DOCUMENT RELEASE AND CHANGE FORM - hanford.gov · Evaporator, in which the P-B-1 pump recirculates slurry within the evaporator recirculation waste loop. For this scope, work includes

1 SPF-001 (Rev.D1)

DOCUMENT RELEASE AND CHANGE FORMPrepared For the U.S. Department of Energy, Assistant Secretary for Environmental ManagementBy Washington River Protection Solutions, LLC., PO Box 850, Richland, WA 99352Contractor For U.S. Department of Energy, Office of River Protection, under Contract DE-AC27-08RV14800

TRADEMARK DISCLAIMER: Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States government or any agency thereof or its contractors or subcontractors. Printed in the United States of America.

Release Stamp

1. Doc No: RPP-SPEC-62735 Rev. 00

2. Title:Procurement Specification for 242-A Evaporator Recirculation Pump P-B-1

3. Project Number: ☒ N/A 4. Design Verification Required:

☐ Yes ☒ No

5. USQ Number: ☒ N/A

N/A-3

6. PrHA Number Rev. ☒ N/A

Clearance Review Restriction Type:public

7. Approvals

Title Name Signature Date

Clearance Review Aardal, Janis D Aardal, Janis D 11/07/2018

Design Authority Servin, Mario A Servin, Mario A 11/05/2018

Checker Bentley, Kenneth Bentley, Kenneth 11/01/2018

Document Control Approval Hood, Evan Hood, Evan 11/07/2018

Engineering Discipline Lead-Civil/Structural Scott, Mark A Scott, Mark A 11/01/2018

Engineering Discipline Lead-Electrical Rambo, Charles L Rambo, Charles L 10/16/2018

Engineering Discipline Lead-Mechanical Goessmann, Glen E Goessmann, Glen E 11/01/2018

Engineering Hoisting and Rigging SME Mackey, Tom Mackey, Tom 11/05/2018

Originator Servin, Mario A Servin, Mario A 11/04/2018

Other Approver Balint, Gregory G Balint, Gregory G 11/01/2018

Quality Assurance Thompson, Tyler J Thompson, Tyler J 10/30/2018

Responsible Engineering Manager Houghton, David J Houghton, David J 11/06/2018

USQ Evaluator Dosramos, Eduardo Dosramos, Eduardo 11/06/2018

Welding Engineer Berkey, James Berkey, James 10/16/2018

8. Description of Change and Justification

Initial release.

9. TBDs or Holds ☒ N/A

10. Related Structures, Systems, and Components

a. Related Building/Facilities ☐ N/A b. Related Systems ☐ N/A c. Related Equipment ID Nos. (EIN) ☐ N/A

242-A 242A 242A-HR-CRN-005242A-HR-CRN-006P-B-1P-B-1-M

11. Impacted Documents – Engineering ☒ N/A

Document Number Rev. Title

12. Impacted Documents (Outside SPF):

N/A

13. Related Documents ☐ N/A

Document Number Rev. Title

RPP-SPEC-41919 01 SPECIFICATION FOR RECIRCULATION PUMP P-B-1

14. Distribution

Name Organization

Balint, Gregory G COGNIZANT SYSTEM ENGINEERING

Bentley, Kenneth 242-A EVAPORATOR ENGINEERING

Castleberry, Jim L TFP PROJECT MANAGEMENT

Houghton, David J TF PROJECTS & INTEGRITY ENGRNG

Smith, Gregory E TANK FARM PROJECTS ENGINEERING

Trevino, Johnny M 242-A EVAPORATOR ENGINEERING

� � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � �Nov 07, 2018

DATE:

A-6002-767 (REV 3)

RPP-SPEC-62735, Rev. 0

Procurement Specification for 242-A Evaporator Recirculation Pump P-B-1

Author Name:

M.A. Servin

Tank Farm Projects Engineering

Washington River Protection Solutions, LLC

Richland, WA 99352U.S. Department of Energy Contract DE-AC27-08RV14800

EDT/ECN: UC:

Cost Center: Charge Code:

B&R Code: Total Pages:

Key Words: P-B-1 Pump, Recirculation Pump, Procurement Specification, 242-A Evaporator

Abstract: This Specification provides the minimum requirements for the design and fabrication of the

P-B-1 Pump for use at the 242-A Evaporator, which is located in the 200 East Area of the U.S.

Department of Energy’s Hanford Nuclear Waste Site. Construction of the 242-A Evaporator started in

1974 and operation began in 1977. The mission of the 242-A Evaporator is to support environmental

restoration and remediation of the Hanford Site by optimizing the 200 Area double-shell tank waste

volumes through radioactive liquid waste volume reduction. Volume reduction is accomplished through

an evaporation process that uses a conventional forced-circulation, vacuum evaporation system operating

at low pressure to concentrate radioactive waste solutions. The P-B-1 pump function is to recirculate

withn the evaporator recirculation waste loop.

TRADEMARK DISCLAIMER. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof or its contractors or subcontractors.

Release Approval Date Release Stamp

Approved For Public Release

� � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � � �

� � � � � � � � ! � " # � $ � % & ' ( ) � * + , - . / & + 0 / ) 1 Nov 07, 2018

DATE:


Procurement Specification for 242-A

Evaporator Recirculation Pump P-B-1

M.A. Servin

Tank Farm Projects Engineering

Washington River Protection Solutions LLC

Date Published

November 2018

Prepared for the U.S. Department of Energy

Office of River Protection

P.O. Box 850

Richland, Washington

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i

TABLE OF CONTENTS

1.0 SCOPE ............................................................................................................................ 1-1

