemal loading from such sources as earthquake or wind, both the

tcnsion and compression sides of the cylinder must be examined. These items

rurc similar to those for a tall vessel under internal pressure only, except for the

Irl(er only one of the sides needs examination. The earthquake loading or thewind loading is resolved into an overturning moment that is further resolved intolcnsile and compressive loads.

Using the membrane shess equations given in Eq. 10.2, the total longitudinalntrcss is determined ftom

And in terms of the present ASME Code, VU-l, the total longitudinal stress isobtained from

,PR W 4M"(f':-|-=-=----..--:-

2t rD^t nDit

lR \ w 4M.6t: *P (t - or/ =i.,';fr

(16.20)

(16.21)

As can be seen from this equation, many different combinations of stresses must

hc examined to obtain the maximum stress such as, with the first term equal tozero when tlere is no internal pressure (vessel not operating), and with internalpressure, with the second term either iension or compression, and with the thirdtcrm either tension or compression. There may be more combinations because

rhe value of W, the dead load, varies depending upon the location of the plane

lhat is being considered. Usually, the maximum stress is located at the supportline; however, when the vessel has various diameters, it may be necessary tocxamine stresses at different cross sections. This, of course, is not consideringany local stresses in the shell caused by the support.

Ilxampte 16,8. The vessel described in Example 16.l is to be supported at theIower shell-to-head junction. What are the longitudinal stresses in the shell

above and below the support line? The intemal pressure is 225 psi.

Solutian. From Example 16.1, the dead load of the various components is

Page 304: Process Equipment

386 TAtr vlssEls

;::: i:;::i:Shelt fluid = 2O,62O lb

Fluid, heads = 2,290 tb

The overtuming moment is

M" = 864,000 in.lb

Using Eq. 16.21, the total longitudinal stress is

- = * <zzst(#* - o 2) !ft#6.u. ffi#3The side of applied force above the support line is

dead load : shell + upper head = ITOO + 815 = 10,515 lbo1 = + (6705) - (110) + (ffi01 = 72OO psi tension

The side of applied force below the support line is

dead load = lower head + contents : gl5 + 22,910 = 23,725 tbo1 = + (6705) + (250) + (0) = 695S psi tension

The opposite side of applied force above the support line is

at = +(6705) - (110) - (600; = 56* psi rension with pressure and710 psi compression withour pressure

Example 16.9, The vessel given in Example 16.3 is to be constructed trom5.{-516 Grade 60 marerial --a o""ign"d f- +zS pri ut iSO;f."I.lle weto jointefficiency is E= 1.0. what are trre tota longiirJina- rtr"rr"r' on uotr, tr,ewindward and leeward sides at the support line? What are the allowable tensileand compressive shesses?

S1luti91, From Table UCS-23 ofthe ASME Code, VIII-I, for SA-516 Grade60 at 650'F, the allowable tensile stress is t = 15,m0 psi. The weight of theshell and upper head above the support line is'determined'from Eiu-pt" tO.S u,

W : 65,2rO + 0.5(3320) = 66.870 lb

. The. overtuming moment due to the wind loading at the support line isdetermined from Example 16.2 as

I6.5 VESSET UNDER INTERNAI PRESSURE AND EXTERNAT I.OADING

M. = (862,570)(12) = 10,350,840 in'-lb

l)etermine the total longitudinal stress o1 using Eq. 16.21 as follows:

oL: + @7s)(*- o.z) t ftffi ' 11ffi#E

ot = + QO3O) -f (350) + (3540)

Windward Side Stresses

|. Pressure, dead load, wind load = +(7030) - (350) + (3540) =10,220 psi tension

2. No lnessure, dead load, wind load : 0 - (350) + (3540) = 3190 psi

tension

3. Dead load only = 350 psi compression

I t eward Side Stesses

f. With intemal pressure, dead load and wind load'

= +(7030) - (350) - (3540) = 3140 psi tension

2. With no internal pressure, with dead load, and wind load

= 0 - (350) - (3540) = 3890 psi compression

A I lowable Stre ss-Tension

& = 15,000 psi for 5,{-516 Grade 60 at 6507

Allowable Stre s s-C omPres s ion

. 0. 125 - 0.12s : o.0go^

= nJ, (31/ l)

and fron Fig. 8.1 I and also Fig. 5-UCS-28.2 of the ASME Code, VI[-l ' the

value of8 is 11,500. This gives an allowable stress ofS": 11,500 psi' Allcalculated stresses are less than the allowable stresses. I

I'roblems

16.13 A tall vessel is constructed of a cylindrical shell with a flat head on each

end. The shell is 4 ft inside diameter by 2 in. thick by 75 ft from end

to end. The flat heads are ?.5 in. thick. The vessel is supported on the

bottom that rests on structural supports that are 75 ft from the ground

level to the support line of the vessel. The wind zone is 110 mph and

Page 305: Process Equipment

!tt8 TAtr vt33!r3

t6.t4

And the axial compression unit load is

thc Unilbrm Building Code prevails. What are the longitudinal streliom wind loading on both the windward and leeward sides abovesupport line?

Answer: o2from wind load = -r 1 660

Assume that the vessel described in problem 16.13 is supported onground instead of supported 75 ft in the air. What are the tonsituJshesses from the wind loading in the shell above the support iinei

Answer: oL from wind load : +1360 pel

16.6 VESSET UNDER EXTERNAL PRESSURE ONIY

For.a tall vessel under external pressure only, in addition to the basic consid.erauons tor external pressure design given in Chapter g, the effect of fluidpressure and dead load is considered. This is very iimilar to those conditiongconsidered in Section 16.3 for the vessel under intemal pressure only. When

S::l bl9: caused by th€_ fluid pressure and dead load create a compressrv!toadrng. lt has to be combined with the loading from the extemal pressure.

- ]he ASME Code, YI[-l, has methods to consider each of these rwo rypesof.loadings separately. Extemal pressure, of course, is described in UG_2g andaluar compresslve stress on a cylindrical shell is described in UG_23(b). How_ever, there is no method given in the ASME code that describes how to considerboth at the same tirne. An arbitrary method to consider these two loadingssimultaneously and use the ASME Code, VI[-l, procedure was developed iyDr. E.O. Bergman in 1954.6 This method combinei the effects of axial loadingeand extemal pressure by establishing an adjusted pressure used in the extem-alpressure calculation procedure given in UG_2g.

Based on the von Mises instability formulas as discussed in Chapter 8 for acylinder loaded with both radial and axial pressure fouaing, "

uju. oJ-r-i,drtermined-for values of L/D. and t / D,. This is plotted in f.igl tO.O tom wtrichthe value ofz can be easily determined for varioius values of"Lf D. versus t/Do,

A comparison of results between pressure on the sides only and pressure onthe sides and ends indicates that the value of z changes very iinle for values ofc < l 0. The ratio a is the axial compression unit toad divijed by the allowabloextemal pressure that is permitted when it is acting alone. Eipressed in anequadon,

p

Pp.

P.. = W' nD^

1000

800

800500400

- 300

a 200

n

! roo

!eoFooE50340

30

100.1

llsure 16.6 Numb€r of Lob€!, 4, into which o .hell will collopse when subi€cr lo uniform extornol pr€ssuro

nnd the compression term m is

1.23 D:"' L',(16.24)

Ity applying Sturm's equationT for the ratio between the extemal pressure alone

rrna thi *i"t "o-p."ssive

loadings, an equation can be developed that gives an

cquivalent external pressure Pj for the combined loading as a multiplier of the

base extemal pressure Po. This equation is

Pl= n2-1+m+mct (16.2s)n2-l+m

For a ) 1.0, the vessel rnay fail by yielding and should also be checked as

u cantilever beam including the axial shess effect due to the external pressure'

fhe axial load from the extemal pressure is

P* = 0.25 P"D- (16.26)

D

(16.22)

'Ihe axial load from external pressure in Eq. 16.26 is combined with the axial

load from dead loads in Eq. 16.23 to give the total axial loading on the cylindri-

cal shell. When this loading is divided by the shell thickness, the result is the

total axial compressive shess on the cylindrical shell. This actual stress is

compared with the allowable axial compressive shess determined according to

UG-23(b) of the ASME Code, VI[-l.

Example 16.10. A tall vessel is constructed with a cylindrical shell and two

589

1.0 2 3 4 56 810Length to diameter ratio {t/Da}

(16.23',)

Page 306: Process Equipment

TAu, VtSSH.S

hemisphericul heuds. The vessel is designed for lull vacuum (15 psipressure) at a design temperature of 550'F. The material is 5A-516 GradeThere is no corrosion allowance required. The vessel is l0 ft 0 m.diameter and 116 ft 8 in. from tangent to tangent. The vessel is to bein the vertical position and supported at the bottom tangent line. It containsffuid weighing 50 lb/fd. Thee stiffening rings are evenly spaced at 30 ft 0 inwith 28 ft 4 in. from each tangent line. What are the longitudinal stressesthe support line?

Solutian

l. Determine a preliminary thickness based on the extemal pressureusing the procedure of the ASME code, vl[-l, uc-28(c)(1).a thickness of t = 0.75 in. D. = 129 + 2(0.75) = 121.5 in. D"/t -121.5/0.75 = 162, and L/D": 360/121.5 = 2.9630. From Fig,5-UGO-28.0, A = O.OO022.

^ 2(O.OW22)(26.38 x 101," = -----ffi = 23.9 psi: t : 3/4 in. OK

,, Determine the weight of the vessel and contents when

Shell-weight : zr(60.7 52 -602)Q4C0)@90 / 1728) = 112,950Heads-weight : (4 /3\n(60.753 -603)(490/ t728) = 9,740Contents-shell = n(61)z (l4N)(50 / 1728)

Conrents-head : (4 / 3) n(60)3 (50 / 1728)

:458,150

= 26,180

3. Determine the maximum compressive load, (lb/in.) using Eq. (16.23) as

follows:

^ w (il2,950) + 0.5(9740)

": no,= "il:lul, = rlu'o lDlrn'

4 = 15.0 psi

P, (310.6)

"= Fh= (,ffi = 0.1704

(1.23) (1.23)

^=A/D"f:ffi=0.1401n = 3.0 from Fig. 16.6 for L/D,: 2.963 andD"/t = 162

p; = e - l *t0:11

13,11(0 r?04) (r5) = rs.04 ps'

As determined in step I, the maximum allowable extemal pressure based ont : 0.75 in. is P, = 23.9 r", at 550T. Because the required pressure of 15.04

I6.7 VESSET UNDER PRESSURE AND EXTERNAI. TOADINO 59I

lir is less than the permissible pressure of 23 9 psi' r .:.0 ?5 in'.is satisluctttry

i;il;; ;i;;; tian I .0' no cantilever beam check is needed' I

l'rohlcm

16.15 A tall vessel consisls of a cylindrical shell with-the lower head a hemi-"" --

soherical head and the upper head a flat head Because the upper head

ffi; ilp".t; J; *"igi'tt or zo,ooo lb from connecting equipment it

is rnaAe- 2'S in. thick. The vessel is designed for full vacuum at room

i".p".*."' Material is 5A-516 Grade 60' and there is no corrosion'

The vessel is to be hydrostatically tested in the horizontal position and

installed in the vertiial position The vessel is supported at the lower

treoa+o-stt"tt tangent line' No stiffening rings are permitted' The vessel

is 5 ft 0 in. insidi diameter by 60 ft 0 in' from tangent to tangent' The

vessel contains only a gas during operation' What is the required thick-

ness of the vessel?

Azswer.' Required thickness = 5/8 in'

I6.7 VESSEL UNDER EXTERNAT PRESSURE AND EXTERNAL LOADING

A tall, vertically supported vessel which is subjected to extemal pressure and

.*rc.uf fouain! contains ,tre'set similar to those in a vessel with extemal

ur"rror" on". ft "

*"thod of combining loadings as developed by Bergman and

il.,scribed in Section 16.5 is used to obtain Pj used in the analysrs-iit"

".f"-Aff"t*"e between Sections 16'5 and 16'6 is that an expanded value

,,,'i;ii#J.i;;; are used in obtaining P" which is given in Eq' 16 23:

W .4We 4MP'=

-trD^

* ;D3- nDz(16.27)

'l'his new value of P, is then used to obtain new values of c and P/ from Eqs'

16 .22 and 16 .25 .

llxample 16'11. For the tall vessel described in Example 16 10' what are the

tonsitudinal stresses when the vessel is designed for earthquake zone 2 using the

Uniform Building Code?

Sotutian, It is necessary to determine the lateral earthquake forces and the

,,u".t,-iog rno."nt at thl support line Using Eq' 16' 1' the lateral earthquake

lbrces may be determined.

y=|fcrzone21= 1.0

K=2.O

Page 307: Process Equipment

392 TAu. VtSSEtS

w 607,(xx) tb

I - l4(X) in.

w 607.000*:'h= ffi: 433.6tb/in.

E = 26.38 x 106 psi

d+t 120 + 0.75t O.75

I,:0.049(l2l.5a - l2O4) = 517,600 in.a

T=ooeo8./ (433.6)(l4ooF : r norov (26.38 x t06x5t7,600)

-1c:_=--::0.{1666ls v(l.0029)r(C = (2.0X0.0666) = 0.1331

CS = (0. 12X1.5) = 0. 18; maximum is CS : 0. 14

KCS = (Z.O)(0.14) = 0.28; maximum KCS : 0.3y = (3/8)(l)(.28)(607,000) : 63,740 rb

F' = 0.07(1.0592)(63,7 40) = 4,7301b but not more than 0.25y = 0.25(63'740, = 15,940 lb; F, = 4730lb

F" = V - F, = 63,740 - 4730 : 59,010 lbM" = (s9,010X1400)(2/3) + (4730)(1400) = 61,698,000 in.-lb

Using Eq. 16.27, determine total compressive loading as

," = ffi* ffr^@# : 310.6 + 5387:1 = s6e8.3

P, = 15.0

P /56OR 1r

"=#r=ffi=3-t266m = 0.1401

n=3.09-l+0.1401

= 15.8 psi

Because r : 0.75 in., MAW? = 23.9 psi at 550.F, the shell is still acceptablewith the earthquake loading. When a is larger than 1.0, the vessel is checkedas a cantilever beam. The axial unit stress due to p- is

P_:2! =Gs)(120.7s) : 452.8rb/ in.

BIBTIOGRAPHY 593

Axill stress is (452.lt + 5698.3/().75) : lt,200 Psi'

lirftowing the method given in UG-23(b) of the ASME Code' -Vlll-l ' thc

lllowable" axial "o-p."riiu"

stress on a cylinder is determined as follows:

0.125determine A = = 0.125181 = 0.0015

R.lt

Ar 550'F, the value of B from Fig. 5-UCS-28 1 of the ASME Code' VIII-I ' is

l;ititi pJ.' -ont"qoently, the actual compressive- stress. of 8200 psi is less than

thc allowable compressrve sness of 8700 psi, and the plate thickness of 0'75 in'

rs satisfactory. I

l'roblem

16.16 For the same vessel described in Problem 16'15' what is the required

thickness if the 20,000-lb force is applied at the edge of the cylinder

rather than at the center of the head?

Answer.' Required thickness = 5/8 in Although--the €ffect of the

overtumlng moment ls added, the thickness originally selected is ade-

quarc.

REFERENCES

ANsvAPlstandard62o,RecommendedRulesforDesignandConstruc|ionofLarse.weucd',Inw-Pressure Storage IdnIJ American Pelroleum Institute Washington' D L '

ANSTAPI Standard 65 O, Wetded Steel Tanks for Oil Storage ' American Peroleum Institute '

Washington, D.C.

ANSIStandardA58.l-lgS2,BuildingCodeRequirementsforMinimumDesiSn.I'oadsinAuiidings and Other Stntct r€r, American Nalional Standards Institute' New York' 1982'

Uniform Buitditrg Code, 1982 ed , Intemational Conference of Building Officials' Whittier'

Cal.

Dechetto, K., and w. Long, "Check Towers for Dynamic stability

"' Hydrccarbon Pro-

c?rrir,g, Vol. 45, No. 2, February 1966, pp' 143-147 '

Bergman, E.O., "The Design of Venical Prcssure vessels Subjected to Applied Forces"'

it"?in vuutt ona piping Design ASME New York' 1960' pp 576-580

7. Strum, R.G., A Study of the Collapsing Pressure of Thin'walled Ctlinders' University of

Illinois, Engineering Experiment Station, Bulletin No 329' 1941

BIBLIOGMPHY

Den Hartog, J. P., Mechanical Vibratiots, 4th ed , Mccraw-Hill' New York' 1956'

Wrndenburs, D. F , and C. Trilling, "Collapse by lnstability of Thin Clindrical Shells under

Extemil Pressure," Ttuns. ASME Vol 56' NewYork l9J4 pp ulv-bzJ'

Page 308: Process Equipment

CHAPTER 17VESSELS OF NONCIRCULAR

cRoss sEcrloN

595

Page 309: Process Equipment

396 V!33H.3 0r NoNctRcutaR cRoss sEcfloN

17,I WPES OF VESSELS

Although many kinds of noncircular cross sections may be used for proces!vessels, only a few configurations are used widely. The ASME Code, VI[_l,limits design rules to vessels of rectangular cross section as shown in Fig. 1i, iand Fig. 17.2 and to obround cross sections. Some additional rules are given fofvessels with a circular cross section that utilizes stay plates to give addedltrengthto the vessel. The rules in this chapter are limiied to vessels with a straightlongitudinal axis and noncircular cross sections. Rules are given elsewhere iorvessels with or without a circular cross section that is made into some other shaoothan one with a shaight longitudinal axis, such as a torus.