2.0 APPLICABLE DOCUMENTS..................................................................................... 2-1

2.1 NON-GOVERNMENT DOCUMENTS.............................................................. 2-1

2.2 NON-CODE OF RECORD DOCUMENTS ....................................................... 2-3

2.3 GOVERNMENT DOCUMENTS........................................................................ 2-3

3.0 TECHNICAL REQUIREMENTS ............................................................................... 3-1

3.1 ITEM DEFINITION ............................................................................................ 3-1

3.2 INTERFACE DEFINITION................................................................................ 3-1

3.2.1 Pump Assembly Interface with 242-A Evaporator .................................. 3-1

3.2.2 Pump Assembly Interface with Pump Casing ......................................... 3-2

3.2.3 Electrical Service Interface ...................................................................... 3-2

3.2.4 Shaft Seal – Barrier Fluid Interface ......................................................... 3-2

3.2.5 Vibration Monitoring System Interface ................................................... 3-3

3.2.6 Motor Bearing Grease Lines Interface (Not Available) .......................... 3-3

3.2.7 Lifting Yoke Interface.............................................................................. 3-3

3.2.8 Impact Wrench Interface.......................................................................... 3-3

3.2.9 Interface Critical Dimensions .................................................................. 3-3

3.3 CHARACTERISTICS ......................................................................................... 3-5

3.3.1 General Requirements.............................................................................. 3-5

3.3.2 Fluid Characteristics ................................................................................ 3-5

3.3.3 Pump Functional Characteristics ............................................................. 3-6

3.3.4 Pump Physical Characteristics................................................................. 3-6

3.3.5 Reliability................................................................................................. 3-8

3.3.6 Maintainability......................................................................................... 3-8

3.3.7 Environment............................................................................................. 3-9

3.4 DESIGN AND CONSTRUCTION ..................................................................... 3-9

3.4.1 Seismic Design/Analysis ......................................................................... 3-9

3.4.2 Rotor Dynamic Analysis........................................................................ 3-10

3.4.3 Critical Speed Analysis.......................................................................... 3-10

3.4.4 Pump Assembly Installation and Lifting & Handling Design/Analysis 3-10

3.4.5 Materials ................................................................................................ 3-12

3.5 DRAWINGS AND MANUALS........................................................................ 3-13

3.6 FABRICATION/ASSEMBLY PROCESSES ................................................... 3-13

3.6.1 Cleaning and Painting ............................................................................ 3-14

3.6.2 Special Tools.......................................................................................... 3-15

3.6.3 Marking.................................................................................................. 3-15

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ii

4.0 QUALITY ASSURANCE REQUIREMENTS............................................................ 4-1

4.1 QUALITY ASSURANCE PROGRAM .............................................................. 4-1

4.2 QUALIFICATIONS ............................................................................................ 4-1

4.2.1 Welding Personnel and Procedures ......................................................... 4-1

4.2.2 Welding Inspectors and Procedures......................................................... 4-2

4.3 INSPECTIONS AND TESTING......................................................................... 4-2

4.3.1 Weld Inspection and Examination ........................................................... 4-4

4.3.2 Radiographic Examination of Impeller.................................................... 4-4

4.3.3 Megger Test ............................................................................................. 4-5

4.3.4 Pump Motor Driver Testing..................................................................... 4-5

4.3.5 Hydrostatic Test ....................................................................................... 4-5

4.3.6 Pre-Pump Run-In Performance Test ........................................................ 4-5

4.3.7 Pump Run-in Test .................................................................................... 4-6

4.3.8 Pump Sealing System Leak Inspection.................................................... 4-6

4.3.9 Post-Pump Run-In Performance Test ...................................................... 4-6

4.3.10 Load Test ................................................................................................. 4-7

5.0 DOCUMENT SUBMITTAL......................................................................................... 5-1

5.1 APPROVAL OF SUBMITTALS ........................................................................ 5-3

5.2 LIST OF SUBMITTALS..................................................................................... 5-3

6.0 PREPARATION FOR DELIVERY............................................................................. 6-1

6.1 PRESERVATION AND PACKAGING ............................................................. 6-1

6.2 MARKING .......................................................................................................... 6-1

6.3 SHIPPING AND HANDLING............................................................................ 6-1

6.4 TRANSPORTATION.......................................................................................... 6-2

7.0 NOTES............................................................................................................................ 7-1

7.1 LIST OF ACRONYMS ....................................................................................... 7-1

7.2 UNITS.................................................................................................................. 7-2

8.0 APPENDICES................................................................................................................ 8-1

8.1 APPENDIX A – PUMP CURVE FOR FACILITY PUMP ................................ 8-1

8.2 APPENDIX B – MOTOR DATA SHEET .......................................................... 8-3

LIST OF FIGURES

Figure 8-1 PUMP CURVE FOR P-B-1 PUMP ........................................................................... 8-2

Figure 8-2. Motor Data Sheet ...................................................................................................... 8-4

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iii

LIST OF TABLES

Table 2-1. Non-Government Code of Record Documents .......................................................... 2-1

Table 2-2. Non-Government Non-Code of Record Documents ................................................. 2-3

Table 2-3. Government Documents............................................................................................. 2-3

Table 3-1. Fluid Properties (Slurry)............................................................................................. 3-5

Table 3-2. Pump Performance Characteristics............................................................................. 3-6

Table 5-1. Summary of Submittals .............................................................................................. 5-2

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1-1

1.0 SCOPE

This Specification provides the minimum requirements for the design and fabrication of the

vertical, axial flow pump (referred to as the P-B-1 pump) for use at the 242-A Evaporator, which

is located in the 200 East Area of the U.S. Department of Energy’s Hanford Nuclear Waste Site.

Construction of the 242-A Evaporator started in 1974 and operation began in 1977. The mission

of the 242-A Evaporator is to support environmental restoration and remediation of the Hanford

Site by optimizing the 200 Area double-shell tank waste volumes through radioactive liquid

waste volume reduction. Volume reduction is accomplished through an evaporation process that

uses a conventional forced-circulation, vacuum evaporation system operating at low pressure to

concentrate radioactive waste solutions.

The 242-A Evaporator has been identified as a critical facility for continued and future Hanford

operations. The vertical, axial impeller type pump is an integral component of the 242-A

Evaporator, in which the P-B-1 pump recirculates slurry within the evaporator recirculation

waste loop.

For this scope, work includes design, fabrication, assembly, inspection, testing, documentation,

packaging, and shipping of a vertical axial impeller type pump designed to interface with the

existing 242-A Evaporator. This scope includes the Pump Assembly (motor-shaft-impeller

assembly), remotable gasket, stand, and any custom handling equipment required to maneuver

(e.g., transport/install) the pump assembly. The intent is to procure a replacement pump

assembly that uses the existing pump casing, interface with the existing facility utilities and meet

performance requirements. The Buyer will install the Pump Assembly into an existing pump

casing currently installed at the facility.

All requirements in this Specification are applicable to a single pump assembly.

Work does not include site services, installation, or operation of site equipment. Additionally,

work does not include fabrication of the items provided by Buyer (e.g., interfacing connectors) to

be installed on the Pump Assembly. Government furnished equipment (GFE) include the

following items to support construction and testing:

! Pump Casing (Lawrence Pump Inc. Drawing E25252),

! Long & Short Alignment Dowel (H-2-57331, “Mechanical Equipment Details Short & Long

Dowels”),

! Stud & Locking Pin (H-2-57332, “Mechanical EQPT Detail-Stud”),

! 2”, 3-Way Connector Nozzles (H-2-32447, “Details & Assy. Stainless Steel 2”-3” Way

Conn. Nozzle”),

! 2”, 3-Way Vertical Connector Nozzle (H-2-32427, “Horizontal and Vertical 3 Way Type 2”

Connector”),

! Free Nuts, 1-1/4 inch (H-2-52963, “Mechanical Equipment Details – Free Nut”), and

! Lower Electrical Connector (H-2-32401, “Assembly Lower Electrical Equip. Connector”)

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2-1

2.0 APPLICABLE DOCUMENTS

2.1 NON-GOVERNMENT DOCUMENTS

The following documents of the exact issue shown in Table 2-1 form a part of this Specification

to the extent specified herein and establish the Code of Record (COR). In the event of a conflict

between documents referenced herein and the requirements of this Specification, the Buyer shall

be notified to obtain interpretation and clarification.

Table 2-1. Non-Government Code of Record Documents

Industry Consensus Codes And Standards

Document Number Title

AISC 15th Ed., 2017 Steel Construction Manual, American Institute of Steel Construction (AISC),

Chicago, Illinois.

ANSI/HI 14.6, 2011 Rotodynamic Pumps for Hydraulic Performance Acceptance Tests, ANSI/Hydraulic

Institute (HI), New York, New York.

API 541, 2014 Form-wound Squirrel Cage Induction Motors—375 kW (500 Horsepower) and Larger,

American Petroleum Institute (API), NW, Washington, DC.

ASCE 07, 2015 Minimum Design Loads for Buildings and Other Structures, American Society of

Civil Society, Reston, Virginia.

ASME B&PVC,

Section IX, 2017

Boiler and Pressure Vessel Code (B&PVC) – Welding and Brazing Qualifications,

American Society of Mechanical Engineers (ASME), New York, New York.

ASME B31.1, 2016 Power Piping, American Society of Mechanical Engineers, New York, New York.

ASME BTH-1, 2014 Design of Below-the-Hook Lifting Devices, ASME, New York, New York.

ASME B30.20, 2013 Below-the-Hook Lifting Devices, ASME, New York, New York.

ASME Y14.1, 2012 Decimal Inch Drawing Sheet Size and Format, American Society of Mechanical

Engineers, New York, New York.

ASME Y14.2M, 2008 Line Conventions and Lettering, American Society of Mechanical Engineers,

New York, New York.

ASME Y14.3, 2012 Orthographic and Pictorial Views, American Society of Mechanical Engineers, New

York, New York.

ASME Y14.5, 2009 Dimensioning and Tolerancing, American Society of Mechanical Engineers, New York,

New York.

ASME Y14.38, 2007 Abbreviations and Acronyms, American Society of Mechanical Engineers, New York,

New York.

ASNT SNT-TC-1A,

2016

Recommended Practice, American Society for Nondestructive Testing (ASNT),

Columbus, Ohio.

ASTM A 744/744M Standard Specification for Castings, Iron-Chromium-Nickel, Corrosion

Resistant, for Severe Service, American Society for Testing and Materials

(ASTM International), West Conshohocken, PA.

ASTM A890 Standard Specification for Castings, Iron-Chromium-Nickel-Molybdenum

Corrosion-Resistant, Duplex (Austenitic/Ferritic) for General Application,

American Society for Testing and Materials (ASTM International), West

Conshohocken, PA.

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2-2

ASTM E 186 Standard Reference Radiographs for Heavy Walled (2 to 4 1/2 in. Steel

Castings) American Society for Testing and Materials (ASTM International),

West Conshohocken, Pennsylvania.

ASTM E 446 Standard Reference Radiographs for Steel Castings up to 2-in, in Thickness

American Society for Testing and Materials (ASTM International), West

Conshohocken, Pennsylvania..

AWS D1.1, 2016 Structural Welding Code - Steel, American Welding Society (AWS), Miami, Florida.

AWS D1.6, 2017 Structural Welding Code – Stainless Steel, American Welding Society, Miami, Florida.

AWS QC1, 2007 Specifications for AWS Certification of Welding Inspectors, 6th Edition, American

Welding Society, Miami, Florida.

IEC 60034-14, 2007 Rotating electrical machines – Part 14: Mechanical vibration of certain machines with

shaft heights 56 mm and higher – Measurement, evaluation and limits of vibration

severity, International Electrotechnical Commission, Geneva, Switzerland.

IEEE 112, 2017 IEEE Standard Test Procedure for Polyphase Induction Motors and Generators, Institute

of Electrical and Electronics Engineers, New York, New York.

ISO 1940-1, 2003 Mechanical Vibration Balance Requirements for Rotors in a Rigid State. International

Organization for Standardization, Geneva, Switzerland.

Hydraulic Institute Hydraulic Institute Standards, ANSI/Hydraulic Institute (HI), New York, New York.

NEMA Standard

MG-1, 2016

Motors and Generators, National Electrical Manufacturers Association (NEMA),

Arlington, Virginia.

NIST Handbook 143,

5th Edition, 2007

State Weights and Measures Laboratories Program Handbook, National Institute of

Standards and Technology (NIST), Harris, G.L., Gaithersburg, Maryland.

RPP-8360, Rev. 6 Lifting Attachment and Lifted Item Evaluation

TFC-ENG-STD-06 Design Loads for Tank Farm Facilities

TFC-ENG-STD-34 Standard for the Selection of Non-Metallic Materials in Contact with Tank Waste

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2-3

2.2 NON-CODE OF RECORD DOCUMENTS

The following documents of the exact issue shown in Table 2-2 are utilized in, or referenced by

this document, form a part of this Specification to the extent specified herein but are not

considered to be COR documents.

Table 2-2. Non-Government Non-Code of Record Documents


1402-WRP-041B 242-A Impact Wrench

A 44106 Detail of Propeller Part No.81

H-2-32427, Sheet 1-2 Horizontal and Vertical 3 Way Type 2” Connector

H-2-99028, Sheet 1-4 Pump Assembly P-B-1

H- 2-52963 Mechanical Equipment Details – Free Nut

H-2-31103, Sheet 1-4 Canyon Impact Wrench PUREX Type

H-2-7249 Socket – Canyon Impact Wrench

H-2-32447 Details & Assy. Stainless Steel 2”-3 Way Conn. Nozzle

H-2-32401, Sheet 1-2 Assembly Lower Electrical Equip. Connector

H-2-57331 Mechanical Equipment Details Short & Long Dowels

H-2-57332 Mechanical EQPT Detail-Stud

H-2-99046 Lifting Yoke P-B-1 Pump

E-25252 Detail of Casing for 28-in. Vertical impeller pump

TFC-BSM-IRM_DC-C-07 Vendor Processes

2.3 GOVERNMENT DOCUMENTS

Documents listed in Table 2-3 constitute a part of this Specification to the extent specified

herein. The most current version of the documents shall be used unless otherwise specified. In

the event of conflict between the documents referenced herein and the contents of this

Specification, the Buyer shall be notified to obtain interpretation and clarification.

Table 2-3. Government Documents


49 CFR 393, Subpart I Protection Against Shifting and Falling Cargo

DOE-RL-92-36 Hanford Site Hoisting and Rigging Manual

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3-1

3.0 TECHNICAL REQUIREMENTS

3.1 ITEM DEFINITION

The P-B-1 pump assembly is a vertical axial flow pump driven by an electrical induction motor.

The pump assembly shall conform to Hydraulic Institute Standards, or a proven alternative

design, except as modified and supplemented by this Specification. The assembly drawing of the

pump currently installed is shown in H-2-99028, Sheet 1-4. The P-B-1 pump is in a heavily

shielded, high radiation, pump room, which prevents normal access for typical maintenance,

installation and removal activities. Concrete cover blocks are required to be removed to gain

access to the pump. Activities such as maintenance, installation and removal are to be conducted

via remotely operated tools suspended from an overhead 5-ton bridge crane, which includes the

removal of the Pump Assembly from the installed location to a lower radiation dose area.

The P-B-1 pump consists of the Pump Assembly (motor-shaft-impeller assembly) attached via a

gasketed and bolted flange joint to a pump casing. The pump casing is an integral part of the

evaporator recirculation piping and will not be replaced as part of this scope. The casing is a

bottom suction, side discharge design and is flanged to 28-inch recirculation pipework. The

design of the flanged joint between the Pump Assembly and pump casing is such that the pump

assembly can be removed from the casing, remotely by the overhead bridge crane, to permit

relocation to a lower radiation area for maintenance, or replacement of the remotable

(flange/pump) gasket.

The installed pump casing at the facility will be re-used with new Pump Assembly. The Buyer

will provide a spare pump casing to the Seller for fit-up and testing purposes.

3.2 INTERFACE DEFINITION

3.2.1 Pump Assembly Interface with 242-A Evaporator

The pump interfaces with a pump casing, utilities, facility Monitor and Control System (MCS),

remote impact wrench, and custom lifting device. The pump is lifted using a custom lifting yoke.

Mechanical and electrical interfaces are made using specialty mechanical and electrical

connectors, which will be supplied by Buyer for pump construction. The interfaces are defined

on existing design details. The following interfaces are identified for the pump:

! Pump Casing Interface.

! Electrical Service Interface.

! Shaft Seal – Barrier Fluid Interface.

! Vibration Monitoring System Interface.

! Motor Bearing Grease Lines Interface (Not Available).

! Lifting Yoke Interface.

! Impact Wrench Interface

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3-2

3.2.2 Pump Assembly Interface with Pump Casing

The pump assembly will be flanged onto an existing pump casing in the facility. Integral to the

pump casing are 6 studs to be used for the flange connection. The pump casing is shown on

Lawrence Pumps Inc. Drawing E25252. Two dowels, a long and short dowel on the pump casing

orient the Pump Assembly into position. A custom gasket, called the “Remotable Gasket”,

equipped with lifting bails for remote removal and replacement, is located between the pump

casing flange, and the Pump Assembly to provide recirculation line seal. The Remotable Gasket

is shown on H-2-99028, Sheet 3.

The pump casing suction inlet contains a profiled section, including 5 equally spaced vanes. The

pump axial impeller will interface with this profiled section. The design for the pump axial

impeller is shown in Lawrence Pumps Inc. Drawing A 44106..

3.2.3 Electrical Service Interface

460V electric power will be supplied to the pump through an electrical jumper that includes an

upper terminal connector. This connector will mate with the buyer provided lower connector (H-

2-32401, Sht. 1 & 2, PN3) to be mounted by the Seller on pump assembly. Buyer will not

supply the upper connector for testing purposes. The wiring of the lower connector shall match

the current configuration. See H-2-99028, Sheet 1 for motor electrical wiring diagram and wire

size requirements.

3.2.4 Shaft Seal – Barrier Fluid Interface

The current pump uses a double-acting balanced, cartridge seal, which uses a barrier fluid for

sealing cleaning and cooling. If required for the new pump shaft seal, two barrier fluids are

available. During operation, filtered raw water, filtered to 5 microns, is used initially as the

barrier fluid. Once the waste evaporation process is running, seal barrier fluid is switched to

process condensate, which is slightly cleaner than the raw water, and reduces water additions to

the process. The seal barrier fluid has the following parameters:

Min Pressure 35 psig

Max Pressure 90 psig

Min Flowrate 0.25 gpm

Max Flowrate 0.3 gpm

Max Temperature 120 o F

Ph (Process Condensate) 9-11

Max Ammonia Content 0.15 mol/l (6.8 g/l)

The seal barrier fluid will be provided to the pump through a jumper that mates with the Buyer

furnished 2-inch and 3-way connector nozzle (See Drawing H-2-32447).This connection is

configured with a seal water supply line, a seal water return line, seal water drain and seal cavity

drain line as shown in H-2-99028, Sheet. 1. A drain is available at the facility to capture any

water drainage from the seal.