Some vessels contain very few openings, whereas many others contain manyopenings. If tlere are only a few openings, they usually are individually rein'.forced by replacing the area removed as described in Chapter 11. In manvvessels, multiple openings are calculated according to the rules for ligaments. Iijlte diamelers of the openings are uniform through the wall thiikness, theligament efficiency is calculated very similarly to that for a circular vessel. Iftheopening consists of several different diameters through the vessel wall thickness ,depending upon the type of calculated stress (either direct membrane sfiess orbending shess), the effective opening size and the ligament efficiency calcu-

Figur. l7,l Four-plore rectongulor hoodcr utilizo! wsld ioints or eoch corner. (Coortesy Ecodyne MR/r{Diviiion)

l7.r TYpES Ot vEsstls 597

Fiour6lT.2 "C" thops headeru wiih lorg€-rodius corne'5 {or minimum sire$ €oncanlrolion dnd flol w6ld ioint

for eosv rodiogroptry. (Courre3v EcodFo MR'vt Divkion)

lations are determined in different ways' Vessels with rectangular or square cross

r;*it*t."y tt built with many different combinations of wall thicknesses'

;it"i"." "o.uinutions

where two opposite sides have the same-wall thickness

^"J*ft".,ft" ",ft- two opposite sides have a different wall thickness ftom the

"ii"# tiJ".. nts $pe is often used in air-cooled heat exchangers' other

ffiil;;;i; fu iioes or different thicknesses' wheteas still others mav

uiitir. ,tuv'ptut"t to stiffen the flat sides of the vessel'-'.

i"n"rui diff"."nt combhations are shown in Fig' 17'3 for rectangular cross

r""ii#ii rt ti r"yplates, in Fig' 17'4 for rectangular cross sections with stay

;;;;d]; F s i'?.5 for obrooid and circular cross sections with and without

"*y ;il; ;ilf""gh the analysis is similar for vessels with intemal pressure

"oirJarea witfr tnos! with extemal pressure, the effect of stay plates on each type

is di-fferent.

Page 310: Process Equipment

+--J

+ l";

figur€ 17.3 Ploin ractongulor crols sectioff. (Courtesy of Americdn So.iery of rt^€€honicol Engineer!, fromFis. l3-2(o) of the ASME Cod€, vlll-I.)

598

fioure 17.,1 Recrongulor crds s6ction' wilh sloy plot€s'

kim Fis. l3-2(o) of the ASl,tE Cod€, Vlll-l')(Couriesy Americon So.isfy of

'{echonicol Engine€n'

s99

Page 311: Process Equipment

:-(

.1--

(c) (d)

Figure 17.5 Obround ond circl.llor cros. .€crions with ond wiftout sioy plote!. (Co,rrr,e5y Americon SociotyoI lchonical Engiru.rc, tom Fig, t3-2(b) ond (c) of th€ ASME Code, V t_I.)

600

(17.1)

I7,4 TIGAMINT ETFICIENCY FOR CONSTANT DIAMETER OPENINGS 60I

I7.2 RULES IN CODES

Spccilic rules for the design of vessels of noncircular cross section have been in

;ifi ;ffi A;;, tI[- 1, iince the r97 7 Addenda' Prior to that time' the ASME

(ieaDDliedseveraldiftbrentmethodsforestablishingthemaximumallowable-,'rir"I

"t i"it= i;; ".tt.it

tr noncircular cross section ln 1963' the ASME

i,;[';:"ffi;A;A Cu." irrs rot noncvlindrical pressure.vessels' This code

,,,r, *.rtin"O the heads and covers to bi calculated according to UG-34' but

il;;i;il;tid;;iuie" p-a["] to ttt" longitudinal axis be calculated according

il;;;6. il;;;;i*rt", p"r-its ttre thic[ress or maximum-allowable working

irr"r*i!',J" i","t-ined analytically or by one of the proof tests permitted by

tho ASME Code.-tn addition to the rules for vessels of noncircular cross section given in the

ASME-Cod", VIII-I, design rules for rectangular vessels^are contained in

i ,i,,yd" R;;i;*;i strippin!,r the Swedish Pressure vessel code'2 and several

other codes.

I7.3 OPENING IN VESSELS WITH NONCIRCUTAR CROSS SECTION

lirr those vessels and headers that contain a limited number of openings that are

:';; ;;;g;-lrt p"n"m, the method of reinforced openings mav be applied For

the flat sides of noncircular vesseis, the reinforcing rules for flat plates apply lfi;; ;;;;i;;t ;;angea in a reluiar pattern' the method of ligament efficiencv

rrrav be apDlied.""i;;Jfi;i"ament efficiency appears in both of the equalions for mem-

brane stress and for bending stress, foi some opening confi€urations it is neces-

,^t a J"i".-it" both *rJ hgament efficiency for membrane stress and the

ili;,-#;i"*t r- t"nain! $ress' In addition' it is necessary to determine

iii**"Ld i"* "in;iency

relati-ve to the degree of weld joint examination' The

k,wer effiiiencY of the two is used'

I7.4 TIGAMENT EFFICIENCY FOR CONSTANT DIAMETER OPENINGS

l'or flat plates with constant diameter openings in a regular pattem as shown ln

i ig.'i?.6, ,ii" flg"."nt efficiercy for b;rh membrane and bending stresses is the

same. When the two opemng's being considered for setting the ligament

"iil"i*"y rtu"" Ano"nt diam;ters, it is necessary to determine an equivalent

oi"-"i"i"i,ft" openings by averaging their diameters as follows:

DB=O'S(dt+dz)

The ligament efficiency is then determined as

Page 312: Process Equipment

vtssEts of NoNctRcutaR cRoss srcTtoN

P_DFcm-eb--

p

Example 17,1. What is the membrane and bending ligament efficiency in arectangular cross section header in which 11:6 lf|.-, h = 12 in., andtt = tz = 0.75 in. with a single row of 1.5-in. diameter holes on 4-rn. cenrer-to-center spacing?

Solution. Using Eq. 17.2, calculate the efficiency as

4-1.5= 0.625

(17.2)

T

!,xrmple 17.2. A single row of openings is altemately spaced on 4-in. and3.5-in. center-to-center spacings. The opening diameters also alternate with firsta 1.5-in. diameter opening followed with a 1.25-in. diameter oDenins. What isthe minimum ligament efficiency for setting thickness?

Solution, Calculate the equivalent diameier DE to be used in the ligament

Figuro 17.6 Op6nings wiih constonr diomerer.

r7.5 IIOAMENT ETFICI€NCY SUBJICT TO MEMIRANI STRT3S OOI

rllicicncy equation i|s

Da=05(1 5 + 1'25):1375in'

.|.|rglisamentefficiencyisbasedontheminimumspacingofp=3'5in.ustng

tlrc eq-uivalent diameter Dr = 1'375 in'

€^ = €r:3's ,.1'3" = o.ao,

l'roblems

l?.lAheaderisdesignedforaligamentefficiencyofe-=-e'=0667Whatis the rninimum cen

".-,o-tJnt"' 'puting for 1 ?5-in diameter openings?

Answer: d = 5'25 tn'

17 .2 Theflat side plate of a rectangular header contains two.rows of 7 /8in'' ' '- iiL"L

"p"oing.' th" 'o*'

ie 3-in' apan and the openings,are on 8-in'

Jt"-ui" r6.gi*-oinal spacing along each row The header. aLso contains

" i""d;JtJi*ao ioint alon'g ttre ienter of the same flat side plate The

;;il'j"t"r, only visually eiamined' has a weld joint efficiency of

f = O.ZO. Wftut is the efflciency used to set the minimum required

thickness?

Answer: E = 0 70, which is less than the ligament efficiency'

17.3 If the header in Problem 17 ' 2 has the weld joint examined by fuli radiog-' ' '-

t"pfty, *ft" is the efficiency used to set the minimum required thickness?

Answer: E = 0'825' which is the ligament efficiency'

I7.5 TIGAMENT EFFICIENCY FOR MULTIDIAMETER OPENINGS

SUBJECT TO MEMBRANE STRESS

Therearemanydifferentarrangementsofplateswith.openings.withmulti.;;;; ",

.iio*n in Fig 17 7' For use in air-cooled heat exchangers' the

."iiidi".J" ar" orr-gJd in increasing diameter through the-plate thickness

*t "*",

i", ,. "a-in

tubJs the larger diarieters are needed for rolling in the tube

for holding power. Any nrrung"'fi"nt of various diameters may be considered'

For me-mLrane stress, the ligament efficiency is

D-Dap

T

( 17.3)

Page 313: Process Equipment

vt33!t3 0f NoNctRcutaR cRoss sEcfloN

11 . p- d1

Figur. 17.7 Op.ning! wirfi muhi{iomeier.

where

o" = I@on + dlt + dzTz + . . . + d,n)

Example 17.3. Determine the membrane ligament efficiency in a headerwhere /r : tz = l.5O in. The header contains a series of openings on 4_in,centers. The openings are multidiameter, as shown in Fig. lt.g.

Solution, Calculate the equivalent diameter DE using Eq. 17.4 as follows:

(t7 .4)

P:4in.da: 1.625 in. ?6 = 0.125 in.

dr = 1.5 in. T1 : 1.125 in.dz = 1.375 in. Tz = 0.25 in.

I7.5 TIOAMINT EFFICIENCY SUBJECT TO MfMBRANI STRESS

Jfigure 17.8 Hole dsloils Ior oxomple l7'3'

D, =1#(r.625 x 0.125 + l.s x 1.r2s + 1.375 x 025) = 1 490

in. IExample 17'4. Tubes are expanded into a rectangular header that is 1'25 in'

tt ict. 'fne

notes ute 0.875-in. diameter with two 0 3l25-in -deep grooves in the

hole for holding power. The grooves are 0 125 in' high with 0 25-in' spacing

between them.-The top gtoove is 0.25 in ftom the top edge What is the

membrane ligament efficiincy if the openings are on 3-in' centers?

Solutinn. Calculate the equivalent diameter DE using Eq' 17 '4:

p:3in'do = 0.875 in. ?6 = 0.25 in'

dr : O.9375 in. T : O.125 in-

dz : 0.875 in- 7i : O 25

dz = 0.9375 n. \ = 0.125 n'

d, = 0.875 in' 7i = 0.50 in'

," = #(0.875 x 0.25 + 0'9375 x 0.125 + 0'875 x 0'25 +

nr

II-,--

INt:

:I PlFl+I

I a, tt.n>jF;--;;;'r*1

do = 1,625"

0.9375 x 0.125 + 0.875 x 0.5) = 0.888

Page 314: Process Equipment

606 Vt33!r3 0t NoNctRcurAR CROSS SECTTON

The mcnrhranc ligunrcnt cllicicncy rs

",=1:jq=o.zo+

Problcms

17.4 A rectangular header contains a series of tube holes on 3.5-in. centers.The holes are l-in. diameter with the ends counterbored 0.25 in. deeo toa diameter of 1.125 in. ff the plate is 1.5 in. thick, what is the lisamentefficiency for membrane stresses?

Answet etu = 0.702

17.5 A seamless square header that hasT l/4-in- inside measurement by 1.125in. thick is to be formed so that it will have a constant thickness. Thcheader contains a row of 2-in. diameter on 3-in. centers. The holes havcone groove for expansion at the midthickness of the plate that is 0.125 in.high and has a2.125-in. diameter. The opposite wall contains a series ofhandhole openings 4.25-in. diameter on 7-in. centers with a seat on theoutside 0.125-in. deep by 4.75-in. diameter. What are the ligamenteffi ciencies for membrane stresses?

Ansver2 e^: 0.328 on tubeside

e^ : 0.384 on handhole side

17.6 A header is to be made from 1-in.-thick plate. The plate contains a rowof tube holes on 3.5-in. centers. The holes are allernate 2 and 2.5 in. Allholes are counterbored 0.25 in. and to a O.Zs-in.larqer diameter. Whatis the ligament efficiency for membrane stress?

Answer: e. = 9'339

I7.6 LIGAMENT EFFICIENCY FOR MULTIDIAMETER OPENINGSSUBJECT TO BENDING STRESS

For a flat plate that contains rnultidiameter openings, it is necessaxy to determinean effective ligament efficiency in bending by locating a neutril axis of thevarious diameters and thicknesses of the openings and the effective moment ofinertia. From structual mechanics, the basic equations are

= 2AX" >A

I7.6 TIGAMTNT ETFICICNCY SUBJECT TO EENDING s]RESS

I =2 AXz

lrrom Fig. 17.1 and Eq. 17 5'

607

( 17.6)

(r7.7)

(17.8)

(17.9)

(17.10)

(17.11)

(r7.r2)

+z+...+4)-/\7;+...+T"l-/

"'n 4)

2A= boTo + bll + bzT) + .. . + b"T"

- >AX Eq. 17 7" >A Eq. 17.8

I=2Ior2AXz

t =boTo3 * brTrt + bzTrt +.. +bE'- tz' t2 12 12

/T^ \2* b'ft (? + rt + 12 + . . . + r. -I)

/T^

>Ax=bofr(;+4/a

+ btrt l; +

/'r-+ brTrl; +\-

/T\+ u.nlil

\-/

From Eq. 17.6

.^lr,-rarrrErT2* "+T,-X)lT -\'z+brr,(;+...+r.-x)/- ?\2

* b"r"v _;)c = larger off or (r - fJ

The width of the ligament is

b6=P-DB

Because c = t/2 and I = bEt3 /12,

(17.5) c tll2\ 6-=-l-------=l=--I 2 \bEt"/ brx

(17. r 3)

Page 315: Process Equipment

608

And

vtsstts oF NoNCtRCUtAR CROSS SECTTON

Dt=P (17. t4)

For bending stress, the ligament efnciency is

D_D"p (17.15)

Example 17.5. Determine the bending ligament efficiency in the header inExample 17.3.

Solwion

P = 4in.To : 0.125 in. do = 1.625 in. bo = 4 - 1.625 = 2.375 in.Zr = 0.375 in. dr : 1.5 in. br = 4 - 1.5 = 2.5 in.Tz = 0.25 in. dz = 1.375 in. bz = 4 - 1.375 = 2.625 in.

2 AX = 2.37s x 0.12s(O.o62S + 0.375 + 0.25)+ 2.s x 0.37s(0.1875 + 0.25)

+ 2.625 x 0.25(0.125\

) AX = 0.6963

2 A = 2.375 x 0.125 + 2.5 x 0.375 + 2.625 x0.25 = 1.8906_ N KOK?X =

1.8900:: = 0.3683 in.

r = + l(2.37 s)(0.12r3 + e.s)(0.37 13 + e.6zs)(0.2s)31+ (2.375X0.125X0.625 + 0.375 + 0.2s _ 0.36S3f+ (2.5X0.375X0.1875 + O.zs _ 0.36S3f+ (2.62s)(o.2sr(0.3683 _ 0.1212

/ = 0.0884

c = the larger of 0.3683 or (0.75 - 0.3683) = 0.3817

From Eq. 17.14, the equivalent diameter is

o/-n

Ds = 4 -#ffi = 4 - z'47: 1'53 in.

I7.6 LIGAMTNT EFTICIENCY SUBJECT TO EENDINO STRESS

thc ligament cl'licicncy lirr bending strsss is calculatcd lrom liq lT l5 us

4 - 1.53

609

= 0.617 I

|.)xamp|elT.6.TheheaderinExamplel?.4issubjectedto'bendingStressesin tt e nut sides. What is the ligament efficiency for the bending shess?