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3-3

3.2.5 Vibration Monitoring System Interface

There are three vibration sensors mounted in the existing motor. These three vibration sensors

terminate at a 13-point lower electrical connector (H-2-32401, Sheet 1). This connector is

mounted on the Pump Assembly and mates with the upper connector (H-2-32401, Sht. 3) which

is part of a removable jumper that connects to site MCS. Three wire pairs are available for this

application. The vibration monitoring transducers communicate with the facility MCS via 4-

20mA signals. Additionally, plug connections, where manual data can be collected, for each

vibration sensor are available at the facility. The current design includes the vibration transducers

are wired as shown on H-2-99028, Sheet 1.

3.2.6 Motor Bearing Grease Lines Interface (Not Available)

The original design included a 2-in, 3-way connector for the motor bearing grease lines. This

jumper is no longer used. The pump currently installed at the facility has been refurbished by

replacing the lower radial bearing for the pump motor with a sealed bearing and replacing the

grease supply lines to the upper bearing with localized zerk fittings. Sealed bearings are

preferred.

3.2.7 Lifting Yoke Interface

The current pump design is configured with lifting bails that mate with a purpose-built lifting

yoke (see H-2-99046). The lifting features of any new Pump Assembly should mate with the

yoke. The location of these features should ensure that when the Pump Assembly is lifted in the

vertical position using these lifting bails and lifting yoke it hangs level and plumb to support for

installation and removal of the pump. Seller shall provide the required lifting device if

modifications to the location and/or configuration of the lifting bails are made.

3.2.8 Impact Wrench Interface

The current pump design is configured with 6 studs & accompanying free nuts to flange the

pump assembly with the casing. A remote impact wrench, as shown in 1402-WRP-041B, is used

to make this flange connection. The Pump Assembly shall ensure enough clearance is provided

to engage the remote impact wrench with the free nuts.

3.2.9 Interface Critical Dimensions

The new P-B-1 pump will be installed in an existing recirculation loop in which the piping has

little tolerance for modification. Therefore, the critical dimensions of the P-B-1 pump are the

dimensions that affect the interface points of the pump assembly with the facility which include,

but not limited to:

1. The pump assembly flange/pump cover dimensions,

2. Location of all connections to existing facility utilities including vibration transducer

signals,

3. Pump casing and its internal features.

4. Lifting bail location.

5. Access for removal and handling of the new pump.

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3-4

The Seller is responsible for identifying any modification to the pump that can affect the critical

dimensions. The Buyer shall review and approve any of these modifications.

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3.3 CHARACTERISTICS

3.3.1 General Requirements

The Pump Assembly shall be designed, fabricated, examined, tested, packaged, and shipped in

accordance with the codes and standards listed in this Specification. Any deviation from the

referenced codes and standards shall have prior approval from the Buyer. If any conflicting

requirements are identified within this Specification,, deviations from such requirements, shall

have prior approval from the Buyer.

Drawing H-2-99028, Sht. 1-4, represents an existing installed pump and may be used for

component type, arrangement, connection position and orientation, and dimensions to ensure

interchangeability of the pump assemblies. This Specification supersedes any equivalent

references found on these drawings. Unless specifically approved by the Buyer, all components,

fabricated parts, and assemblies supplied by the Seller shall be fully compatible with the pump

casing furnished by the Buyer.

3.3.2 Fluid Characteristics

The pump shall move a radioactive slurry with a range of physical properties listed in Table 3-1.

Table 3-1. Fluid Properties (Slurry)

Waste Property Range

Specific Gravity 1.0 – 1.8

Viscosity, cP 1 - 140

Temperature (flushes/transfers) 40 to 200∀F

pH range - Normal 7-15

pH range – Acid Flush 1 - 7

Particle Size (Micron) 15 – 1000

Hardness 3 – 5 MOHS Scale

Abrasiveness, Miller Number (ASTM G75-82) < 100

Solids Loading (vol %) 0% - 30% by vol

Sodium Hydroxide 0 – 8.0 M

Sodium Aluminate 0 – 3.0 M

Sodium Nitrate (NaNO3) 0 – 5.0 M

Sodium Nitrate (NaNO2) 0 – 4.43 M

Sodium Carbonate 0 – 2.0 M

Sodium Phosphate 0 – 0.21 M

Water 100 – 30% by weight

Total Organic Constituents 0 – 80 gm/L

NaF (for pH 7 only) 0 – 0.6 M

Ammonia 0 – 0.4 M

NaCl (for pH 7 only) 0 – 0.6 M

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The P-B-1 pump will recirculate a slurry stream that is being evaporated. The process begins by

introducing and recirculating water. Then vacuum is applied (to nominally 60 torr) and steam is

applied to heat the recirculating fluid to the boiling point. The liquid portion of the tank waste

(supernatant) is added continuously to the evaporator/separator system until the slurry is

concentrated to a density, typically 1.37 – 1.42, which provides the required volume reduction.

Once the target density is reached, flow to a receiver tank is initiated (via another pump), and the

process runs continuously until the source material is exhausted, or processing objectives are

met.

When concentrated, the stream being recirculated is a slurry, consisting of a concentrated salt

solution with precipitated salts. The precipitated salts are predominantly natroxalate (sodium

oxalate), thermonatrite (sodium carbonate), natrophosphate, kogarkoite, and nitratine (sodium

nitrate). Small volumes of other salts or insoluble solids are possible.

3.3.3 Pump Functional Characteristics

The pump shall have a stable head/capacity curve that continuously rises from run-out to shut-

off. The hydraulic requirements of the pump are detailed in Case 1, shown in Table 3-2. Pump

maintenance will be preceded by pumping a decontamination solution described in Case 2.

Attachment A provides the pump curve for the current pump.

Table 3-2. Pump Performance Characteristics

Parameter Case 1 Case 2

Media Pumped Slurry per Table 3-1 Water

Temperature 200 oF (max) 210 oF

Specific Gravity 1.8 (max) 0.96

pH Normal 7 - 15 7.0

pH Acid Flush 1 - 7 -

Vapor Pressure 12 psia 14.1 psia

Viscosity 10 – 140 cP 0.3 cP

Rated Conditions Case 1 Case 2

Flow 14,000 GPM 16,100 GPM

Total Dynamic Head 21.0 ft. 10.85 ft.

Static Suction Head 26.4 ft. 26.4 ft.

Suction Pressure 3.91 psig 10.22 psig

3.3.4 Pump Physical Characteristics

3.3.4.1 Pump External Physical Characteristics

a) The pump assembly shall be a pullout design (e.g. Pump Assembly to be removable

without removing pump casing). The Pump Assembly, the remotely installed gasket, and

all services to the pump will be installed and removed by a remotely controlled 5-ton

bridge crane and a remotely controlled impact wrench.

b) The design shall minimize the collection or holdup of liquid on the external pump

surfaces. The design shall allow for easy wash-down of external surfaces during removal.

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c) Adequate vertical approach clearance shall be maintained around nut retainers to permit

access by a remotely operated impact wrench (reference drawing H-2-31103). For this

reason, the current design limits the motor diameter not to exceed 36”.

d) The pump assembly height shall not be greater than 5’-7” when installed (i.e., from the

bottom of the pump flange/cover to the top motor). This is to avoid any interference with

the concrete cover blocks used at the facility.

3.3.4.2 Pump Internal Physical Characteristics

a) The pump shall be self-draining with no internal traps, which can retain liquids.

b) The pump shall be provided with balanced double silicon carbide mechanical seals,

unless specifically agreed otherwise with the Buyer in writing. Five-micron filtered water

or process condensate [See Section 3.2.4 for parameters] are available for shaft seal purge

and cooling. Static pressure of the pumped fluid at the pump cover shall be no greater

than 10 psig.

c) The design pressure of the shaft seal chamber shall be a minimum of 90 psig.

d) The impeller shall be dynamically balanced in accordance with ISO 1940-1.

e) The pump shall be designed such that there is no significant (first or second, as a

minimum) critical speed within 25% (above or below) of operating speed at any

operating condition, as verified in the Seller’s calculations.

f) The rotor assembly shall be sized and supported to minimize vibration and promote

maximum bearing life.

g) Surfaces that will be regularly wetted with the pumped process fluid require special

considerations to minimize areas that could trap or hold contamination. Areas of concern

include:

! Exposed bolt threads,

! Crevices between pump and seal flanges,

! Impeller hub area.