Solution

P=3in'To : 0.25 in. do : 0.875 in' bo = 3 - 0'875 = 2'125 tl:,'

Tr = 0.125 in. dr = 0.9375 n' h = 3 - 0'9375 :2'O625 \n'

Tz= 0.25in. dz=0.875\n' bz=3- 0 875 :2lZ5 in'

Z: = 0.125 in. dz = O.9375 in' bt: 3 - O'9375 : 2'0625 in'

Tr : 0.5 in. dr = 0.875 in' bq = 3 - 0'875 = 2'125 \n'

r, AX : (2.125)(0.25)(0.125 + 0.125 + 0.25 + 0.125 + 0 5)

+ (2.0625)(O.t25)(0.0625 + 0.25 + 0'125 + 0 5)

+ (2.125X0.25X0.125 + 0.125 + 0.5)

+ (2.062sX0.12s)(0.062s + o's)

+ (2.12sx0.s)(0.25)

X AX = 1.6484

t A = (2. 12sx0.2s) + (2.062sX0. 125) + (2'r2s)(0 25)

+ (2.o62s)(o.r2s') + (2.12sx0's) = 2'6406

- 1.6484x = L64C6 = u.o4+)

r = $ l<2. rzsxo.2r3 + Q'062s)(o.r2r3 + Q. t2sr(o'2s\31

+ (2.0625XO.r25)3 + (2.125X0.5f

+ (2.125)(O.25)(O.l2s + o.lzs + 0.25 + 0 125 + 0'5

- 0.6243)2

+ (2.0625)(0.125)(0.0625 + O.25 + 0.125 + 0.5 - 0'6243)2

+ (2.125X0.25X0.125 + 0.125 + O.5 - 0.6243)2

+ (2.0625)(0.125)(0.0625 + 0.5 - 0.6243)2

+ (2.125x0.sx0.6243 - O.2s\2

Page 316: Process Equipment

610 vrsslr.s 0f NoNcrRcurAR cRoss s[cTtoN

I = 0.3451 in.a

c = the larger oI O.6243 or (1.25 - 0.6243) : O.6257 \n.

Equivalent diameter is equal to

(6)(0 345r \De = 3 -ffi = 3 - 2 tl8 = 0 882 in'

1-ntR?eb : '-:------::-::= = 0.706

J

In looking at the efficiency from Example 17.4, this is a case where the groovclfor expanding the tube have little to do with the efficiency because e. = 6.794and eu : 9.796. a

Problcms

17.7 T\e header in Problem 17.4 is subjected to bending stresses as well a!membrane shesses. What is the ligament efficiency for bending stresses?

Answer: eu = 9.792

17.8 What are the ligament efficiencies for bending shesses in Problem 17.5?

Answers: et : 0.333 on tubeside

et : 0.367 on handhole sido

I7.7 DESIGN METHODS AND ATIOWABIE STRESSES

Design rules given in this chapter are for vessels and headers that have a sraightlongitudinal axis with a noncircular cross section and closure plates on each end,The fonnulas are based on assuming a unitJength vessel section with nostengthening effect form the longitudinal direction of the plate. However, forcertain uniform thickness vessels and headers, provisions are given for plates

with a length-to-width ratio of two or less to compensate for the added strengthfrom the longitudinal direction.

The design rules in the ASME Code, VItr-I, provide for vessels of rectan-gular and obround cross section where different walls may have different thick-nesses. The method used in the ASME Code, VI[-1, combines plate and shelltheory and stuctural design theory where it is necessary to assume wall thick-nesses and calculate stresses that are compared with allowable stress values.These methods were described in Chapter 7.

For vessels and headers of uniform thickness, e.quations can be developed that

I7.7 DTSIGN METHODS AND ALLOWABTE STRISSES 6I I

solvc lbr minimium required thickness in terms of geometry and applied bad-

ings. Even in these cases' some assumptions are. necessary because the thickness

isiirectly related to primary membrane shess, but, it is related by the square of

lhc thickness to primary bending stress '

B;th il.rty;embiane and primary bending s$esses are determined for th€

various configurations at each point examined' Where required' shesses may

"""J "O.i"t*E t f"r the effect oi a weld joint efficiency' if there.is one' and for

both thJ membrane shess and the bending saess ligament efficiencies when a

rspeating pattern of openings is used.-'n.""iai"g to ttre ASME-Code, VIII-I, a weld joint efficiency according 10

uw- t Z ls reiuirea for longitudinal butt-weld joints (and-some other butt joints) '

.trtrr.ugn tftJ*"fa joint eficiency is applied to the membrane stress at all points

"*u-in""O in tn" noi side plates, iiis applied to the bending stress only at the weld

'"i"i. ri A" examined binding stresJ is located in the flat side plate rather than

ui tt" *"tA iom,, the weld j6int efficiency is not applied' The ASME Code'

VUi- t , is "onsiOAng

applying the weld joint efficiency to the allowable stresses

instead of modifyinf thJcalculated snesses' However, in examining any polnt'

either method worki when the proper weld joint efficiency is used in the equa-

tions.'"-Only the lower efficiency of the weld joint and the membrane and bending

lit es."', efncien"ies is used. The weld joint efficiency is not modified by the

ii*u*"n "tn"i"n"y;

only the lower efficiency is used' If the weld joint does not

"3"* "i rt" p-", irxamined, only the ligament efficiencies. need be considered'

Provisions are given to account for holis with different diameters thrcugh the

olate thickness.-For those cases, an equivalent diameter is determined for calcu-

iating the ligament efficiencY.- iio- ttt"" for"going discussion, one realizes that care is. required in deter-

-i.i; tlt"- tttd"s a:t any location. In general, it is. easier to separate the

a"-ti-" stress and the bending stress at each location examined ln most

"r"ig*"ti-t , shesses should be ixamined at the midpoint and ends of the side

pf"telt waf as at the weld joint, if one exists Other points may also have to

be examined.The calculated primary membrane stress is limited to the basic allowable

t"nril",t "r.

gin"nin the applicable code; however, the combination of primary

-".U.-" .6tt pfus primary bending stress for a plate thickness assumed to be

rectangular in cross section is limited to the following:

1. At design temperatures where tensile strength and yield strength govern'

the lesser of the following:(a) 1.5 times the basic allowable tensile stress at design temperature'

(b) Yield strength at design temperature'

2. At design temperature where creep and rupture strength govem' the

lesser of the following:(a) 1.25 times the basic allowable stress at design temperature'

(b) Yield strength at design temperature'

Page 317: Process Equipment

612 VtSSttS OF NONCTRCUTAR CROSS SICT|ON

["br externll prcssure, where the total stress may be compressive, a limitation ilalso set based on buckling of the side plat€.

The basic theory is the maximum strsss theory that is generally used instructural analysis. For cross sections of members and stifieners other thanr. Tlangular, the combination of primary membrane plus primary bending streslis limited to the shape factor of the member times the basic ailowable tensilcstr6s in the applicable code but is not to exceed the yield strength at the designtemperatures where tensile strengtl and yield strength govem. At design teir.p€ratures where cre€p and rupture strength govem, the same limits apply, but thoshape factor multiplier is limited to 1.25 regardless of the actual shape factor,. As_mentioned previously, it is necessary to calculate shesses at various pointlin order to determine which combination controls. Certain analysis methods,such as that in the Swedish Pressure Vessel Code, combine the mjmbrane stresgand the bending stress in the same equation. It may be necessary to separate themfor evaluation when different efficiencies apply to the membrane stress ratherthan to the bending shess.

I7.8 BASIC EQUATIONS

For analysis purposes, the noncircular cross section of the vessel is consideredas a skuctural frame. Each component of the rectangular or obround framecontains a load that causes a membrane stress and i moment that causes abending shess. The total stress at any point is the summation of these twostfesses.

_ As shown in Fig. 17.9, the direct or membrane skess at any point is causedby intemal pressure loading against the adjacent walls. fhls toaaine is resistedby

-the-thickness, strength of material, and weld or ligament efficilency of thelvall! that are carrying the load. The applied loading d e)(1,) and the resistingloading is (&Xr)(2d. When these are equated to e;ch other and solved for S,lthe membrane stress for the short-side iJ

-Pht^: xrn

and for the long side, the membrane stress is

(17.16)

(17 .17)^PH

2t2E

From the theory of structural frames,3 the basic moment equations for arectangular frame under intemal pressure loading p when the two pairs ofoppcsite sides have equal thickness and equal length, as shown in Fig. -.9, areas follows:

llcnding moment at cOrner O is

M"=+Hl{'##)

llcnding moment at midpoint of long-side M is

u" __ un _P#

llcnding moment at midpoint of short-side N is

ur= un_P#

17.8 BASIC EouAlloNS 0r3

(17.18)

( 17. 19)

(17.2o)

Ith'

MM

Internal Pressure, ?

rigur€ '17.9 lnbrnol pr*3'rr. looding ond b€nding moment diogrom ior reclongulor 'ro$ !€crion heodor'

Page 318: Process Equipment

6t4 Vt!!!ts 0f NONCTRCUTAR CROSS SECTION

Momont ol incrtiu /1 lirr short-side is

t3L=\'12

Moment of inertia 12 for long-side is

r31.. '2| - n 07.22,t

The basic equation for bending stress rs

So:M'IBending stress in comer of short_side is

G)a=ryx!Z.lt E

Bending stress in comer of long_side is

6;)a=ryx!2lz E

Bending stress at the midpoint of the short_side is

tsr.lr: $ * 1UtEBending stress at midpoint of the long_side is

$,:ryx!simplifying equations, the equation for the bending stress at the midpoint of theshort-side is determined as follows:

Cross multiplying Eq. (17.18)

M. = P (t!!!-!'h\. t2\ hlr+HIz/Substituting Eq. 17.27 in Eq. 17.20 gives

(t7,2ll

(r7.23)

(r7 .24)

(17 .2s)

(17 .26)

(r7.27)

17.8 BASIC EQUATIONS 615

. P /htl, + Htlz\ PHzM,=ilffi)-? (r728)

('learing Eq. 17.28, we obtain

p /hJt. + Hjlz\,. - L t:_:.L--""- t2\w,+at, J

Clearing P/12 in Eq. 17.29 gives

P l2rrzr28 (17.2e)

(17.30)

(17.31)

(11 .32)

M-=+ffi#-1.s''?)Multiplying Eq. 17.30 through by (-l),

M-=+('5"'- +J#)Substituting Eq. 17.31into Eq. 17.25 andcfor hf2:

$),=h(""'- +tuo,.;

Ilxarnple 17.7. Determine the adequacy of a rectangular cfo-ss-sectional

headeiwith a design pressure of 150 psi and made from a seamless forging with

tn allowable .t "ti oi t2,soo psi' The header inside dimensions are 14 in by

7.25 in. with a constant thickness of 1 in. All openings are reinforced'

Solutian

1. Calculate the moment of inertia:

,=*$=oo',,2. Calculate bending moment at comer Mc using Eq. 17 l8:

= 1838.28

3. Calculate bending moment at midpoint of long-side M1a using Eq lT' 19:

Mu = Ma -'+ =1838.28 - *Tq = - ft3632

.. 150 /(14)r/0.0s33 + (7.25)3/0.0833\ua: i \- r+rerffi -llfr /

Page 319: Process Equipment

6t6 VtSSEtS Of NONCTRCUTAR CRO55 5ICT|ON

4. Calculate bending moment at midpoint of shorfside Mry using Eq.

Mu = Mo - + = 1838.28 - (150x-7 25)'? : 852.7J

PH2

8

5. Calculate bending stress at corner of lons-side:

(S)aa : (1838.28)(0.5) : 11,030 psi(0.0833)

6.

,f

8.

9.

10.

Calculate bending shess at midpoint of long-side:

( 1836.72)(0.5)(r"" = --O:d833- = I l'o2o Psi

Calculate bending stress at corner of short-side:

(S6)qv = 11,030 psi

Calculate bending moment at midpoint of short-side:

^ (852.73 )r0.5 )tsr)" = -to.offi : 5120 psi

Calculate membrane stress on long-side:

,", _PH (t50x7.2s)rs-,u= T = ,(D :540 psi

Calculate membrane stress on short-side:

Ph ( t50)( 14)(J'),v=t= r(ri: lo5opsi

Total stress at corner of long-side:

(S)o,u = (,S.),r.r * (S)aa:540 + 11,030 : 11,570 psi

Total stress at midpoint of long-side:

(S)u = (&)v + (Srr : 5,40 + 11,020 = 11,560 psi

Total stress at comer of short-side;

ll.

12.

13.

I7.8 BASIC EQUATION5

(S)c',v = (S')'v + (Si')or: 1050 + l l'030 = l2'0ti() psi

14. Total stress at midpoint of short-side:

ot/

(S).,v = (sJ,u + (S)' = 1959 1

All sfesses are less than allowable sffess values'

lrctory.

l,)xumple 17.8. A rectangular cross-sectional header is made from two C-

rcctions and butt welded along ule center of the short-sides' Th€ weld joints are

r|)otexaminedwiththebacking,t.ipt"ftinplacefromTable.Uw-12ofthe,ili*,riit"J", vrii-r' r = o.si' The design pressure.is l15,psi,at room tem-

,"r",ri."] *O tft" .","""f is se-S t S Craae i0 with an allowable stress of 1 7 ' 500

ilI. ri'!il;; ;il;ir.i uv r in thick and the short-side is 6 bv 0 625 in' thick'

( )ne lons-side contains a row ot i'S in diameter holes on 3'75-in' centers ls

thc desiln acceptable?

Solution

1. Calculate the ligament efficiency of the long-side with the tube holes:

c^=€t=:'ls,;1 s=oeo

2.Calculatethemomentsofinertiaofboththelong-Sideandtheshort-side:

l,r (0.625)r tz\ (lt -L = i= \-'Y:-' = o.o2o3 I,: i=;- = 0 0833

3. Calculate the bending moment at the comer Mp using 8q 17 18:

Calculatethebendingmomentatthemidpointofthelong.sideMMusingEq. 17.19:

M, -- Ma - ( = ror.rr- (115X13'5f : -1778'so

5. Calculate the bending moment at the midpoint of the short-side Mrv using

Eq. (17.20):

5120 = 6170 Psi

so 1-in. thickness is satis-

4.

Page 320: Process Equipment

6t8 vlsSIts of NoNctRcutaR cRoss stcTtoN

Mn = Mo -'+ = 84r.3s - t+q :323.8s

6. Calculate the bending stress at the corner of the long-side with the(E = 1.0):

<s,t*=W:ffiffi=5o5opsi

7. Calculate the bending stress at the midpoint of the long-side withholes (E = ea = 0.60):

Mucz ( 1778.50X0.5.)tsttu = -ilF: (0.0S33X0O

: I /./eu psi

Calculate the bending stress at the comer of the short-side (E = 1.0):

Maq (841.35)(0.3125)ttilaN = iE

: (o^oro3xl3) = 12'950 psi

Calculate the bending stress at the midpoint of the short-side (E : 0.80):

Mucr (323.85X0.3125)t.)att : lF = (oJro3xojo) = bzru Psr

Calculate the membrane stress on the long-side (E = e^: 9.691

PH (l rsx6)\r.)M = Ui = ,(lx0f)

: )uu PSr

Calculate the membrane stress on the short-side (.E = 0.S0):

Ph (l1sxt3.5)\r^tN = zttE = ,(o.6rsxo3) = l55u Psr

Total stress at corner of long-side:

(S)oy = 6^)u + (S)e1a = 580 + 5050 : 5630 psi

Total stress at midpoint of long-side:

(S),v = (S.),y + (Stff : 580 + 17,790 = 18,370 psi

Total stress at comer of short-side:

8.

9.

10.

11,

12.

13.

t4.

. 17 9 EOUATIoNS lN THE ASME CODt', vlll'l 619

(S)o,v = (S,)'v + (Sr')o'v = 1550 + 12'950 = 14'500 pst

15. Total stress at midpoint of short-side:

(S)p = (S'),v + (Sa)rv = 1550 + 6230 = 7780 psi

'l'hc allowable stress for membrane stress is 17'500 p:'-Td ft^t't* combined

rrrembrane plus bending t*t""t-'it"i i-s = l 5(li'500) = 26'250 psi All

|rlculated sfesses are tess tnan tne aiowable stresses and are acceptable'

l'roblems

17.9 A header is made ftom from two C-sections that are-buttrvelded along

the centerline of th" 'tto*-'iA"

fn" *eld is not examined and the backing

il;;;. in pro""; tr'"tiiott' E = 0 65 -The.header-is

12 bv 6 bv

I in. thick with a de"gn p'";tit" oiZoO psi' What is the stress at the weld

joint?

Answer: Maximum stress = 10'160 Psi

l?.10 A square header is made from two C-sections that are bxtt welded along

the centerline or t*o oppoiit" liJes' The wetd- ioint efficiency is 0 65'

The adiacent side co"tain' u 'ow

of openings that 'are

2-in diameter on

5.75-in. centers' fr'" O"'igtipt""ut" ii ttoisi and the lreader is 7'25 by

0'75 in. thick' Wf'ut it tfi"''l*ito* stress and where is it located?