3.3.4.3 Pump Motor Characteristics

a) The motor shall be in accordance with NEMA Standard MG-1, Type B. The motor shall

be 460 V, 3-phase, 60 Hz., operating at 720 rpm rated at 200 HP (electric). The insulation

system shall consist of minimum Class H, or better, insulation material. See motor data

sheet in Appendix B. Note the service factor in the Data Sheet should be 1.15 not 1.5.

b) Motor horsepower capacity shall not be exceeded when operating at any point on the

pump curve, with the fluid specified in Section 3.3.2 of this Specification.

c) The motor #1 wire leads from the windings shall be spliced to the #4 SA 125 leads in the

motor J Box using bolted type connections and encased from there in a flexible carbon

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steel liquid tight conduit that is connected to the lower electrical connector. The Seller is

responsible for providing a NEMA 3R motor connection box.

d) The procedures given in IEEE STD. 118 and IEEE STD. 119 should be used when

measuring the resistance of the stator winding (and the rotor winding on wound-rotor

machines).

e) Motor bearings shall be constructed and lubricated to maximize service life. The motor

thrust bearing can carry the thrust load of the pump as well as the rotor weight.

f) A vibration monitoring system shall be provided which shall include monitoring in 3 axes

(e.g., vertical, horizontal & lateral). The vibration monitoring system components shall be

in accordance with the following description:

1. Vibration Transducer(s) with matching connector and manufacturer's standard

pigtail cable assembly shall be installed on the motor. The cable shall be

terminated in a NEMA 3R junction box installed on the motor frame.

2. Signal conditioning amplifier for peak to peak (mils) displacement monitoring

and indication, with high and low alarms, and internal calibration and controls, in

a rack mountable case for Buyer's 120V AC, 60 Hz power supply.

3. Vibration spectrum analysis capability is a desired upgrade from original.

3.3.5 Reliability

a) The operating regime for the pump includes up to 4, short duration campaigns, of

approximately two weeks each through a typical year. The recirculation pump is expected

to operate for up to 10,000 hours of intermittent operation over a 10-year period with

minimum preventive maintenance, which may include no maintenance.

b) During the intervening periods of downtime restrictions due to radiation prevent

personnel access to perform manual maintenance servicing or repair in situ. The pump

shall be designed to accommodate this duty.

3.3.6 Maintainability

a) The pump will be flanged into a recirculation loop in a high radiation environment that

restricts manual access for normal maintenance activities. All design changes that affect

maintenance requirements for the pump shall be approved by the Buyer.

b) The Pump Assembly shall be interchangeable as a complete unit and in component parts

for ease of maintenance.

c) Preventive maintenance provisions to account for layups and long term storage shall be

considered by Seller. Specifically, a method to manually rotate the rotating assembly

shall be considered. Seller shall provide a recommendation for such provisions to be

approved by Buyer.

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3.3.7 Environment

The following are the ambient conditions for which the P-B-1 pump assembly shall be designed:

Temperature, °F: 120

Pressure: Atmospheric

Relative humidity, %: 15 to 90

Radiation Level, R/hr: 300

3.4 DESIGN AND CONSTRUCTION

Hydraulic Institute Standards, or proven alternative design standards, shall be considered an

integral part of this Specification, and shall be complied with except as modified or

supplemented herein. The pump shall be designed and constructed in accordance with the

manufacturer’s standard practices and approved design and fabrication details.

The Seller shall prepare a Pump Design Report that documents the material selection, design,

analysis (including calculation package), component Specification data, electrical product

acceptability, drawings for the pump and motor driver, and a 3-dimensional computer aided

design solid body model of the pump assembly compatible with SolidWorks®.

Following completion of fabrication, assembly and testing, the Seller shall develop a Final Pump

Data Package to include Pump Design Report, all testing procedures and results documentation;

completed shop travelers, welder qualifications and nondestructive examination (NDE)

procedures with NDE personnel qualifications; chemical and physical test reports;

inspection/examination reports; updated vendor data and as-built drawings including a finalized

3-dimensional computer aided design solid body model of the pump assembly; installation,

operation and maintenance manuals; and spare parts list.

3.4.1 Seismic Design/Analysis

The Seller shall provide a seismic analysis in accordance with TFC-ENG-STD-06, Design Loads

for Tank Farm Facilities, to ensure the pump maintains structural integrity after a seismic event.

For the structural analysis the following input requirements and assumptions shall be used:

a. Load combinations, allowable stresses and strength requirements shall comply with the

International Building Code (IBC) and American Society of Civil Engineers (ASCE) 7.

b. Design spectral response accelerations applicable:

SDS (short periods) Vertical = 0.346g Horizontal = 0.588g

SD1 (1 second period) Vertical = 0.098g Horizontal = 0.192g

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c. IBC Seismic Use Risk Category I/II, Seismic Design Category D, with Importance Factor

of 1.0.

d. There is no design requirement that the pump remain functional following a seismic

event; however, it is a design requirement that the pump assembly retain its structural

integrity and to be removable following such a seismic event.

e. Additional inputs for seismic analysis to be provided by Buyer as needed.

3.4.2 Rotor Dynamic Analysis

The Seller shall provide a rotor dynamic analysis supporting the rotating element design and

support features, ensuring minimum vibration and high reliability. This analysis shall be used to

verify that there are no damaging responses in the lateral or torsional rotor dynamic modes of

vibration at the operating speed of the pump.

3.4.3 Critical Speed Analysis

The Seller shall provide a natural frequency analysis to demonstrate that there is no significant

(first or second, as a minimum) critical speed (wet) within 25% (above or below) of the pump

assembly operating speed.

3.4.4 Pump Assembly Installation and Lifting & Handling Design/Analysis

Installation of the pump will be by overhead bridge crane with 5-ton capacity. The Pump

Assembly will be lifted in the vertical position using lifting attachments on the assembly and a

lifting yoke (H-2-99046). The pump shall be designed to hang in a vertical orientation so that it

can be installed in the pump casing using an overhead crane. The Seller shall provide rigging and

handling instructions.

All crane and rigging shall be in accordance with DOE/RL-92-36 the Hanford Site Hoisting and

Rigging Manual, and the Buyer’s procedures. The manufacturer may use the following

Specifications for hoisting and rigging or provide lifting instructions proprietary to the

manufacturer.

3.4.4.1 Lifting Attachments and Equipment Design

The pump should use the lifting bail design of the current pump configuration. The current

design or any alternative designs for the lifting attachment(s) on the pump (lifting eyes, lugs,

ears, etc.) and the lifted item shall be designed/evaluated in accordance with RPP-8360, Lifting

Attachment and Lifted Item Evaluation, except that ASME BTH-1 should be used to verify

lifting lugs hole diameter compared to the shackle pin diameter (the D to d ratio). The design

shall consider equipment orientation, i.e., vertical. Other appropriate design standards may be

used with the approval of the Buyer. Hoisting and rigging device or equipment designs, tests, and

reports shall be submitted to the Buyer for safety evaluation and approval during design review.

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3.4.4.2 Below-the-Hook Lifting Device Requirements

If below the hook (BTH) lifting devices are needed, then the structural and mechanical below the

hook lifting devices, as defined by ASME B30.20, Below-the-Hook Lifting Devices, shall

conform to the requirements of ASME B30.20. The design of BTH devices shall conform to the

requirements of ASME BTH-1, Design of Below- The-Hook Lifting Devices. Load supporting

devices not clearly defined as BTH shall be clarified by contacting the Buyer for interpretation.

The Seller shall submit documentation and calculations to the Buyer as evidence that the

appropriate welding codes, qualified welders, non-destructive examination procedures, testing

requirements, etc., have been used. Calculations will be required for the design of all BTH

devices and associated lifting points. Below-the-hook lifting devices shall be load tested to 125%

of the rated load as required by DOE-RL-92-36. All custom designed Hanford Site lifting

devices shall be rated for cold weather temperature of at least 10 °F.