Azs*er" Maximum stress = 5950 psi at corner of welded side

I7.9 EQUATIONS IN THE ASME CODE' VIII-I

Appendix13.r,h:f y:::*h#t" j;,:.lllllll1lH"',,'Tl:H jiJ,::iT;

ttriillT:l:i:Tfl irs:i;if#l:h'#' jfi *::*'ffi 'll"l,l:ASME Code :re expressed m c

to the sPecific geometries shown'

When the opposite sides have the same thickness' the equations in the ASME

Code, V[I-l, are the same * tnot" *iu"n in Eqs 17 16 and lT lT However'

when opposite thicknesses *"tt' *"*rt"" theri are rounded comers' or when

some other variation occurs , iir"'g"".""y, ue ,esM! code has a specific

equation for that conngo'ut'on 'f'ui

oiut J"utiopta ttot the theory of structural

ftHl'"quu,ion, for the bending stresses were similarly.developed The prin-

.ipi", oi"*o*a f.T::"',::1"*f .J:rT: ;#:ffiil:tX"il:^1f'""?#'fl

to sive different equatrons rol

Page 321: Process Equipment

;

(J

di

F

IqJ

5

6

(J

+Z:

\-l-!:'{

-(\-+I

,: -s*slj

I

\iI

I

+:\)

N+i .-i- i-]^!J -i1c.|

-Nl+ dl- ili< *llc ll-s tl.+Y ^ t!.1"l! rls q,i

Qaa

a<

ul!"4Fe-rr

-i+:'al+

:\]+\]f'l

r_]d d Idl .\ilN 6Jora.a\*<-<\'la '--:a lA

-l i ,lla :l :tN -t{ rN

Fa O lrl€E!

<at\

$\J

r- c- F-

621620

T-r't!.c.l

;,-..:\^;l{-l+

'{olI

E

le{-l$

IN

+: +crs \l*I

t(a

-^-r-i- T 5 i€-E-'"r l-lt5\(lFst. ,n F .*

{lv ^slv I ^r c'lol+ *l+ + + I

ll-=l- E o N-l-tir +.:_-:-\

"? ^' ]: : \"1^ :J

*+.F\E I ].tl$ ti! rl$ tlH ;F it5

3a93qLraaEEEFEEEEE:>S"a'Si

ii3333SsrxrrSSrC

3+I

9,)

-B'Ed9!YE->

9

rio0F

Page 322: Process Equipment

622 vfssg.s oF NoNctRcurAR cRoss sEcTtoN

same equatlon as given in Eq. 17.32 is

bending stress at thc midpoint of the short-side of a rectangular cross-sectlrheaderisEq.3of Article l3-7 of the ASMECode, VIII_1. bevelopment of

as,: ffiltsn'- o,ttti :ff

K=

| + o2K = t * l4 * I:, 1] - h3lt + H3t2. Lh,.. r,^i]____Fh

r+K=l *11 "',.1 -htt+Ht2Lh rtl hll

_h2(l + a2n = _orlhtl, + Hrl, u H, I(l+K) -L h'1, "ht,+Htr]

Substituting Eq. 17.38 into Eq. 17.33 gives

@,:#,rftt"'- +:#]Equation 17.39 is identical to Eq. 17.32 and shows the relationship between thlgquations in Appendix 13 of the ASME Code, VI[-l, and those derived fronbasic theory. The ASME Code contains extensive nomenclature in Article 13.!fo-r yarioug configurations. Equations for the bending stresses in Table l3_lg,lof the code are shown in Table 17.1. In addition, equations for membrana

:hTle! for various configurations in the ASME Code, VIII_I, are summarizodin Table 17 .2.

Although all the formulas have been developed on the basis of a length_to.width L1/H and Ly /ft of four or more-the ratio where there is no long dimen.sion effect-provisions are given for the simple rectangular header shown inFig. 17.3a to reduce stresses when the aspect iatio is lei than two. The mem,brane stresses remain the same, but the blnding stresses are reduced by multl.plying by the factors in Table 17.3. The stressei are then obtained by using thofollowing equations:

For the short-side at the comer:

(Sa)o = Eq. 17 .23 x C2

For the shon-side at the midpoint:

n

t;td

_ h3lt + H3I2

hlt + HI2

Iqble 17 .2

l,rIure Location Membrane Stress (Psi)

(t7

(17

(r7 ,

(r7.

(r7

(t7 .

l'l .3a

t't .3b

17 .3c

t't .3d

l7 .3e

tt.)a

t't .5b

Short-side

Long-side

Short-side

Long-side

Short-side

Long-side

comel

Short-side

Long-side

Shon-side

Long-side

Midpoint, curve

End, curve

Side

Midpoint, curve

End, curve

Side

Ph /(2hE)Ph/(2t28)

Ph /(2^D

-=:=--=l4NH'-2h'? | (K, + k?)b./Yttt2l I L

-kt(Kt + k) + "'k Kr - Kr))\

P(a + L)/^EP(h + s)lhEp(tE l17 + d/nsPhp/2(At + ph)E

PHp 12( z + pt)E

P(L+L.l+a)/hEP(h+h+a)/t2EP(a + L)/nEPa/hEPaltzE

P(a+L)pl(At+ph)EPap/(A, + ptt)EPap/(At + ph) E

(17

Tqble 17.3

LtlH or Lr/h Cz

1.0

1.1

1.2

1.3

1.4

l.)

1.6

1.8

1.9

2.O

0.560.640.'13

o.790.85

0.89

o.920.95

0.9't0.99

1.00

0.62

0.70o.77

o.82

0.87

0.91

0.940.960.9'l0.99

1.00

(17.40)

623

Page 323: Process Equipment

vEssH,s oF NoNctRcurAR cRoss sEcfloN

(Sr,),v = Eq. 17 '25 x Cl

For the long-side at the corner:

(sa)o = Eq' 17 '24 x Cz

For the long-side at the midpoint:

(Sa),r.r = Eq. 17.26 x Cl

For those cases where eitdrrer Lr/H or Ltf h is elss than 1.0, it is necessary

reorient the axes of the header and to recalculate all properties such as

of inertia of the wall. Dimensions are chosen so that the longest dimension is L1,the next dimension is ft, and the shortest dimension is 11. This may result inpafi which was originally considered to be an end closure becoming a wallthe header. All calculations are based on this revised confieuration.

Vessels of noncircular cross section may be subjected to external pressuro,

Membrane and bending sfiesses are considered the same as for intemal pressununless the resulting stresses are compressive where stability may be a possibhmode of failure. Interaction equations are used to examine the various plates fotstability. Calculated stresses are compared with critical buckling stresses with Ifactor of safety applied. This is described in Article 13-14 of the ASME Codo,vl[-l.

Example 17.9. The rectangular cross-sectional header in Example 17.7 ilmade according to ASME Code, VIII-I, rules. What are the bending stresses atthe midpoints of both the short-side and the long-side?

Sohttion. Knowns: Il = 7.25 in.: h= 14 in.; r= 1 in.; c = 0.5E = 1.0. Calculate a. 1. and K as follows:

"=#=T:o.ttnrl fl\lr=i=;-=0.0833

. = (,:)" =0.0833 :0.5179

(0.0833X0.s 179)

Calculate the bending stress at the midpoint of the short-side using Eq. 17.33and Table 17.1, second equation:

(1s0)(0.5)(Ja)":l2(0.0833)(1)

fr s,z rsv - /t4), I + (0'5t79)3'l

Lt.J\t.zJ, - rr+,

-l

( r7.4

r7.9 EQUAI|ONS lN THI ASMI coD[, vlll'l

(Si,),v = 5120 Psi

Calculate the bending stress at the midpoint of the long-side using Table 17 l'

lirst equatlon:

(l50x0.s)(l4f f, . - I + (0.51?9)rl = lr.020psi(s,)" = 1;(o58txt L' ' I -t o.5l7e I

l,lxample 17.10. The header in Example 1?'9 is to be truilt with a shortened

ffi;;ffi;;; = ia in. wttu' '" trt" foesses at the midpoints considering the

rho-rtened length?

Solutian. Zr = 18in';H = 7 '25 in'; andh = l4it' Calculate the following:

L' = 18 = 2.48 cr : c2 = l.oo

H 7.25

L: = 9 = t.ZS Ct = 0.79 znd Cz = 0.82

h14

The strengthening effect applies to the long-side only because the length-to-

width ratio ii less than 2'0 This gives

(s)1q' = (s6)r x cl = (11,020)(0 79) = 8?10 psi I

ExamDle l7.tl. The header in Example 17 9 is to be built with a shortened

ffi1ilfi;;''= iz in' whnt is aonejo trt" n"aaer axes for analysis and what

^r"",il"'r'o""". " ,rt" midpoints oi the short-side and the long-side?

Solution. Calculate the header geometry properties as follows:

Lr: 12 = t.66H 7 '2,5

4 =9 = o'ssh14

Since Lr/h ( 1.0, the axes of the header must be reoriented for analysis ln the

ffi;#, r,) tqin.,h= 12in', andrl-= 7'tf in' - -,,1:The first assumption is that the originat flat end closur-et^which have now

b".;.';i;;";'also I in trti"t on'tttur basis' 1= 0'0833 remains'

" =+ =ff = o.suz

K = O.6042

I

( 17.

and

Page 324: Process Equipment

vEsSEt s o; NoNCtRCUtAR CROSS SCCTTON

Check il thc strcngthening I'actors apply:

L, t4V

: 1O = t.lZ Ct = 0.99 and C2 = 0.99

L, 14

h = i= 1.17 Ct = O.62 and C2 = 0.68

Shengthening fagtors apply to both short_side and long_side.Calculate the bending stress at the midpoint of the sliort-side using Eq. 17.4

ts,r,=ffffil' rrrrrl - ozrfffilro.el(Sa),v = 2280 psi

^ Calculate the bending stress at the midpoint ofthe long_side using Table 17. l,fust equation:

/c, - (150X0.5)(lD2f .- I + (0.6042)r'l'""' - D6lEl5?i) 1t': - 1; fi,ai |

(0 62; = ae5e o,'

Problems

17,11 A rectangular vessel of the cross section shown in Fig. 17.3c irconstructed from 5A-516 Grade 60 material. The design pissure is 75psi.at a design temperature of 300.F. There is no cfusion and fullradiography is applied at all weldjoints. What are the total stresses in tholong-side plaies and in the comer section using the method in the ASMECode, VI[-1, Appendix 13? Dimensions are as follows: 11 = 0.75 in,;a=3in.;L=6in.;h:3:[il.

Answen At center, ,t = 14,100 psi

At end, ,S : 1480 psi

In bend at 26.e, S : 10,720 psi

I7.IO DESIGN OF NONCIRCULAR VESSETS IN OTHER CODES

In addition to the ASME Code, VI[-l, design rules for noncircular pressurevessels are contained in other design codes as well as in various textbooks. Inaddition, empirical design rules have been developed and used for a numUer of

l7,lo DGSION Of NoNclRcutAR VESStLs lN OTHER CODES 627

vcurs based on dellection and burst proof tests Among those design codes lirr

l';;";;;; ulrr"i, *" the Swedis'h Pressure Vessel Code and the Llovd's

il"*'.i"' "i

ii*p*g n"r"-"1'*i::l"T",i ;$,"%il'ni-":X',"*"';1ff #:1':,1

Lrl structural ftames, spectnc appt

luro different.

l7.lO.l Method in Swedish Pressure Vessel Code2

(i)ntained in Chapter 18 of the Swedish Pressure Vessel Code are rules and

il;;;t-f- ilGning rectangular cross-sectional headers subjected to intemal

:ffi;";;;;i,h G ,ut"-ttti"tn"" of walls on all sides' There are no rules

i;ff;5;it ffi ;tilerent watl thicknesses' when the wall thicknesses are con-

J;"i, ;;;i;;; ;iu"n for ttre st'"ss"s in both the long-side and the short+ide'*i{;-basJ;q"^u';

for the long-side from the Swedish Pressure vessel Code

is

;=(;,-&*6One term in the denominator is the membrane effect and the other term is the

t "nOing

em"ct. Substituting terms from the ASME Code' VI[-l' gives

hs*i. = I ^ =; 2: €n 21 = eb K = bending moment tenn

100 for kilo x = d

Substituting these terms into Eq 17'rg gives

P- = (z' '2s \/'/ *i;. +1hKtr'

Rearranging terms and solving Eq' 17 45 for S gives

Ph lta 3hK\s=*\*= " )

lf e- = e6 = E, F.q' 17 '46 may be simplified as follows:

s = Ph =

(td. '+ 3hn- 2Et'

The basic equation for the short-side ftom the Swedish Pressure Vessel Code

is:

(17.M)

(r7.4s)

(17 .46)

(r7.47)

Page 325: Process Equipment

628 VtSStts of NoNctRcutAR CROSS SECTTON

p _ /100\ rz

s - \;i '^,Jz ! 6^k/4

Substituting terms from the ASME Code, VI[-l, into Eq.

p /)\ tz- = I:lS \1,/ t/e^ + 3hKfe6

Rearranging terms and solving Eq. 17.49 for S gives

( t7.48)

17.48 gives

(r7 .49)

(17.50)

(r7.5t)

(17 .s2)

( 17.53)

(17 .s4)

'=#(*='+)If e^ = e6 = t, Eq. 17.50 may be simplified as follows:

s=#e+3hn

The various values of K are determined as follows:

Midpoint of long-side:

K^: \-LA--rZd

Midpoint of short-side:

KN:q-ttq-z

Any point y. from midpoint of long-side:

K^,: K.- o.s (Y-)'\m/

Any point n from midpoint of short-side:

K^ = K, - 0.5 f)-)'' \n/(17.55)

Example 17.12, Using the Swedish pressure Vessel Code formulas for nrectangular header, determine the maximum stress at the midpoint of both the

I7.IO DESIGN OF NONCIRCUTAR VESSETS IN OTHTR CODES 629

krng-side and the short-side of the rectangular cross-scctional headcr givcn in

lixrrnple 17.7.

Solution. Design data ftom Example 17'7 are as follows:

h:14\n. H = 7.25in' P = 150Psi r:1'0tn'

:H =7 25

= g.51g E:1.0h14

li)r the stress at the midpoint of the long-side' use Eqs 17'52 and 17 47 as

li)llows:

K:K^=

s _ 1s0(14)(1 x 0.5_1_8_-t__? x 14 x 0'250) = 11,570 psi

lrortheStressatthemidpointoftheshort-side,useEqs.17.53and17.51aslbllows:

K = K^ =(o.s18f + 40.s18) - 2

= -0.116

s _ 1s0(14X1 +_1lj-_lj x (0 116) = 6170 psi

Problems

17.12 Using the design conditions for the vessel described in Example 17 12'

if thJ same cross_sectional area is kept but the cross sectlon $ square

iort*A of a""t-gular, what are the maximum stresses at the midpoint

and comer of thJ side using the Swedish Code?

Ansrver: Stress at midpoint : 4560 psi

Stress at corner = 8370 Psi

lT.l3ForthevesseldescribedinExamplelT12'what-isthemaximumallowable working pressure for the header if the thickness is increased

tot= 1.5 in'?

Answer: MAWP = 600 psi based on the stress at the corner of the

short-side'

T

Page 326: Process Equipment

630 Vl33tr3 0F NoNctRcutaR cRoss stcTtoN

17.14 A vesscl of the dimensions in Example 17.12 is made from twosections welded along the centedine of the short-side. The weld iointonly visually examined and no backing strip is used (E = 0.70). Wtare the maximum stresses at the midpoint and the corner of theside?

Ansrrel: Stress at midpoint = 8810

Stress at comer : 12,530 psl

17.10.2 Design by lloyd's Register of Shipping Rules

Rules for the design of forged, rectangular cross-sectional headers air givenChapter J of Lloyd's Rules. In order to use the rules, the header has\i conradius of not less than 0.25 in. As with other desisn methods forcross-sectional headers, stresses at the corner and in the ligaments betwecnopenings are examined.

For an irregular pattern of holes, that is, one in which the spacing betweenop;nings is variable but the opening diameter is the same, the ligamentefficiency is

The method used to detennine the efftciency of ligaments between openinglis similar to that used in other codes except that Lloyd's Rules permit coniiderin'gthe reinforcement area in a welded tube stub as giving a smaller equivalentdiameter. Without welded tube stubs, the hole diameter is used.

For a regular pattem of holes, the ligament efficiency is

p

- p, Io,-ZdL =" -

PtrpzFor an opening without a tube stub, the hole diameter d is used. For an

opening with a welded tube stub, the diameter used is the equivalent diameterd. determined by

d"=d-LT

where I = nominal thickness of shell or header (in.).

A, = excess area in tube stub over that requ ed for internal designpressure plus area in attaching fillet welds within perpendi_

l7.lo DESIGN Ot NoNclRCUl'AR VESSELS lN oTHER coDts 63l

cular limits measured from the vessel surlace of b = {7L'where d, is ttre actJ op"nin^g Aia*"tet and

'd is the nominal

,fti-.tn"t' of the tube stub (in'')

Once the ligament efficiency.ls determined from either Eq' 11 44a or F4'

fl.+S, th. valie of K is determined from

where S : allowable tensile stress (psi)

P = design Pressure (Psi)

E = ligament efficiency

'l'he value ofA/8 is then determined where A = distance ftom centerline of hole

il;#;;;;";;,uaio' -a r = ditt*"" from tangent of comer to tansent

of corner (both in inches), u' 't'o*n

in Fig lT l0 Using the value of K' enter

lri.'"..iiJ" #i;.;t. irj"'ii ""4 ""'JJlvio

the.value of A/B'Readhorizontauv

ro determine the value ot 'lo' 'n" uJui of r' the minimum required thickness'

H;"ji.i;',H*1""a. fi," "Au.

of r tnitt U" greatel than t. [f the values are

uDart. the value of I ls reduceo und th" pto""doi" repeat€d until the values are

cIose.