BTH lifting devices shall be provided with markings in accordance with ASME B30.20 and tags

in accordance with DOE/RL-92-36. In addition to the requirements of ASME B30.20 and

DOE/RL-92- 36, the marking shall include Hanford drawing number (if applicable), special

lifting instructions, and clearly indicate lifting attachments. The marking shall be in the form of a

name tag, name plate, or other permanent marker.

The above requirements do not apply to the existing BTH shown on drawing H-2-99046.

3.4.4.3 Pump Lifting and Handling

Lifting instructions and lift diagrams shall be provided. The lift diagram must show estimated

weight and center of gravity. The Pump Assembly must be level and plumb when suspended,

which will need to be determined visually. The design shall consider the pump orientation. All

lift points, both permanent and temporary (if necessary), shall be identified on the pump

assembly.

The Seller shall provide a lift analysis to ensure the fully assembled pump can be lifted without

distortion, damage, or exceeding allowable stresses when using the existing crane and BTH lifter

or new BTH lifter. Any temporary attachment points on the pump at a location analyzed to

prevent pump damage shall be clearly identified.

The Seller shall detail any special handling requirements in the instruction manual to ensure that

the Pump Assembly can be safely lifted and installed without damage to the pump. The plan

shall address righting the pump if shipped horizontally. All drawings and procedures required for

pump installation/removal and operation shall be included in the manual for quick reference. All

lift/attachment points shall be designated in the Shipping and Handling Plan (See Section 6.3).

The pump assembly should be stored and transported vertically to prevent damage. The Seller

shall design and provide a stand compliant with AISC, Steel Construction Manual, to allow the

pump rotating assembly to be loaded, and off-loaded from a truck trailer via two methods:

! A single crane utilizing the lifting yoke (H-2-99046) or BTH lifting device attached to

designated lift points.

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! Single forklift utilizing designated engagement sleeves built into the stand.

The pump assembly installed on the stand will enter the facility via a 11’ 6” tall door. Preferably,

the stand would provide sufficient clearance to remove the impeller for maintenance (min. of 14”

is required) and provide enough clearance to get pump assembly installed on the stand through

the door.

3.4.4.4 Welds / Critical Welds

All critical welds on the equipment shall be identified in the design media. For the purpose of

this requirement, critical welds are defined as those welds whose failure could result in loss of

load or loss of load control. All critical welds on lifting devices shall be full-penetration welds,

if possible, and shall be verified by approved NDE.

3.4.5 Materials

a) Materials must be selected by the Seller based on acceptable performance when subjected

to the environmental exposures described in Sections 3.3.2 and 3.3.3.

b) Material and components shall be new.

c) All metallic portions of assembly in contact with either the pumped fluid or seal water

shall be stainless steel of suitable type and grade for the purpose intended except the

impeller shall be ASTM A890, with supplemental requirement S32 (tensile test). Note

previous specifications for impeller material specified ASTME A 744 Grade CD4MCU.

Pipe and/or tubing for seal water shall be seamless stainless steel. Motor frame, lifting

attachments, fasteners, and other external components can be carbon steel. Seller to

provide recommendation for impeller material to be approved by Buyer.

d) Material selection shall be identified within the design data for Buyer review, and

material certification data shall be submitted prior to shipment for Buyer approval.

Material identification shall include the applicable ASTM Specification number and any

proposed supplementary feature listed as optional in the ASTM Specifications. Material

certification shall present the results of chemical analysis and physical tests required in

applicable ASTM Specifications.

e) Brass, bronze, and copper base materials, if used, shall not come in contact with the

pumped waste fluid. The use of aluminum is not acceptable.

f) The materials of construction shall be chosen to prevent differential thermal expansion of

the individual pump components (i.e. shaft) from adversely affecting the performance of

the pump over the specified range of operating temperatures.

g) All major pressure boundary and rotating parts shall be furnished to ASTM material

specifications and shall include Certified Material Test Reports (CMTRs).

h) Materials used for other parts shall be clearly identified on the bill of material as to

material type and grade; however, CMTR are not required. Materials shall be non-

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asbestos, non-absorbent and suitable for the chemical and radiation environment in which

they are used. All elastomers used shall comply with TFC-ENG- STD-34, Standard for

the Selection of Non-Metallic Materials in Contact with Tank Waste.

3.5 DRAWINGS AND MANUALS

a) As-built, detailed, dimensioned assembly drawings shall be submitted to the Buyer for

approval. Drafting shall be done according to applicable ASME Y14 series standards

(ASME Y14.1, Y14.2M, Y14.3, Y14.5 and Y14.38). As-built dimensions shall include

the following at a minimum:

1. Distance from the bottom of the pump impeller to the base of the pump flange

plate (not including the gasket thickness).

2. Distance from the bottom of the pump flange plate (not including the gasket

thickness) to the top of the motor.

3. Distance from the end-face and applicable centerlines of each mechanical

connection to a single datum to allow the fabrication of future piping spools.

b) All component parts shall be listed in the bill of materials, referring to the applicable

material Specifications or manufacturer and part number or supplier’s fabrication

drawing.

c) A manufacturer’s Installation, Operation and Maintenance (IOM) manual shall be

supplied with the pump. Instruction manuals shall contain storage, installation/removal,

start-up, operation and maintenance instructions for the pump and all associated

equipment. As discussed in Section 3.4.4.3, lifting instructions including lift diagrams

shall be included in the IOM manual.

3.6 FABRICATION/ASSEMBLY PROCESSES

a) Welding of pump pressure-containing components or any repairs to such parts shall be

performed in accordance with ASME B31.1.

b) Welding of structural members, as well as any repairs to such parts, shall be performed in

accordance with the applicable AWS welding standard (i.e. AWS D1.1 for steel or AWS

D1.6 for stainless steel) for statically loaded structures, as applicable.

c) Machining or grinding of stainless steel shall be done with tools that have never come in

contact with materials other than stainless steel. In addition, the following shall apply:

! Wire brushing of stainless steel shall be done using stainless steel brushes that have

never been used on materials other than stainless steel.

! Grinding wheels shall be resin-bonded aluminum oxide.

! Rotary files shall be faced with tungsten carbide.

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d) Metallic material-handling devices used for machining, positioning, supporting, welding,

etc. that come in contact with stainless steel shall be made of stainless steel. It is

acceptable to use high-strength carbon steel clamping devices such as machine chuck

jaws on stainless steel, provided the Seller has a program or procedure for ensuring that

the stainless steel has not been contaminated by the carbon steel. This procedure shall be

available at the Seller's facility for the Buyer's review.

e) The finish for structural shapes and plate surfaces shall be mill finish, 125 RMS on cut

surfaces and machined surfaces shall be 250 micro inches RMS finish or better to achieve

function.

f) The nozzle and electrical connector locations to be “As Built” to the nearest 1/64”.

3.6.1 Cleaning and Painting

a) Before delivery to the site, the pump and all associated components shall be cleaned with

a cleaning procedure or plan prepared by the Seller and submitted to the Buyer for

approval prior to use. Pump and all associated components shall be clean to the extent

such that extraneous materials, such as those listed below, are not present.

! Metallic or other dusts (shop dust), chips, and turnings

! Abrasive particles or dirt

! Weld splatter

! Rust and other loose corrosion products

! Magnetic/liquid penetrant residues, dye check, etc.

! Foreign material, such as paper, plastic, wood, tape or tape adhesive

! Cutting oils

! Excess lubrication grease and oil

! Marking dyes

! Residual test fluids

b) Cleaning solutions shall not contain halogenated compounds. Solvents and cleaning

solutions used on stainless steel shall not exceed 25 ppm for halides and less than 50 ppm

for chlorides.

c) Mechanical cleaning tools used on stainless steel shall not have been previously used on

carbon steel or any other materials that would contaminate stainless steel surfaces.

d) Exposed carbon steel components shall be protected with an epoxy paint. Powder coating

is an approved alternative to paint, color shall be gray or as specified by the Buyer. The

color of free nut retainers and lifting bails shall be yellow. Supports for nozzles and

brackets shall be a different color than the motor.

e) Stainless steel components do not require painting except as needed for identification or

for targeting. Paint used on stainless steel shall be epoxy-phenolic or Buyer approved

alternate.