Example 17.13. A rgctlnSlr| doss-sectional htd:t -lt-,*t]t

using the

Llovd's Rules. The header rs I :]in' -square

wittr no ftbe openings' The allow-

abli stress of the materi* is rs,o0O fsi':oJ th" d"tign pt"ssure P equals 150 psi'

ffi"ij, ,it" rnrnrfi required thitkness of the header?

Solutinn

SEx=V

(17.s6)

(17.s7)

(17.58)

J = 1.0

K=Y= lfiH = rooo

4=o anctB

tB

0.056

B:7'5-2(o'2s)=t'or = (7 0X0'056) :0 392 in' I

Example 17.14. A row of2-in' diameter openings on 3 5-in' centers lies along

Page 327: Process Equipment

6t2 vtgSlrs 0i NoNC|RCUTAR CROSS SrcTtoN BIBTIOORAPHY 633

A/B

E3333SB I 4 = 0.s0B

B

1 = (0.23)(7.15 - 2 x O'25) = 1.668 in' I

Figuro l7.t0 Rcclongulor hooder thickness r K

Rssisior ot shippins) 'aquiremenis for tlovd's regisr€r ot shippins (courl'elv Llovdl

the centerline of a header that is 7. 75-in . square with 0. Z5-in. inside corner radii.The material's allowable stress is.15,000 psi -a tf," J"riln f."rr*" fSOO pri.What is the minimum required thickness bf the header?

Soltrtion. Calculate the ligament efficiency as follows:

^ 35-)E=::_:____-::=0.42g6

Calculate the other properties of the header as follows:

r = sE

= (15,000)(0.4236)

P (1500)

I'roblems

17.16 Using the Lloyd's Rules' what is the minimum -requi-red.thickness

of a

' "^" ;J";;er'with 0'25-in corner radius and 9-25--in' inside wall-to-

i^l;i;;;;"rtrl" urro*uur" tensile stress is 1s'000 psi and the

desiqn Dressure 1800 psr' One side contains a row of openings that is

i.o-in. aiut.t.t on 3'b-in' spacing along the center'

Answer: t,ni,, = 1'75 in'

u.lTwhatistheminimumrequiredthickness(withinl/16in')inProblem17. 16 if welded tube stuus' are added at the openings? The tube stubs are

1.O-in. inner diameter uy O ZS in' ' tttict anA aftached by a 0'25-in' fillet

weld.

Answer: t";n: 1'75 in Cannot be reduced to 1'625 in'

REIERENCES

l. Lloyd's Register of Shipping, chap J' "Boilers and Other Pressue vessels"' it Rules and

Relulatiotls for the Co structon and tlassirtcaio of Steel Ships' London' lg72'

2. Swedish Pressure V essel Code' Calculation of the Strength of Pressure^Vessels' Publication

Series A No. lE, Swedish ttessure vessel Commission' Stockholm' 1967'

r, tiJg"t, o.", w ., DesiSn ofwellments, 8th printing, August 19?6, James F. Lincoln Arc

Wetdog gounAation, Cleveland' Ohio' 1963'

BIBTIOGRAPHY

Allovlable Working Presswes--square vnd Recnngular Headcts' Rabcock & Wilcox' Barberton'

Ohio, 1950 (private communicatlon) '

Roark, Raymond J. ' andwaren c Young' Fom ulasfot Stess and Strai'' 5th ed '

Mccraw-Hill'

New Yolk, 1975

10865432

K

AIB

0,30

o,m

0,15

tlB

0,10

0,08

0,07

0,06

0,05

= 4.286

Page 328: Process Equipment

,!t

APPENDICES

635

Page 329: Process Equipment

APPENDX AGUIDE TO VARIOUS CODES

GUIDE TO ASME sEC. VIII' DIV' I

ffibv ft e Am€ricon societv or :l:;1ffi .'liJi"l

H;:ij,'"3ill:"1il'.f;".)'li i,Li; lill iH' Lv ioo'z''o'n'"'i nn''""'' e

l'Jll"i'i,J-*it, ""** ins' De'' \ela \

1r

illt

I

IIil

u

tl

ll

G l'"*;+.r*, ":"1ili*d,*:1. -,,

**iir:'**';*:.::, qgt:l.l**"

fu|.fu4'A*dirr'.'cu^nno

Lill:;ll;T;X;'i: 'lif;f;l'l' . ,' ,"'

'3,S'11i1"?t1'**'

Is:s''x: ** : :i;'-T,l'j'i-Ir"? *.r;l*"t+lg;_:'tiix - ;$l;::J: :*,*::"";,";.*.1;t;," _" ., ;;;;i*i-.6 D -'$

'$ll r';:*::r;-J T:. *,- ,".', ",.

:5:.:ji:s Jil:Ti;

637

Page 330: Process Equipment

GUIDE TO BRITISH CODE BS.55OO

J. W. Strowson, Oil Componies Mqleriols Associotion, London

Fisuro A.2 cuid6 to Brirish Cod6 SS.55OO. (p,rblirhed by rhe Britilh gondords Insriturion, 2 pdrk Sirser,London WfA 2BS, co{r.t sy ot Hy&ocatbn kocessing, De<. lg7'.)

sb,ve-J'.tNol..

taen tftu*) 6on- 35!

GUIDE TO A. D. MERKBTATT CODE

H. Steffen, Vereinigung der Technischen Uberwochungs-Vereine e'V''

Essen, Wesl GermonY

ffi cort HeymonnsVerlos KG, Gereoftrr*!€ 18-32,

o-sOm s cotogn", F.derot Republic ot Germ ""i' i3,'n- a n'***bon Prccessins' D* 1978')

lB:i'",-,..*'

^o.B?- rr.iriLon (o!u{n rdrcn

1,---^-*--J:l

tribi (,dud) dm

-aos2

^D.s3- srh..ic.rt d'hd

ii*ri*;;'::m*:::::*l3:llll"ft-*-^"""""

i'drcnit G!-11:::PEumia Gi

-aY-:.-:

P'oo' rer .ea.:

r#r:g:'liJ.Tffi:ddd4e/od_ - -- '::;:;

11 e B lf$<

:liEEry,.+LEg I

-",..::::",""tmFFif

"."f.";Y'

639

Page 331: Process Equipment

GUIDE TO DUTCH STOOMWEZEN CODE

P. von Rossen, Diensl voor hef Sloomwezen, ,s-Grovenhoge, TheNetherlonds

sE'9.|4-Geo'12!)D &h'c. ri.

-G@oqn)..1.' [h -oo8l?!.o..0|

etn-oo.o3{10'd)

hl.|plpic-6@013e|

sd..! .,,,i.1 F*. -.""

?9Tt

ssdd.c @ido3g1l,.

gtigffiuwTrEedm 6Fi^ll strlt.l'

eli, rxvl.vi|.

F.DrD _Ooaqs.|[email protected],o7oi

fisu.6 A.,{ cuid€ to Dukh Stoomw.zen Code, (Published for rhe Minisrry of Sociot AfidiB [Di€nsr voor h6rStoomwezenl by Govornm€nr Publishing Offico, Chrisioffel Plonriinsrroot, The Hdgue, N€thendnds; courbiyol Hydrea$on Processing, Oe<. l979.l

GUIDE TO SWEDISH PRESSURE VESSET CODE

l. Berglund, Tryckkirlskommissionen' The Swedish Pressure Vessel

Commission, Stockholm

Fio'ire A.5 Guide to Swsdi3h P'e$ure ve$er code (Published bv Trvchkkorkkommi'3ion€n lvA' P o Box

l":ti. l-iti;;1.anorm, sweden; courtesv ot ttdrcnrbon Prccessins' DEc teTa')

lo,5-xozh..dorc.h.d

l1rli?..-i,-",".'--)

:ffll"

-i;;' i i

id,.,",--d--1'1.

*f;?sl;ffi!ft:x'.,Jffi fi ;;,."",-..,.-_''.,,

*'-""---- ":::7"

H:H l*T'":il -,"..?,r

"x

il

nnd.bl j ;;;;

ilT:I$ll;:i X;1;1

'"' Sf{*,.*if :i#lBffiil$rj#'1fiilj{ffilljlf;3$C*{E"F}::#'3'ff:U'ii

640

&1

Page 332: Process Equipment

GUIDE TO ITATIAN PRESSURE VESSGT CODE

R. lV\ozzoncini, Brescio, lfoly

Fisu.o A.6 Guide to ltolion Pres5ur6 Vossal Code. (pubtkhed by Co3o Ed;rrice tuisi Di G. piroto, vioCorFlico, P.O. Box 3680, Mifon, lt'j,ly 2468Ar <owtety ot Hdroc bon pro.essing, D... 197A.,

GUIDE TO JAPANESE PRESSURE VESSEL CODE

M. Koike, NiPPon Kokon K'K" TokYo

% Ab'irvoku Yo'iki Kouzou Kikohu' bv rhe

Fisur€ A.7 G!i& ro rory:a P:'*:"::::;;iln s-ss-r st'il'o r^ino'o-Ku,Iokvo, roPon' courtesv

r.rinirtrv oI I'obor, poblish€d bv the JoPon borrc

"l tlioeorbon processns' De' 19741

rird ,itit

-r,r.o2

wdd oFrir

-v.s.R.r.t,s^l.t.iob-v.s'i''''i

rrntu l'-G.n Bbi

-v5e.r.F.3

atu6,d rul.

-s3

r\

Ia

ffiur. w.rd loiir or.9

-s

2'0 I

".!-$ll'#:'""'"'-

-a1..=1e-lAH{H'rud",.;:.d.;;i#6i."!-?o?1r"

-

tt \=lE!-T

:1-- l,llx.li'" ---."r{; iEEi'i' J Xl ;":;-.-, -""- "

I=IHH ::il'H*4fi' iX'bF *t;;* :tt'i= Ifr;;u^d o{gd-nt! '5

5'.".--'' .rdn.lor.u.--4rie

g2&3

Page 333: Process Equipment

GUIDE TO JAPANESE STD. PV CONSTRUCTION

M. Koike, Nippon Kokon K.K., Tokyo

GUIDE TO JAPANESE HIGH PRESSURE GAS CONTROT tAW

M. Koike, NiPPon Kokon K'K" Tokyo

Figur€ A.8 Guide to Jor,ono!€ Srondord pV Construction. (JtS B B2tg-IgT?, pubtished by rhe JopcnSfondor& A5.o€iotion, 4-l-24 Akcoko, Minoto-Ku. Tokyo, Jopon; courrery oj Hydrccchon pft,cassing,D€c. 1978.)

*l;::l:$:'J"T:J:1hiu:rrv, poblished bv th6 In3lil"le tor wr€ry

Hvdrocorbon Procassing' D* 1974'l

hi.rn6 ridi.l r.gr

-

3 2..tr d.D .nrni rtur

- i45..5.t

.r. -^cj.cd.F

not

cod,|6imn.!-..''4|

Ar- sor

-arrr

Lndb tdl6t ..en

-4r,.r

,hr*'u itund ,'uur_r4{,

Mrr rndrbb *dit p,[*r-t3

1?

-rh'cri..n.d..r tru'.

f-'ikhd{n@.|pr@[

2c-^di.c-r oP-r.lt

i;;;;d;F;'-,.,55

^r.rt4. t22r

rrx30.. t'dldr d'd -ir'tl

'nfi|*.i.n.''i.@-..

rhddh'dd9.dd.-1.thB|lA.eij'.d.-B

-rN?,*l'il lJJt::l

T-ffi;liliiffiPF-.J,ffisqstud. l\

r2..1-r'.n|lM (r.dd) d4

12 -senrk

rv dbH @

n::,ffi;u:--"*.'. ii:}i:F,s--- ";flllf:i"---------;lifuol4[ch( Ej-.':;f,ll*1i:!l-=--'tu:;;:: '{i=----------=1r'

d44645

Page 334: Process Equipment

APPENDX B

SAMPLE OF HEATEXCHANGER SPECI FICATION

SHEET

u6 47

*n ." ot,t.,uluto, ,xchongsr Monufocturerc Atsocialion' New York' N Y'

HEAT EXCHANGER SPECIFICATION SHEET

fi:--swc- ttNGrH Plrcrr

Page 335: Process Equipment

API Strndrrd 850Stor.gc Tlnk Spcctllcltlon Dlta Shcet

sh..t 1 ol3FlL No.

hlvnlnbn (!Y Ptt!at-.)

Phdic _---

APPENDIX

SAMPLE OFSPECIFICATION SHE

|lLr ta! ol P|.'

ib ._-- T.t* C.FdtY (t'll:i.||.r h bblfir' ot

-.- Dlfi.

h.r.Ung T.inFnur.

|{d $rdld.le

D-igo s!.dic Ot vlty

-

@lF(.d

fb.fitC Rool APg H

hoar5 Yo

-

t'ao --tod.r Unlto?rn t r. (cdt ld.t tGY)

Lo.dkE (p|oYLt

frdgn par APP. E: Y- --- & ---lo.r. (Fle. E.t)

tL Bod! (3.10.4.5): Y.!

--

l{o --_X pllllcrddr Fer O.dctlo.llld.rll (T&|. E 1)

L.d: V.lodtY (m9h)

h ld.dn dllt $finddit r (a!F 39.9):Yr--t{o.-_h. F ht.

Ethclr: Ftrll, m.t"

Dbnatar, nur,rd/or 8.bin Rdtena

l,t i!i!. rs.Co|EtL

u8

Court$y ot lhe An€ricon Pelroler,m Inslitur€, Woshinglon' D'C'

g9

Page 336: Process Equipment

ahrt 2 0t:Ff. o.

8h.at 3 ol 3

Flh No.

Conalnrc on On I. (!t ttrutotur., rnr'o, Frxdr-r, ar ^tDtb!b)I Manul&arcr

-

Clty

Clly

$araS.fial tto.

2 Fabrlcator Flulh-TYP.Doof Stt..t ( PP.

lrllold Htlcrr grcton [email protected].

- Top wlidgirdr (r,rc .r ritr,ory): y.! _ l{o _l0 Rool Typ.: S'.Fpo.iad S.tt.SI

Ya!

-

lil,o

-

Ittamd FY,D.: Swlno U|.iaadne Co{ Stltt F At riooi Ddn: no-li.ll Mrnw|Y.:, i'lo. Jd E2c

hr Mrflty!. llo a,|c Si.iiru [:rJ ta- ttg. *8, ]5, s€,

"d r'bb! 3€ ]e

'r'd ]10)

ll Fd rbrd.. (lidt *t v.ilthe od'tttdotr) (s.. Flg. 3.4 aid &r5 itd T.blc &t6 'nd

$t4

S.rhl No. aq, ll.3 ri,hbdll Sp.dnc.tdlj sli.I

FoolEolio.n6'nrictudsSlioll Coul!.. (no. ot)Ads rudh rnd ntch6 (hdulng conBdon dowrnc.Ia

7

t Tank Bonom: ptata litdsEaa

7!c

Scrmr (cli.d( one) _ hp _ dr,Slope

Bottom Annutrr Pt !. tfin. nb$ arld ltkrot- (!..Root to Str.ilO.rdt: Ftg. FlIrbm.dhi. Wirdliidrr: yG _ t{o

--

Phb20 Pud[rar,a Ratafaica Drar,ttg2l T.nk SLc: Dtr'l| tar.nd |htght i, tt.&| O.!. ot €dt0on or R.trton ot Apt S||rd]d A5O

h. p.r t C||.d( q'l.: To-Fto.r_caot

l?

Slop. or R.diu.'It R6t ptrio: t chr€a

Bur Joh

ll T.nk Bo(brn Cofdnt: ht do..yaa_ o _,itd.rldApplb.tio.t Sp.dtb.ton

la Prhi S-tn cturlt S.tr.t tih.-yar _ o _ eir{or.y.r _ Lo

16 lfiFdion By: Shogla lvcld Ellrn|mtonr R.dofmph

supp|.?iantary uquld parFarai or ultarrict7 Fllmr

--

PDp.rty OIt L.rt T.'dllgr Aotb.nSh.ll

lg iilll T.d R.porb R.qutrrdl

650

l{ot.r Stadl atd/ot aaDatn Ji"t ttr|y !' d'dr.d b cov'r '9'd'l

nqulrmcnt3

651

Page 337: Process Equipment

APPENDIX

SAMPLE OF PRESSU

Pressure Veesel Deslgn Dsta Sheet

Bcagr.4s$c!

cepaclty of v65e1:

de.1e! code: rSrc Sectjon VIII - Dlv. I

coD3tructioo:

Skeich and Genelsl Dbenstone of V€6se1

ec.ktns pte6Bure: ----l?!- P"18

rorka!8 !.aPe!6ttrte: ;:P9- deg' F

<cilos1on allol'ance: 0.063 bcrl

4-lnch outlet ulth r€tru.n8 neck fl.nte

3€ao1e$ di8heil head, !re3€u!€ oncorcave sld€, unstayeal

8-iD(h outlet wlth la! loinrflaige

sPeclgi cast 3tee1 oeldlng

Epeclal folted Eteel bllndflente

:-1./2 lnch blosdoh ourlet rlth reldtr8

Uateltal Speclf lcatlon8 :

latcllel sP.ct!1c!tlon8 E...1orra lUooable 6t!e56!No.

GlP.No.

sA-204, &ade ! 17,500 P61 abl. ucs-23 3 2

sA-215' ctade I|cA i5,000x0'8=12'000Tbl. UCS-23UG-24(.) 1 1

forAlnS6 SA-181, cla.€ 70 17,500 Tbl. ucs-23 I

bolrl[g sA-193, Crrdc 816 20,000 rbl. ucs-23

PlPl!8 9A-106, Grade B 15,000 Ibr. Itcs-23 1 1

l/16 lEch asbe3to6 y-3 ,700 Fz ,75 Tb1.2-5.1

653

Page 338: Process Equipment

.10ata

Ihdgn ol Hord and Shell

th.lt lttcta...! !c-27 (c)tltl. dDlEl! r.qrd lhtcb.tr, !. pt

fsb-:-id' 5P-t

APPTNDIX

Dectgn of Head and Shell (contlnued)

atrrl rir'\?IiSdli-ffi6j:io-fi-3E - o'7e1

|ild coEo.lo! rllosroc.s ,?9t + .053 . .8j4 ts.Z. Cb.cL pos! rold hcrt !t rtDtsr rlit r.dtoSrrpb rcqult sllrr.

VCS-56, Ib1 I'CS-56 [o!. O)(r): port e!1it b!.t rrcrlE.lr r.qul..d lt.ac.!dr 5/3 t!;b.c.$. 0.8500.625r por! e.:.d b.rt !r.*!!ar t.qulr.it UFfI (a), IrCS_j7cf D$-52): r.illotr.ph r.qstr.d t-3, Cr 1, 2, 3 1f t> O.?50 r!.;b.c.ur. 0.851D0. 750 rdll.ogrrpby tr !.!ulrcdr.crlcuLtc tl{cbcrr rrqut!.al orb8 f - 0.85 (rbl DT-12, 3Eot .tr6b.d)t + c '?ir-s66++=ii?5ir .ll'1,.,1'lll.Ll"l'l

;.i#c$.cl |Ppltcrbltttt of foinutr: UA-27 (c)(1)0.385 sl - (0.365) (rt500) (0,85) - 5?2Oi 525<5720 forsutr fi0,5r - (0.5) (18) - 9.01 0,750<9.0 JomuL of,

Aud frlct!..s: {EG-3ZI

l. l dlrhld ie&! dll b. u..tt, !C-32 (J) r.qulr.r rlrt rb. tl|taL buckh lritltrarh.lll bc not 1,..r ri& 6t of rh. ou!.td. alr"o.tcl ot th. .t1!!, lor l.t. rha!tbr.. ct!c. th. h.|tl !hlct!.ra.

^lro, rh. b.l.dc .touD E.iHtlt l. ro Dot .r-

c.ral !L. outr:litc (tt6.r6t ol tbc rldlt, lhur lsy:llaill. crorrn r.dtr[, t - 27 i!.<37.3t5 t!.llllde l lcllc s.illu., Ir 4 tu.>(0.06 r 37.375 - 2.24 r!.

lh. chcck Ernt-Erd thtchlis: !G-32 (b)t'

"ot. Joint lfflclencv of 0'85 b€tt'en head '!d 'he11'

post s'ld hcat ti'at'd

double_buitaelil fot th' c1lctDfetentlll lo'!t: U6_32 (f),r-_ltrio' rc:rl lr-EEfuu _' F | 'dn.0.3l8:"1a' 6:E5 iii--mo-ii=iclFsrt '

(..rtir!e 8 - 0.?0, Tbl $t-lt(doubl. e.ld.d bur! Jotlrt

0.318<0.68E, thlckneB6 oR

3/32<0.688, thtckn€38 oK

check t!1d'lEi instde lnuckle iadlus! Uc-32 (J)

(3) (0,688) . 2.053 'a'd->2 053 knuckle ;adrus 0&

cyundlr.cal 3k1!t: rr,l-13 (a) 0.688<(1'25)('750)' 0'937

A cyllDttrlssl 6klrt b o9llorlat for Ehe h€'ail butta€lded to the Ehell' t

rangeot of 1-112 In. 1e4!h l'tll be used to Provide a b€!e1 fot the butt

e.ld, lbtu uU1 rvoltt cultln8 th' bevd rnto the L^nuckl''

Skctch;f h€.d lnil 3b€lL shotdng ?llDcipal dlo'Dslo!! and to!'!3nc€'

(!) v.3!cl to bc Po.t e.lil hclt t:clted !t 1]'00'F fo! 3/4 hout

(b) drxl.'tE Dclrtu.1bl. off.et of ctrc@fe!'nt1a1 JolEt' ' 3/16" (Un-33)

(c) .Pot cxllllitloE ot e'ldcd lotnts Pet UP-52

@ 3/32" rclnfotctEg bc!d: w-35 (a)' u{-91(a) (1)

No of!r.! P!.Pst!t1on n.cc!.mv bett'en hcld ind sh'll b'c'u!! thlckltlt'er

do no! illff.! bv Eolt lhrd 1/8 ln' ux-g(c) '

tllcbcr. r€qult.d: lrA-a (d)I -

---!I!--(2SE)-(0.21)

t + "o={i3t}*32}={i:4-rzsr +

- 0.568 + 0.063t + c - 0.531 thu.!or. gr. h.rd phr. thtct!$r of 0,688 b (tt/16)

frd Ucs-16 (b):

1e

a . 1.00 fot rcalcrs t.rAtot LIt - 2114 - 5.75,

x. r.4o (tbl D^i.2)0.053

th.l.l. lulfrcG of h..d 'hrU not d'vlrtc

."'.-ir'i. lltO" rtoD 27'r rrdlus uG"81 (r)

I r-r/2", b.v€l 30' fo! $eldh8

Page 339: Process Equipment

6t6

Data Sheet for Relnforcement Calculafions (UG.3Z, -40)

She1l -€r--s€.d- (€!ecrfv ld..crlption: (Iontltudhal butr Jcl.nt, dcJbte eelded, poEr vetdnear treaEed, spct fBClotraphy)desi'" pr66'ore ........,,"....,.,....,,. p 5_gll!tlJo1!! err1c1€ncy ..,.. ...,,...,...,,..., E lu5!€*lDLo alloeabte slres6 . !. i . .. . ,. . ,

corlo61on all@encellBrde rsdlu' .'

"""t', "- r".-,. .;';;;:.",'..';;;;-;;",.';.,,."-*a€+{+ (s!€clfy) befolc coiloBion atr.D@rnal,h1c'.!e.6, .,rc''ii.ve of ".,.J::':,i:,:::'.1,.1..i:: I #*bhlEle lequlred thlcknels (!efere.(€: U6-Z,) ... .....,.... ._ ;;;

" -

rsr-;jta-o€xce8E thlckDea€ ....., ,...........,. r_t_ 0,137Norzle

tlalertal uEed: se€lless s.eet pt!€, sA-i06. clede B (s3h 80)toaxlD@ aUorable 6t!es3 . !.... <,.. ...j.n'l.e ittuere! of lblshcd "".,r"r r,.;,"r"; :"";r;;";'...:: :tr*ndlnal thlcksess excluslr€ 6f co!!.€ron 6Uoasn4. . . ,.. . .. , . r 0.438 in.thlcknese lequlled for hrrp.Ere6s ,U"-rtl ,.....,......... ,_] ;;;

tTPR.

". -

GE :{ol-:?r - ar*-ra-3fii3#isi

3. sk€rch of le1nforc.€Eepr ,:rh dto€nslors 6id seidlns deialt (W_15._X5._1E.1

2,

rn= O.l3b

Y6 -- o,2q3

5tfAPPENDIX

Relnforcement Calculatlons for E Inch Nozzle

r. R.1afore.r.!t lcqut.d: Itc-37

A - (a) (!!) (F) - (7.?50) (.550)(1)

!t trl colslil.lctl !o h.v. t.LDfolc1ng vrLu:: !G-40(d)

A- ' s.t..l lD th. 3h.Il . l! th. not!1c eru elthto lh'-f ;i.ii rlsll thtcb.i. rvrtlibt' fo! r'lEforc'E nt:

.h.11: (15.50-8.525) ('r37)

Dorzr!: (8.623-7.750) (.137) (15,000/17'500)

(cf ttc-4b)

A- - Ectrl' ln th. aotrl. rlll oultlil' th' 'h€11

!btcy!!t3' rv.ll.bl! fo! r!bfotc@'D!:

(.438-,$e) (2) G)(.43S-.139) (2) (1.s95) t" belo' for h

A- - r.L1 ritil.il .| t.i.3lorc@cat '!d !'trt b 'lircbo6t

- rililoil tolaforcrocrt (U2 Lach Phtc' 8-5/8 :D bv 14-5/8

oD)

(.50O) (r4.525-8.525)

o4-belt tnch fuU ftU€t s'ld! 'losad

o'rt3fi! ofi.raiotcf"g Plrtc .!il srolad noztlc srll:(.50) (.50) (.50) (4)

3. Ifdth ol .!.s of t.luforc.DcDt nolEil to v'sscl nrll:

oc-40(e)(2.s) ('587)

(2,5) (.438)

ptl,3 .dd.d -.1ofo!c.ocut

4. sr@rtY:relDfotcco.!! uacdt

Al: sli.U r[a aoz . .....".'""' 1'045

Lz'

^ . {.260 r.. ln,

- ,942 3q, rn.

- .103 3q' ln.

\ . 1.045 so. ln.

At - .J9Etr x. i.r.

:-:913-cs.:-$.:-

.3.000 rq. 14.

. .50O .q, b.

4: - g.soo 'o. b.

- 1.720 1D.

.1.095

:-9=!9qh - 1.595 (th13 toverD6)

aorzle ............,".,..""" 0'954

.ilahil letufoic.o.rt rod ttclds'. !:Ega aee g!LEgLl@{'

Page 340: Process Equipment

658

Attochmcnt Weldlng for 8-tnch Ouflet (UW-fS, -16)

lllo!.!1c .t!.3!G6 1p vc1d6: (Tbt. Un-lsJ(!) ccabiDcd 6at rlit 31d€ loadLlt €rr.s6 1n brrt ,.1d6

(17500) (0.74) -(b) cmblned .[d ind s1d. lo.trlls 6t!!86 tD flllct eeld€

(17J00) (0.49) -Strhrth of l,l€1d6:

(r) outer ftuer s.Ial b.tr..! ves6cl ratt lDd r.hfolcbg plar€6\ 04.62512) (0.500) (Es5o) -

(b) butt rr.ld b.tr..r v.sr.l r'ru .nd !6rzt! !'eU(n) (8.52512) (.687) (12r9s0) .

(c) f1U€! !r.1d b.tt'ecD lorrl. |!it r.lDforclDS phr.(1) (8.6?'s12> (0.500) (8550) .

(d) b!!! ultd b3rt'!.! aoz.tc ndl rlil t.bto!c!.!8 ph!.(n) (8.625/2) (0.500) (r2950) -

E$!:(r) .tt.!gEh 1n !.n.toD of rh. pL!. rroov.d firC-41(b)(2)

(17500) (.550) (8.6?5) -(b) .r!.Dgth of !.trt 1D vcrr.I rrtl .v.lhbl. for r.lnforc.r!.!t

(17500) (.137) (15,50 - 8,625) -(.) rclEJorc6!6r lord e.!tLd by rh! ro:rt.|'rtl

(15000) (2) (.438) (.687) -+ (15000) (2) (.2ee) (1,59i) .

(il) rclDfolc.o.a! 1o.dt c.rrLat by r.l.DforctoS lhtcE3!000 - (15,500 + 23,380) -

4. -9.w.:(r) 16.d !o bc crrrt.d !y rltrcb.it r.hforc.o€nr

E3,000 - 16,500 -rtr.Dtrh of rtt.clDllr - 98,500 + 120,500.

(b) lord to b. clrrlcd by lorzh ritl -atlen8th ol rttrchElDt -

(c) r6.d to bc c.Flcd bt r.hfofcllt ptrt€ -.r!.n8th of rttrclE.nt -

Attr.hD.Dr elldl[g ls lrtlsf.ctor?

APPINDIX

It-Inch Lap'Jolnt l'lange Attachment and Selection

r.l chcck tleldbg b'r'c'! noztl' rtrd 6h'11 rnd t'l[fo!c1!8 fo! '!r'rgth !o

I ot.h".^od hvillollrllc 'ril fotc'

;:;;; '""' 6t!c' LB butt .'']d' (rbl n$-15)

10,500 PE1

(u,sOO) (.60) ';.1;..;.; of butt r"1it (cf

'h!* 4 for drDdlloDs)

(r) (s,525) (.687) (ro'500) -

;'";..t".Dd !orc! to bslil' ilt'!'tet o: noz'rc

(n/4) (?.750)' (525) ':;:"'.;:'";;; ,.,u .'*'

'. *r' ro! b'd!o3t!tlc 'Dd

foic' rEr)t's ltd Flttrt'gs' uB' 4o0 l!'2, Fror A161 315.t192 srlrL PlP lt

!.!.il .! 565 Ptt rt 50' F'

FtoD vtti'6'! cttrlogtD,'!b!! of boltt.1t' ot bolt'boll cltcf ill'Dltct """"'""'

13 lnchli

,, o.. ;:;.;t 't!rb 'Dd' 8'625 oD bv ?'625 lD bv I tDchcs lons

-;: ;;;; crirl'os' ts' 1^5 ln' saskot - i2 rn' (D bv I tn' D

APPENDIT

l.

2,

12,950 }rt

E,560 ?.1

9E,500 lb.

1.20,500 lb,

38,000 r!.

87,600 rb.

831000 $.

15,500 11.

195,450 tb.

24,700 tb.

195,460>24'700 lb. .

9,030 :.b,

14.330 It.23,380 tb.

43,120 th.

55,500 tb,219,000 Ib.23,380 L!,

120,500 :.b,

43,120 tb.98,500 1!.

Page 341: Process Equipment

10.

d.!tr! p!G..ur! - S2S:rrna! d.318n rt!.!i r ]2,OOODort d.8tgn .t!€si . 2O.OOO

try 1.250 ln. Dl.s!t.! bott!,! root .!e. - 0.943 iq. tn, (8i e6rtEar. 8. . 0.553 1n.

WY

Itr@. lhtt the hydrosEatlc.n.t fo!c€.the sssk€r leactron, .rd

"-l'-1:.'lr*tl"' to 22 lnch dl&€re!' rle assue.rr. dcal&r hydros$tl" *.,;,;,;--';,:,:;jil,I,;;i"" " *" - T":t;;;;T"i;",'' :"ffi;:3df,?il,;ioi?o':;oii :Ti",*'" .'".,

3. elr2 - (Lr2)(0.s63 + 1.0) - .?82 (thlB cobP.rlB favolablv $lth 24)

4. fo! th€ crttlcat s.ctlon !t 15,875. ,.",o- "oo,"roro! ;;; rii.-iiii-tl,(,lj:'i:1,;,':.l;i(ii:ffiiiio.l.,";;

1",,.n ",5. Auo,ablc bott road on s€cior = (20,!oo)j0.443) "- " -'ir,ruo ]'o.nrn5. raBb€r te.ctloD - L8,B6o_(U2a\ G/4) (zz2) <szsj - 18,800 _ 8,330 - ,o,rro,*.n*,7. bendlEt Dooent at crlttcal lecrlon

cto

Prollmlnary Derlgn of tE.Inch Inregrel l.lrnge

APPENDIX

Prellmlnary Deslgn of lE'Inch Integral Flange

ll ,. ^

r/rS lnch flat aBlestos sasket HlI1 be us€d ' 19 lnch ID bv 22 I'ph @

z,

),

Flon Table 2-J.2t

basrc sasket Beatitts f,ldth, \o = G/z)(n - 19)/2 = o'?5o i^'

effective €€,sk t sea,tjns rlitth, b = (1'/z) -dffr = o'D3 rn'

locatlon of g.sk t load reaction' fabk 2_5'2

d= 22'o'2(o.4)t) = 22'o ' 0'866 G = 21'1?r in'

661

I B.crlon fo!f radlarh frary.

fi olcttca6K--hub

tly h r 3,00 1!.tly R.2.00 1n.

trrC.24,0in.

t?y 24 bolr!