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f) The following areas of the pump shall be painted yellow for targeting.

! A 1-1/2-inch band around the top of dowel guides/holes or as space permits.

! Nozzle kick plate.

! The top portion of lifting bails.

g) Identification shall be painted on the pump as described in Section 3.6.3.

h) Visual direction indicating disk on top of the motor shall be painted half red and half

yellow.

3.6.2 Special Tools

a) Special tools and fixtures required to disassemble, assemble, lift, or maintain the pump or

associated components shall be included in the quotation and furnished with delivery of

the unit.

b) Each tool shall be labeled to indicate its intended use, with instructions in the manual on

its use. Any special tooling required shall be supplied by Seller at a minimum of 2 each.

c) The pump is to be placed, secured, and delivered utilizing an appropriate fixture (stand).

3.6.3 Marking

a) The pump identification number (P-B-1) shall be as stated in the procurement

documentation. The pump identification number, this Specification number and revision,

and the weight of the complete pump assembly, shall be painted on the motor frame. The

numbers/letters shall not be less than 1 in. high block type, black on yellow background.

The use of a vinyl decal, minimum 3 mil thickness, is acceptable for identifying only the

Specification number/revision and weight.

b) The pump shall have a manufacturer's nameplate with the following minimum

information:

! Flow(GPM),

! Head (ft.),

! Horsepower (HP),

! RPM,

! Impeller Diameter,

! Assembly weight,

! This Specification number and revision,

! Purchase order number.

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4.0 QUALITY ASSURANCE REQUIREMENTS

4.1 QUALITY ASSURANCE PROGRAM

a) The Seller shall comply with the quality assurance requirements stated in the

Procurement Documents.

b) The Seller shall have a Quality Assurance Program (QAP) that establishes quality

control.

a) Once the Seller's QAP is approved by the Buyer, any deficiency to the approved contract

or QAP must be reported to Buyer for evaluation. Reports shall be in writing and

submitted within 24 hours of the identification of the deficiency.

b) The QAP shall apply to all activities, including subcontracted activities and work

performed for the Buyer.

4.2 QUALIFICATIONS

4.2.1 Welding Personnel and Procedures

Personnel and procedures for welding pressure-retaining components along with attachments

thereto, shall have been qualified in accordance with ASME B31.1, paragraph 127.5 prior to the

start of welding. Personnel and procedures for welding structural components shall have been

qualified in accordance with the applicable AWS welding standard (i.e. AWS D1.1 for steel or

AWS D1.6 for stainless steel) prior to the start of welding (welding qualifications and procedures

per ASME B&PVC, Section IX are acceptable).

In lieu of qualification of Welder Procedure Specifications (WPSs), Standard Welding Procedure

Specifications (SWPS) developed and controlled by the AWS and accepted in Article V of

ASME B&PVC Section IX may be utilized within the specific limitations of ASME B31.1

paragraph 127.5.4. The AWS is considered a responsible and recognized organization and prior

approval is not required. If utilized, SWPS shall be demonstrated and documented in accordance

with ASME B31.3 and ASME IX (QW-100.1, Article V and Appendix E). Document

demonstration tests using Form QW-485 (from ASME B&PVC Section IX) or equivalent form.

SWPS shall be demonstrated prior to the start of welding. Documentation tests are considered

synonymous with qualification of a WPS in accordance with ASME B&PVC Section IX, QW-

100.3 and the current edition and mandatory addenda of ASME B&PVC Section IX shall be

used.

A copy of welder performance qualification test results and renewal of qualification

documentation shall be maintained at the jobsite for the Buyer's evaluation, if desired. A copy of

the Weld Procedure Specifications, Procedure Qualification Records, and Supporting

Demonstration Records, as applicable, shall be maintained at the jobsite for the Buyer's

evaluation, if desired.

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4.2.2 Welding Inspectors and Procedures

Visual weld examinations shall be performed, and appropriate documentation prepared by

Certified Welding Inspectors (CWI) who have received certification in accordance with AWS

QC1. Certified Associate Welding Inspectors (CAWI), certified in accordance with AWS QC1,

may perform examinations when under immediate direction of Certified Welding Inspectors.

Qualification/certifications of CAWI and CWI under whom the examinations were performed,

shall be included in the Pump Final Data Package.

Personnel performing nondestructive examination shall be certified in accordance with Seller's

written practice, which shall meet requirements of ASNT-SNT-TC-1A. Level II or III personnel

shall be used to interpret test results.

The Seller shall maintain a file containing personnel certifications and nondestructive

examination performance procedures as applicable at the fabrication site for Buyer's evaluation,

if desired.

4.3 INSPECTIONS AND TESTING

a) The Seller shall develop a fabrication, inspection, and test plan (FIT plan) that sequences

the fabrication operations and denotes the Seller’s inspection and test points. The FIT

plan shall be reviewed and approved by the Buyer prior to the start of fabrication. At the

time of the review of the FIT, the buyer shall specify all applicable witness and hold

points.

b) The Buyer reserves the right to witness all tests listed below and shall be given a

minimum of ten working days’ written notice prior to each test date. It should be noted

that third party inspectors may be required to be present during testing as the

representative for the Buyer or an independent representative for the Buyer’s

stakeholders. The following includes the witness/hold points for the Buyer and/or their

representative for specific points in the fabrication/testing process:

! Welding and NDE of pressure retaining components (Section 4.3.1),

! Megger Testing (Section 4.3.3),

! Pump Motor Driver Testing (Section 4.3.4),

! Hydrostatic pressure testing (Section 4.3.5),

! Pre-pump run-in performance test (Section 4.3.6),

! Pump sealing system leak check (Section 4.3.8),

! Pump run-in test (Section 4.3.7). Only the start and finish of the 24-hr run-in test need

to be witnessed to ensure proper operation of the pump assembly,

! Post-pump run-in performance test (Section 4.3.9).

Any additional witness/hold points for the Buyer and/or their representatives will be

specified during their review and approval of the FIT plan.

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4-3

c) Prior to the performance of these tests, the Seller shall submit a procedure for each test to

the Buyer for review and approval. Test information recorded or calculated shall be

documented and submitted to the Buyer.

d) Inspection/examination of the pump assembly shall be in accordance with applicable

Hydraulic Institute Standards, or other appropriate standards.

e) Verification shall be performed all on critical dimensions. The Buyer will provide critical

as-built dimensions for the existing design and required tolerances to Seller. The Seller is

responsible for verifying the location and dimensions that affect interface points of the P-

B-1 Pump (See Section 3.2.3) are in accordance with the Buyer approved fabrication

drawings.

f) The Seller shall submit all nonconformance reports (NCRs) that specify “Use-As-Is” or

“Repair” to the Buyer with a proposed disposition for approval. Work related to that

NCR shall not proceed until the NCR disposition is approved by the Buyer.

g) NDE reports and radiographs shall be traceable to the item examined, include all essential

examination parameters, and signed and dated by the NDE examiner. These reports and

radiographs shall be submitted for approval by the Buyer prior to shipment of completed

items.

h) For measuring and test equipment (M&TE) used in examination/inspections and testing,

the Seller shall provide legible, reproducible copies of Certificates of Calibration

traceable to the National Institute of Standards and Technology or other documented

evidence must be submitted stating the basis of the calibration. This is not required for

commercial equipment such as timing instruments, rulers, tape measures, and levels, if

such equipment provides the required accuracy.

i) Where NIST compliance is required, Measurement and Testing Equipment used in the

tests shall comply with NIST Handbook 143.

j) A pump casing will be furnished by the Buyer. The spare pump casing will be shipped to

the Seller to use for testing purposes. The pump casing is shown on Lawrence Pumps Inc.

Drawing E25252.

k) A vertical 2”, 3-way connector (Drawing H-2-32427, Assembly 2) will be supplied by

the Buyer to facilitate the Seller's testing that is required.

l) Final test reports shall be submitted with shipment. Pump tests shall be conducted in

accordance with Hydraulic Institute Standards (ANSI/HI 14.6). Data and test results shall

be obtained and presented as outlined in the standards.