2. c.nt€r 11n. bolt cilclc to hub l (r.j)Db _ o.j)(r,25) - r.8753, DlntltlD bolr cllc]e itl.ecrcr for !4. bo,, Bpaclna - g rn. or (2.25ror):'.;Xn; ]',:,i'li:.',r. nu!b!! of bot!! . r(21.0)/2.Er r 26,s

r. hub l.Drth, r, i-'JE . \\n r"-;;l;; . ,.0,,,

aI - 2.00 h c. 15.875 + 2(2,00 + 1.875)

- (18,860) (Ll2) (24,o - 18.438) - (ro,53o)(r/2)(22,00 - 18.43s)- 52,500 - 18,750 - 33,850 tb. tu.8. cdlcutatld thlck!rcse for taillat fl

12,o0o - (33850) /(r/" u.,rii.t,, JT'r]il"""' %' uc/r' (uA-s2)

calculatsd lhlc*ness !o! lolrglrudlnat nub 6E!.s6 (UA_52)(12,000)(r.5) - (33.850)lQ/5)(2,42r(s,2) :, e.z _ q,aar€v16e estbateit ftange dlDcns1ons usrirr

..t - 2.65 1'l.tryt.2.75 1n.

& 8I - 2,15 tn.

R - 1.875 1n A - 24,525 + Z(t.25)h - (3)(2 -.563) .4.31 .ay 4.50 1!.

- 24.625 1n,- 27 -I25 tn.

^ - (27,L25)

c - (24.525,

Page 342: Process Equipment

APPiNDIX

Bllnd Flange for l8-Inch Manway Flange

I,

u6€ 2-112 thlcls"63

663

1/4 tn.

!r@ uG-34 (c)(2)r t - a rld/s + t ' 78!nrc/sd3 ', F&' uc-34(J)

Fro6 shect IO: n ' 453'000 Ib':!'c' QI2) (24 '625-2L'133) ' r'745 16'

d ' G ' 21'$3 1!'B ' 184'000 lb'

3. rroD shcet 1: s - 17,500 Psi (sA-181 c1'6s ?O forSlot)

C - O.3o UG-34(d)

- 2.359

2.359 + 0.061 - 2.422rddlat cortoslo! lltotaoce I

5. Sk.tch of bllniM!!8'

2-114 b. dla., sPot face fo! Euts

I-5l8 lD. dla.

2-Ll2 La,

( 2r.13-r SZ

DESICT COIIDIIIOI{Spcrrurc, r- 525 pri t!op.!.tu!.. @!g.rr.., #'rat tqge.ro:. Fl"tD r z?'aD

lolgl.tudtral hub .tt.!3r S" - (fu) /(r.e

!!dl.el fLrs. .tr!!!, sR - (€x)/(!t") -

!raa6!t.l fhng. !rr..., S- - (nt/

a,zt6

AT,LOI'A3II STRESSES

II'IESS CAI,CI'IJITIONS

3,Zoo

Page 343: Process Equipment

1. sh.u ..-.fl..t-{ !p.cl fy)d..cllPtlod:

*:f+:+:i*tr!lsr,-_cr!!b""1d.d.,.,t ""1@,d..lar p!!!su!. ,.. .. .... .. ploht .fflc1€ncy

, ,.. .,.... EDrtbuo .llor,!bt. lticls ......,.,..... ,..,...., scorroslon alloe.rc.lDltd. r.d1us of .h.Il,--elr-rr-qr erora r.Cr--, e- .lsr,-^t.-n .Fh.-1o.1

---r.a&.-(!p.clfy) .bcfolc corro.io! atlorarc. 1. lddcd ..,,.,., a, L, K.D!oEl 1 thlchr.!3, .xclulive of corroslon ltloelnc. . . . . . . , . . . . . , . . , .

..Elnlelr !€qut!.d thtches3 (!.fe!cnce uc_27) .€! .hc.r 4 . ... ., ,... . t!

664

Dolo Sh€ca for Relnforcement Calcula ons (UG_37. .40)

.xc.33 lhlcla.us .,.,..r !_r,2. Nozzl.

lrtellal ur.d ! r.&t€.s ar..l plpe. 5A_106. clad€ ! (Sch 40)

APPTNDII

525 e.r.0.85

17.500 prt0.063 1n.

t8 1p.

0.687 ln.0.550 1n.

E :ri!ur! .11@rbt. srr.l3

0.137 ln

r.5.000

17,0 1n,

.500 ln.

.304 ln.

ln3td. dl.roete! of flnt6hed op€ing h colrod€d cordltlon . .. . ,.. .,... droElnat thlcltless a(clualv€ of colloslon aUorance , , . . . . , . . . , , . . . . . tthich.sr r!qu1!ed for hoop .t!.Bs (UG-27). ,. ..,. .. .. ..... ,.. ,..... . '

.." - rci:+fu:iltSkerch of lltnforceE.rt slrh dtuen6lopE and,eldlnr detall (Uw_15._15._18)

tr, =.SoOt-r.=.'b4

,60tl+ DIA

APPENDIX 66!

R€inforcement Cslculations for l8'Inch Manway

Alternate Method: Load Calculations Based on Nozzle and Vessel O' D'

1. roral(load i:r5!iliig,r'"- rld of !'rEfolcaleEt

'' ""'tfi.9i HTlJ:li",S:$,*'a or retiro'!c'eit

,.'.'""til,?i ?fi:l:;:li ii::tt.;'*' salr'!hlcraeE6

.. -* E*i"tJd ""-t. ".u['j..'i,;'e6su!' ln Dozzl€

(s25) (18) (1.72)

'. "'.Ti!o8i ?;;"b'?i:,;llo;i"'o' v'63'r r'au tbtckncss .

(.500) (z) (1.72) (15,000)

".''iii.!Li"i"ti,$l-;:llii;,'": :":":::*iio:iioi - is,iso " r.rzl'10,310+ e'550

t- Lo.it to b€ csrrlcd by rdd'd r'hfolc'Dent333.000 - 192'300 - 15'660iillooo - rsz'loo - 19'850 (h ' 1'72 1D')

8. Are! tcqul!.d of add'd !'b!o!c€o'dt124,840/17,500

StllDarh of lebforclacnt rdded(7,58) (u,s00)

tudth of 6ta of r!bfo!c'D!Dl' h"---"(i:5t(.e87) ' 1.72 1r' (Eh16 tover's)oa

( 2.5) (.500) ' 1'25p1u6 rdd.d '.*. ' l:ti

snlo|Al!road calcd.lEeil to hev' €t'1't€d 1n th' o'tal t"ovc'l

(52l) G7.37512)(L8)

StrcDAth ot Detal ,! vcss?l vall ivs11abl! fo! t'lD-

(,13?) (34-18) (17'5oo)

StlcEgth. of nozzle 'sll 'vru!bl' fo! reinfotc'ocot

'' -* :i.'fi"*"";inl',i'i:* rD bv 27'5 ,o'b o! . .-.^. ' 7't2 ta'Z'**ii"vi-il4' :ttt?l r'e1d6 ' ('75) ('7s) (2) (1/2) : +*16.l!_

- 333'000 1b.

. 192,300 ]!.

. 10,310 1!.

- 9,450 h rb.- 16,260 rb. cot!.

15, 000 h 1!.25,800 1!. co!r.

. 1.5,860 lb, .6t.19,E50 $' cor!.

. 124'840 lb. .5t.120'840 t!. cor!'

. ?.13 h.2 cst'

10. . 134,400 lb.

b E 1.72 1n.

38,350 lb.19,860 r!,

134.400 1b.str.dSth of rdil"d lctufolc'oc[t

b.cau6e the total 6tt'ngth trc€ed6hsr,e €:(16t.d 1n th. lcta1 r'oov'o t

lotal 6t!€$tth - I9?,-0!!-l!.the load calculated tothe il.31F 16 GatlgfactorY

Page 344: Process Equipment

c66

Dota Sheet for Relnforcement Calculadons (UG-37, .4())

1. sh.U or H..d (sp.cltv)o..cllptlonr dbh€d, 27 tach crorrn r.dlus. 4 lnch tpuckt€ rldlus

'' .rE!ffi:E - i-#-4j+Ar=-sEi

d.slgn pr.s!u!€ .,.,.............,_rolnt €rrlcr".cy . . . . . . . . . . . . . :. . : :::

' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' P 525 p.{lE'<ite .lro$sbte

".,""",... ",.,... :,'''''''''''''''''''''''''''' E

corlos1on ellorance . .....,.,.....,.. . .....,,,................. s t7.500 prl

rnsl.e redlu. or she11, o! ,,",." ;;;';;;;";: ;_.;;;;;"'.. c 0.063 h,

tphellca] radlus (!p.crfy) beror€ corro6r.or itro,aac€ 1sadd.d ,. ..... .. ,. ,. ..

H*lll"L!i";'i1"""1:'x;: ;:$": .' .: :: :: :: t'#*E ' r, !t. 1

uc-37(b)' uA-4(d) """' t! ll*

APPENDIX

Relnforcement Calculatlon for 4'Inch Nozzle ln Dished Head

'''"Eli?iL;?,:i"i:!;t':*ii' *ca of !'lhfolc'Dent

'. ..i::i!l(;:,i;.: f!l"-,ift.;''!et.torc"e",. ".i::i!},::;":"1:;iii,f;:il hcrd e'r'1'chlct$esa

4. Iolit crrrl.d by lotzle tr1l 'lu' to P!t'6ur€ 1n not'le(525) (4.50) (b)

5. 6t!en8th of nozlle erU outBlde of h'rd thlcv'lle63(.2?4) (h) (2) (r5,Ooo)

6. 6tt.Ee!h of Dozzl. r.11 rvrtl'bl' fo! r'1Efolc'Deal"' .'i,iii"iielito-- z,rso)c') ('3!' h'1)

&,

5,140 + 4,020

load to b. crrrl.d bt tildcd rebfotc'ocnt

33:333 : 8i:i331*;13!'- 5E,600 - {4,740

rr.! t!qu1r.d of tildcil tclafolc" !!10,400/15,000

Fc! of rclDfolc.lcnt u!.d: ts 5/8 tnch f1l1'! a'eldt

iiJa.'.iii'i-rr"" cxtcnsto! on Eo22]' Inlld€ of h'rdldcldEr (.525) (

' 625) (' 5) (4)aor21.: (.625) ('274) (2)

"ii98il tii,iSS'i'iS?i,iili3',vtil!.h of r!.. o! t.bfotc'o'!t' i

<2.5) (274) sr@s!,

loril crlcul.t.d to h|vc 'ttl!!'d 1r !b' E !!I t'Dov€il

G2s\ /.rl2' (27 + 1.25)(4.50).r?.nrrh of Dc!41 h herd rve1llble to! lelnfolc'ocnt- -i,z-igl

<t. poz - t'50)(17t5oo)

.!rc!8th of Dozzlc aall tv'tlablc to! t"nfo!"o'Dt

strcaEth of !.ld.il r.l.folcr[clt !ct.1 itlcntth

- 56,600 Ib.

. 3t,200 tb.

- 5,110 Lb.

- 2,350h Ib.

- 8'220b Lb.

- 11,000 ]b. .3t.- 9,160 lb. .o!r.

- 10,400 Ib. crt.- 13,850 lb, corr.

- 0.694 6q. b. Itt

- .781 tq. b.- .342 sq. b.

- 18,810 lb'

h . 0.565 14.

cxce88 thlckle6.2. Nozzl€ """"1"" t-t!

eat.riat used: s€apl€ss ,tett ptpe. S4_106, clade B, schedule 80Da:(letrD aUoralte st!!3s .. ,...,..lns1i'e i,rsDete! of frEtsh€i, .".,,;;.;;.;;;;.; ;;;;;;;;.....:..:

s 15.000 p.r

DcelDar. thrck..s. e*.lusive or ..r;""r"" "rr*"--^:-- d 3.9s1 1p.

,hlcknes. r€qu1led ., o*" **,"'iiXl,i']lllll......:. :.. :.. .L *#. '- - GE{"',u -.##Ifi.rrtft%, '' "sric--s'l'

,.

. ^to

14.

33,400 Ib.

13,050 1b.

9,150 1b.

18.810 lb.41,020 10.

b.ciuse th. tot.l strGrtth of 411020 lb' Gxc'ed6 th€ lold of 33'400 tb'

thc dlsis! ls .!!l3f'ctorY

Page 345: Process Equipment

APPENDX E

SAMPLE OF VARIOUSMATERIALS FOR PROCESS

EQUIPMENT

APPENDIX

,

MATERIAL SPECITICATIONS

Tubes

Seamless

CARBoN STEEL ASMB SA-179 cold drawn'

ASME SA-210' sPecifY grade'

r,ow ALLoY T** i:MB it-?33; ,o** o"u".

llrcs AIIoY STEEL ASME SA-213' specify grade'

ASME 5A-268' sPecifY grade'

NICKEL AND NICKEL A[oY ASME 5B-163' specify alloy and temper'

ALUI,flNUM AND ALLl4I\ruM ALI'oY ASME SB-234' specify alloy and

temPer'

coppER AND coppER ALLoy iiil| |i.lll, |fl-1,il llli ill lilill.

Welded

CARBoN STEEL ASME SA-214' electric resistance welded'

HIGII Au-oY STBEL ASME SA-249' specify grade'

ShelIs,Chonne|s,Covers,F|ootingHeods,TubesheEts,ondF|onges

PtPe

CARBoN STEEL ASME 5A-106 seamless' G^rade B or Grade A'

ASME SA-53 Grade B or Grade A'

I-ow AILoY STEEL ASME SA-335' specify grade'

IIIGH A[oY STEEL ASME 54.-376' specify grade'

ASME SA-312' sPecifY grade'

ALUMnfl,\4 AND ALUMINT'M A[oY' ASME SB-241' specify alloy and

temPer.

Coppen AND coPPER ALLoY' ASME SB-42'

. ASME SB-43, sPecifY temPer'668

Page 346: Process Equipment

ato

Plat

CARBoN STEEL. ASME SA_2g5 Grade C for plates up to 2_in. rhick.ASME SA-S15, specify grade.ASME 5,{_516, specify grade.

Low Au.oy STEEL. ASME SA-204 fuebox quality, speciry grade.ASME SA_203 Grade B firebox quality ior plates

to 6 ft thick.ASME SA_387, specifi grade.ASME SA.357

IIrcH Au.,oy STEEL. ASIVIE SA_240, specify type.

NTCKEL AND Nrcrcr Ar,roy. ASME 58_162, specify ternper.ASME SB-127, specifu temper.ASME 58-168, specig temper.

Al-ulvrtrutvr AND AruMtrnM Aury. ASME SB_209, specify alloy andEmper.

CoppER AND CoppER Arioy. ASME SB_ll, specify type.ASME 58_96, specify alloy.ASME 5B-169, speci$ alloy and temper.ASME SB_171, specig altoy.ASME 58402, specify alloy.

Castings

CARBoN STEEL. ASIVIE 5A_216, specify grade.ASME SA-352.

l,ow Alroy STEEL. ASME SA-217, specig grade.ASME SA_352, sperify grade.

IIrcH ALLoy STEEL. ASME SA_351, specify grade.

CoppER ALLoy. ASME 58_61 valve bronze.ASME 58-62 cast brass.

GRAY IRoN. ASME SA_278 Class 30.

ALUTTNUM AND ALUMTNUTVi ALLoy. ASME 58_26.

APPENDIX 671

Foryings

CARBoN STEEL. ASME SA-105 Grade I or II'ASME SA-181 Grade I or tr'ASME 5A-266 Class I or 2'

L,ow AND IIIGH Au-oY SrBEL' ASME SA-182' specify gpde'

ASME 5A-336, sPecifY class'

' NICKBL AND NICKEL AIr-oY ASME 58-160' specify temper'

ASME 58-164, specify temper and class'

ASME 58-166, sp€cify temper'

ALUI"ff.IUM AND ALUMINUM ALLoY' ASME SB-247' specify alloy and

temper.

Bolting

Stu/s artd Stttd Bolts

Au,oY STEEL. ASME SA-193, specify grade'

NICKEL AND NICKBL ALt oY ASME 58-160' specify temper'

ASME 58-164, specify temper and class'

ASME 58-166, sPecifY temPer.

ALu\,m{uM AND ALUMINUM ATLoY ASME SB-2 I 1 ' specify ailoy and

temDer.

Nurs

CARBoN STEEL. ASME SA-194 Grade 2H' minimum requirement'

AIIoY STEEL. ASME SA-194, specify grade'

NICKEL AND NICKEL ALLOY. ASME 58-160,' ASME SB.IS'

ASME 58.166,

ALUm{uM AND ALUMn'rL'4 ALLoY' ASMErcmper.

specify temPer.

specify temPer and class.

specify temPer.

SB-211, specifY alloY and

Page 347: Process Equipment

APPENDX F

REQUIRED DATA FORMATERIAL APPROVAL IN THE

ASME SECTION VIII CODE

APPENDIX

APPROVAT OF NEW MATERIATS UNDER THE ASME BOITER AND

PRESSURE VESSEL CODE

A. Code PolicY

1. It is ttle policy of the ASME Boiler and Pressure Vessel.Commiftee to

'' ;d.il;.'i;;il.ion in s""ti* n onlv such Specifications that have been

adopted by the Amencan Society for Testing and Materials

2. lt is expected that requests foi Coat approval will normally be for

materials for which tn.r. ,.'t'nSiV Sp#fication. For other materials'

request should be rnuO" to 'CiTN{ to develop a Specification which can

Le^oresented to the Code Codmittee'

B. MechonicolProPerlies

l. Together with the Specification for the material'-the inquirer shall fumish

the Committee with uO"qout" ouil-on-*ttl"h to but" ailoyalte sfess values for

inclusion in the applicable stress ible' The data shall include values of ultimate

il;;;;dd."l.futh, reductio;i;a' elongation' creep strength' and stress-

rupture strength of base metar and welded joints over the.lang:-1f-.temperatures

at which the materiut i, to u" ot"O' etty healt treatment that is required to produce

the tensile properties strouto ue'fuiii Ott"tiu"o' Adequate data,on the notch

toushness in the proposed 'ung"

ii"titt temperatures must he furnished'

Seriice experience in the temp;;a;iunge contimpluted witl be usetul to the

Committee.2'Ifthematerialistobeusedinvesselstooperate.underextemalpressure,

sfess-strain curves (tension "t

titp*1ti*l shall be fumished for a range of

design temPerature desired'

C. WeldobilitY

The inquirer shall furnish complete data on the weldability^of material intended

for welding including <lata on piocedure and performance 'qlalification

tests

made in accordanc" *itr' t'" "qliitt"nis or secton x w-etaing tests shall be

made over the full range tr friJt""tt i" which the material is to be used'

Pertinent information, such ul t'"ut tt"ut-"nr.Jequ]red: -suj::etibility to ar

ffi;;;; il;ount or "*p"ti"nt"

in *elding the material shall be given'

D. PhYsicol Chonges

It is important to know the structural stability characteristics and the degree of

retention of properties *itft "-pJt*t

-^i i"tpttutut". of new materials' The

influence of fabricution p'""ui"i totft as forming' welding' and thermal treat-

ments of the mech*i""f p"p"tt[t ' Jo"iiltty' .-d ti'tt":At:: of the material

;fi.i,ilil;il"'i"irv i"r'"i" a degraclarion in eroe-el::.Tav be encoun-

tered. Where particot' t"tp"'ut*" *n'ges of exposure or heat Eeatment' cool-672

Page 348: Process Equipment

6f4

ing r0tcs, combinetions of mechanical working and thermal treatmenh,cotion practices, and so on, cause significant changes in theproperties, microstructure, resistance to brittle fracture, and so on, it is of primaimportance to call attention to those conditions which should be avoidedseryice or in the manufacture and fabrication of parts or vessels frommaterial.

E. Potenls

The inquirer shall state whether or not the material is covered by patents andwhether or not it is licensed and if licensed the limitations on its manufacturt.

F. Code Cose

In exceptional circumstances, the Code Committee will consider the issuance ofa Code Case effective for a period of three years permitting the use of a materialprovided that the following conditions are mec

l. The inquirer provides evidence that a specification for the material icbefore ASTM.

APPENDIX G

P NOC-T O U NE F O R P ROV I D I N G. ..-DATA

FOR CODE CHARTS-FOR

EXTERNAL PRESSUREDESIGN

5.

The material is commercially available and can be purchased within thospecified range of chemical and tensile requiements and other require-ments described in B.The inquirer shows that there will be a reasonable demand for the mate-rif by industry and that there exists an urgency for approval by meangof a Code Case.

The request for approval of the rnaterial shall clearly describe it in ASTMSpelincatiol foll, including such items as scope, process, manufacturc,conditions for delivery, heat teatment, chemical and tensile requ E-ments, bending properties, testing specifications and requirements,workmanship, finish, marking, inspection and rejection.The inquirer shall furnish the Code Committee with all the data specifiedinB0oE.

675

Page 349: Process Equipment

676 APPENDI q aPPENDIX

5.

677

On occasion the ASME Boiler and pressure Vessel Committee is rcqucsrctr ((rprovide for a new material chan for external pressure design such ai thosc irrAppendix V of Section VIII, Division l. The SGDE/SCD requires reliable rlttuupon which to base the construction of charts. The SG is not in a position todevelop or evaluate the required data. Consequently, the SGDE recommends thcfollowing procedures to be followed in providing the SG with adequate andreliable data.

1, The compiling and evaluation of material data are rightfully the re-sponsibility of the Subcommittee on hoperties of Me1ds. The threcsubgroups involved would be the SG on euenched and Tempered Steel,the SG Strength-Steel and High Temperature Alloys, and the SCStrength-Nonferrous Alloys.

2. Upon receipt of an inquiry for a new chart, the secretary should refer theinquiry ro the appropriate SG of SCp. The SG shall ditermine whetheror not adequate data are available or whether the inquirer shall be re-quested to supply the required data. The SG should screen and evaluatethe data and forward them to the SGDE with their commenrs or recom_mendations. The Materials SG should clearly identify the material anddefine its use as to product form and, where applicabie, any restrictionson the method of fabrication of the completed pressure vesiel (i.e., heatheatment or welding limitations).

3. It is su€gested that, to expedite processing of inquiries, a specific individ_ual might in some cases be designated as the member iesponsible forliaison with SGDE. This member would be responsible for the trans-mission of approved data to SGDE.

_ _A description of the data required for proper preparation of the design charts

follows. It is felt that these are minimum requirements for the preparation ofreliable charts. The use of so-called typical stress-strain curves based on astatistically significant volume of data may be satisfactory if the region betweenthe proportional limit and the yield shength is accurately reprisented. Thedeveloprnent of the tangent modulus in this region is a critical step. It is sug-gested that this description be prepared in a form suitable for attachment to anyrequests for material data from an inquirer.

A copy follows of a description of the method used to derive the materialcurves on the charts directly from the laboratory stress-strain curves. It was feltthat this procedure might enable the Materials Subgroups to better evaluate ourdata requirements. The balance of the lines on the chart are functions of thegeometry of the vessel, and so do not change with material of construction.

DATA NEEDED BY THE SG EXTERNAL PRESSURE FOR THEPREPAMTION OF CODE CHARTS FOR EXTERNAL PRESSURE DESIGN

For the use of the SG on Strength Properties and the SG on Nonferrous Mate_nals.

l.

2.

The nrinirnurn specilied yield strength or yield point (statc which) as

given in the specifications for the material.

Stress-strain curves representative of the material at the following tem-

perarures:

(a) Ambient (room) temperature.

(b) The highest temperature for which coverage is desired'

(c) One or more intermediate temperatures as may be desirable to

facilitate interpolation on the chart.

Temperatures at some multiple of 100'F are preferred'

The shess-strain curves should extend to at least the 0'37o offset point

(to ensure being able to obtain reliable values of the tangent modulus to

O.2Vo offset). Consideration should be given to extending tests to higher

values of strain for possible future use with stress intensity values in the

elasto-plastic range. (This is much less expensive than to run additional

tests at a later date.)

Stress-strain curves in compression are preferred. It is recomrnended

that compression tests be made in accordance with ASTM Specification

E-9, Standard Methods of Compression Testing of Metallic Materials'

Stress-strain curves from tension tests will be acceptable if there is

sufficient background of information to show that there is no substantial

difference between the stress-strain characteristics of the material in

tension and compression. Data should indicate whether tension or com-

pression tests were made.

The expected properties of the material at the temperatures described

above, for material having the minimum specified properties, are as

follows:(a) Yield strength or yield point (state which).

(b) Proportional limit.(c) Elastic modulus (state whether by the dynamic method or from

stress-strain curves).

The condition of the material as stated in the specifications, for example,

annealed, hot finished. cold drawn. temper. and so on'

Stated whether intended for welded construction. The above data should

properly include the effect of the heat of welding on the properties of the

rnut".iut. It it acceptable in such cases to use data for the material in the

annealed condition .

The inquirer should supply data from at least three specimens at each

temperature and that these specimens should preferably be taken from

more than one "production lot" or "heat."

3.

4.

6.

Page 350: Process Equipment

,.Q

APPENDX H

CORROSION CHARTS

.-".;*, '"

,,",^, ., " ' ".. 1 :Y:l;:li":i "'"" """"^'".'"''"'" ""

Corro3ion chorls courtesv o( t}E Nooter CorPototio'' St l-oois' Mo'

679678

i

^iiiri.t:ir

"i?

Ii:ti:t

trl

t"tI rl1"tt"lI 8l| 31

l;tl3ltl

t^trl 3l

!l il't"ltI,t .:t

't"l

Page 351: Process Equipment

I

ti

E

;

ilIi

iItt':

6l

;tl

ri

I;

!

litlti

,,i..'-:''l'::X:l'..i::

rlll r ll'i il i '1.'ll

aa':l.

ill:il:lilt

lii.i

i

t::t^""

lrlitI

Ti

^",1

"liiltl

;r*-l%

IT

t:

.:- l-l

t;

,G

*l:lrii

Ti.!lit

ti

tii

i

ii

il

tw

680 68r

Page 352: Process Equipment

;{

T

APPENDIX

VARIOUS ASME DESIGNEQUATIONS

683642

l

lI

l

l

I

i..

:l!:9,l

lrll

I

lll

l

Page 353: Process Equipment

^l

RI

.. oqlg* o16lle.l

I

oll

?lxl

TlEI{il

t-. Inl

ilr-lc-lel

@l

cr/rl

r* ls "l;l- ll @lo

n[ nle ;l:l\ lr Kltrr lE ro

lr-

El* >Fl+ !1.it., \tcalc.l

rq l* ltla ld ^l-El; El* dlLlu lR lR

:lE E --^S*E E $ *EEl" H* e

Bg $e :t $Eg 'l tE .i

qt alol ol*

JI- U^[.l \l

sl+ nl? Hl;lo< la< lo

lc^l

t?t>ldl+ltrll?rlc.l

I

q)

afu

fr.

6856U

8C]

Ic.l

I:lAI

ol ql+l olr..t | * +l&6dt

=l€l ill-:t vlwl q,l

El sl+l* +l&qt &la.t {l

lo 11-lg ul*

l.E le l&

sl? *F $l?ta( IE la

ri)3

cil

sl* lft

gII FII R

re lt lftrl? rl? Rl?lu lH lH

g, F* F, gest

$e $

u'^EEaa v)

9^='dfteFd

li

(l)^!.=(ir v

A

Page 354: Process Equipment

APPENDIX

JOINT EFFICIENCY FACTORS

Toble J.l Roundobouf lt Full X-Royed

F

FULLX-RAY

S POT

X RAYSEAMLESS SEAMLESS

LL

SEAMLESS SEAMLESSFULL

X-RAY

SPOT

X_RAY

HEADJ, E. t.o .85 t.o t.os,.R

too% loo% looo/oOt

too,/o

SHELL

,=qQ

J.E t.o I.O l.o .855r

too% too% rco% looY.

2!)2 Y,',

z9

J.E t.o t.o t.o .85

too%o/

IOO/o too% too%

Toble J.2 Roundqbout ls Portiol X-Royed

nSEAMLESS

FULLX'RAY

SPOTX.RAY SEAMLESS SEAMLESS

LL

SEAMLESS sEAMLESS SEAMLESSFULL

X-RAY

S POT

X. RAY

LJtrANJ. E. t.o t.o .85 I,O I,O

too% too% too%' rco% too%

SHELL

ia,=6

J.E t.o t.o l.o LO .85s,

''E- rco% too% too% too% na%

29=ii==zo

J. E, .85 .85 .85 .85 Q5

t-no% too% too% rco% too%

697

Page 355: Process Equipment

Tobb J.3 Roundqbout lr Spor X-Royed

l-l- NOX-RAY

5EAIVLEsS SEAMLESS

LSEAMLESS

FULLX-RAY

SPOTX-RAY

HEADJ, E. .85 LO t.osf.R

too% 63 lo 6)./o

SHFI I

>=q u-,

J.E LO .85 R5

^t^t ^-O/6) /o too% roo%

zi"

56

J.E .85 .85 .85

too% too% too%

Toble J.4 Roundobout ls Not X-Royed

tAD

SEAMLESSSPOT

X- RAY SEAMLESS sEAMLESS

tL SEAMLESS SEAMLESSFU LL

X- RAY

SPOT

X-RAY

TI-EADJ. E. t.o .85 t.o t.o

q 6U /o too% ^-o/6) /o ^- o/6a /o

qHFI I

cio

==g<D

J.E t.o t.o 85 .85

80% ^-o/63 /a too% taao./tww /o

2 i,"

fiG621

J.E .70 .85 .85 R5

too% too% too% lOOo/o

688689

APPENDX K

SIMPLIFIED CURVES FOR

EXTERNAL LOADING ONCYLINDRICAL SHELLS

Page 356: Process Equipment

| | | I tttl

M,

| | | ttl

Bending str$s = I(, [,|

:\:

tt".ottd"tMcD #,

\"3J

0.0010. t0 1.0

Figut K. I t'{o.crt tl6 a @"/ tn) duc to an ex".nol cir.",mfrronr'ror mon,.nr ,,L on o circuro. cyrnd"..

| 0.0

690 691

.,Vr|!-.'dp...

0.q)1 10.o0,r0

figurc K,2 , .mbrono forct N6,a (d"/'{i.) luc to on trLrnol mofieni i'lc on o cird,,lor qlind€r'

" f{tr

t.o ,,",,'_

Nr

,'^/\/No

Mambrane 3tres = K,lNv,i)ld"Tll'l"ll

= 7l--_//

/

L

Jz

'1.0

'' ,/D-r

Page 357: Process Equipment

\o

rrtttttl

t4s

Mo

\

'".,,**j"ilj;*N

Bendins strels = ff, t,nr', "

lr,rr.,, * \t

\T\\-

''1\

0.0010.10

r = --js-,E_rF'o'rrcK'3,{om*r,{k,(d./roducroon.xtlmor

ro.,girudinor mom.nr /lt on o cir.oror cy'indor.

692693

'.,Mm*--

0.001

. ., ?rL!!4. .rrlllltrtr

0.t 0

I | | lll llrr

Mombrane stress = *"t*,,,, to.rtr7lffi

E

cq

{

0.01

0.10 r 0.0

'/D.rFig!ru X.,t lrt mbrsn€ tor.e NF,a (d"t/r.) doe to on €xlrrnol nomcnl 14 on o circulor Eylindar.

1.0

Page 358: Process Equipment

\D!,lT

Eenditg rtre$ = tr, {it(, N,00f

T'-

I tl

."'!M'RF'*..-

0.10

t.o

-

I I | | | lll

=\

Bonding gtre$ = ,(, (ttt', d /;a\

2(x) V6m

I ttl

0.10

=

3

0.01

0.0010.r0

Fi$r. K.5 Lnding morn€nt t{(&A du. lo onlongihdinol arb, ,t{a/P on frunwrn <uit.

1.0 to.o- 'lo

,/DFod.rnof rodiol food P on o .ir.ulor qlindf'. tl/p on

1.0

a= 7"1./6)T

Figir. K.6 Bcnding mdnGnt ir(,,it.lu.lo on.xtornol rodiol lood on o cirorhr cylinder' 't'l'/Pon longi|vdlnol

oxi., l,|,/P on lrols€rt. qxb.

694 695

Page 359: Process Equipment

'!U;|F F*-- ., --, "a?.e!.r,ry@!

1.0 I tt tl tttl

\.",

lvlembrane 9tr6ss = I(, (Nt c.6flnft

:

t--eJ

E

ri{

0.00t

0.01

0.0011.0

,/aAFiguro K.7 rrtemhrone iorce r.,h,a t/p due io on .x|€rnsl rodiol lood p on a cirorlor cylind.r (rqnw.r.. orh). Figure K.8 ,rt mbrcnc lorc6 N(,rI/P due io on sxi.rnol rodiol lood P on o cirsrlor <ylinder (loqgiludiml

arir).

0.100.10 1.0

./87

696697

Page 360: Process Equipment

APPENDIX

CONVERSION TABL

-,wF6'-*-

Multiply English Units

.,.._.-*".- *rr'w'|Converrlon to SI Unltr

Bv Factor To Get SI Units

IlchU.S. gallon

FoofPound mass

Pound forcepsi pressure

Bar

BtuHorsepower (550 ftlb/s)Fracture toughness (ksi V-in)"F

0.0254 Met€r

0.003785 Metef0.02832 Metef0.4536 Kilograrn4.448 Newton6,894.8 Pascal

100,000 Pascal

1,055.056 Joule

745.7 Watt

1.1 x 106 Pa VmcF - 32)/1.8 'c

General Conversion Units

Multiply By Factor To get

Foot3

BarMile

7 .48

14.50

5280

U.S. gallonpsi

Foot

Multiply SI Units

Conversion to English Units

By Factor To Get Enelish Units

MeterMetefMetefKilogram mass

NewtonPascal

Pascal

Joule

WattFncture toughness Pa \6"c

39.370264.201

35.311

2.2050.2250.m01450.00001

0.0m94780.001341

0.9091 x 10-6

l.8c + 32

Inch

U.S. gallon

foodPound mass

Pound forcepsi pressure

Bar

BtuHorsepower (550 ft-lbh)ksi VinT'

699