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4-4

4.3.1 Weld Inspection and Examination

Piping and containment welds, joints, and attachments thereto shall be examined in accordance

with ASME B31.1 for normal service. Volumetric examination [radiographic test (RT) or

ultrasonic test (UT)] of welds where specified by ASME B31.1 shall be performed where

possible (i.e., in-process examination shall not be specified). 100% of RT of pipe butt welds,

with the exception of grease lines, per ASME B31.1 shall be performed.

Inspection and examination of structural welds shall be performed in accordance with the

applicable AWS welding standard (i.e. AWS D1.1 for carbon steel or AWS D1.6 for stainless

steel). Welding qualifications and procedures per ASME B&PVC, Section IX, are acceptable. In

accordance with original drawings, 100% liquid penetrant testing on structural welds cover pass

per applicable AWS standard shall be performed.

All welds shall be visually inspected as a minimum. The seller shall perform 100% visual

examination of all root and cover welds for the pump and pipe pressure containment welds. Weld

maps shall be prepared and submitted. Non-destructive examinations, including Visual,

Penetrant Test, Radiographic Testing, or Magnetic Particle Test examinations, shall be recorded

and submitted. Radiographic Testing film shall be included as part weld documentation submittal

if Radiographic Testing was performed.

Certified weld examination reports shall be provided.

4.3.2 Radiographic Examination of Impeller

The finished propeller shall be given a 100% X-ray examination per ASTM E 446 and E 186 as

determined by the thickness of the material examined. The classifications from which to

determine the radiographic standards to be used for evaluation of defects shall be:

Under ASTM E 446 Under ASTM E 186

Category Severity Level Category Severity Level

A 5 A 4

B 5 B 4

C 5 All types C 4 All types

D 1 D 1

E 1 E 1

F 1 F 1

G 1

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4-5

4.3.3 Megger Test

A megger test shall be conducted on the pump motor. Prior to the megger test perform a

continuity check between the phases to ensure no shorts exist. The megger test shall be

conducted between each phase and the ground individually. The acceptable value is greater than

or equal to the values in MG-1. Measured megger resistances shall be recorded. Resistance

measurements shall be corrected for temperature and documented in the test results.

4.3.4 Pump Motor Driver Testing

The motor shall be given the following testing listed below to demonstrate that it is free from

mechanical and electrical defects. The testing shall be conducted in accordance with ANSI/IEEE

Standard 112.

This testing shall include:

! Typical tests on completed assembly motors per NEMA MG-1, Section 12.55.

! ANSI/IEEE Standard 112, Method B, dynamometer test

! ANSI/IEEE Standard 112, Locked rotor tests

! Vibration Tests: For vibration refer to NEMA MG 1 Part 7, IEC 60034-14 [B4], API 541

[B2], or other specified standards as applicable. Vibration displacement, measured at the

outer edge of the mounting flange, shall not exceed 0.002 inch under any stable operating

condition of the pump.

! Test voltage: The commonly specified AC high-potential test voltage for factory testing

of new stators is 1000 V plus two times the rated voltage of the machine.

! Speed-torque and speed-current curves: The speed-torque characteristic is the

relationship between torque and speed, embracing the range from zero to synchronous

speed for a motor and from synchronous speed to pull-out speed for an induction

generator. This relation, when expressed as a curve, will include maximum (breakdown),

pull up or pull out, and locked-rotor torques. A speed-torque and speed-current curve test

shall be performed using whichever method the supplier choses.

4.3.5 Hydrostatic Test

a) The pump casing with pump assembly installed shall be hydrostatically tested at a

pressure of 50 psig. There shall be no drop in pressure when under test for 4 hours.

b) Water used for hydrostatic and performance testing shall be tested for chlorides if

austenitic stainless steel wetted materials are present. The chloride content of the test

medium shall not exceed 50 ppm for water temperatures of < 149 °F.

c) A test certification shall be provided with final data submittals.

4.3.6 Pre-Pump Run-In Performance Test

A performance test, performed prior to the pump run-in test, shall be conducted using the fully

assembled pump in accordance with Hydraulic Institute Standards (ANSI/HI 14.6). The

performance test shall obtain sufficient data points, including rated performance point and run-

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4-6

out, to plot a full performance curve at the rated speed. The following shall be recorded and/or

calculated:

! Flow rate

! Total head

! Power input

! Pump efficiency

! Actual speed (rpm)

! Motor amperage and voltage (one each phase)

! Pump Vibration

Following pump testing, the Seller shall prepare a certified correct pump curve reflecting pump

performance at the discharge nozzle with water. Information shall include impeller type and size,

head/flow curve, and estimates of BHP @ maximum specific gravity (1.8), efficiency, and

NPSHR. Information shall include high- and low-end allowable operating regions and any

limitations of operation.

4.3.7 Pump Run-in Test

A run-in test shall be performed on the fully assembled pump. The run-in test shall be performed

in compliance with Hydraulic Institute Standards (ANSI/HI 14.6), and be conducted for a

minimum of 24 hours of continuous operation, with the pump operating at the rated performance

point. As a minimum, the following readings shall be determined and recorded every 30 minutes

during the test: Flow rate, total dynamic head, NPSH, power input, actual speed (rpm), motor

amperage and voltage (on each phase), and pump vibration.

4.3.8 Pump Sealing System Leak Inspection

The pump shaft sealing systems shall be inspected for operation and any leakage of the pumped

fluid into the barrier fluid. No observable leakage shall be permitted. Mechanical seal and

assembled seal water supply lines shall be leak tight to 135 psig.

Leak test for the remotable gasket shall be performed at 14 psig. See H-2-99028, Sht. 3, note 4

for details.

4.3.9 Post-Pump Run-In Performance Test

A performance test, performed after to the pump run-in test, shall be conducted using the fully

assembled pump. The intention of this test is to validate that the pump run-in has not degraded

the performance of the pump. The performance test shall obtain sufficient data points, including

rated performance point and run- out, to plot a full performance curve at the rated speed. The

following shall be recorded and/or calculated: Flow rate, total head, power input, pump

efficiency, actual speed (rpm), and motor amperage and voltage (one each phase).

Following pump testing, the Seller shall prepare a certified correct pump curve reflecting pump

performance at the discharge nozzle with water. Information shall include impeller type and size,

number of stages, head/flow curve, and estimates of BHP @ maximum specific gravity (1.8),

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4-7

efficiency, and NPSHR. Information shall include high- and low-end allowable operating regions

and any limitations of operation.

4.3.10 Load Test

Any pump lifting device provided shall be tested at one and a half times the weight of the pump

assembly. The maximum test load shall be stenciled on the lifting device on two sides in

minimum 2 inch letters. A test certification shall be provided.

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5-1

5.0 DOCUMENT SUBMITTAL

Required submittals are identified and listed on the procurement Master Submittal Register

(MSR). Table 5-1 provides a summary of these submittals. The MSR identifies the minimum

submittals required by this Specification and identifies when the submittals are required to be

submitted in the procurement process. The MSR included with the purchase order will constitute

the governing MSR.

Submittals shall be provided using the TOC Incoming Letter of Transmittal form provided by the

Procurement Specialist. All transmittal subject headings shall contain, at a minimum, the

subcontract number, submittal number, and submittal description.

Submittals shall be provided in electronic format unless available only as a hard copy.

Electronic submittals shall be sent in accordance with instructions provided by the Procurement

Specialist. Electronic formats must be non-password protected in one of the formats noted on

the Procurement Website located and the following web address:

http://www.hanford.gov/tocpmm/files.cfm/APPROVED_ELECTRONIC_RECORD_FOR

MATS.pdf

All deliverable documentation shall be complete, accurate, legible, and reproducible. Before

delivery, design media and documents shall be reviewed by qualified Subcontractor personnel

for technical adequacy and appropriate content in accordance with the Subcontractor’s Quality

Assurance procedures. The Subcontractor shall attest, in writing, to the accuracy and

completeness of the information contained in the final deliverables.

Deliverables shall be subject to approval by the BTR. Deliverables shall comply with this

Specification and technical basis documents and other requirements identified herein.

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5-2

Table 5-1. Summary of Submittals

Item Title Purpose When required

1 Schedule Pre Evaluation With Proposal

2 Proposal Data Pre Evaluation With Proposal

3 Quality Assurance Program Certification Approval With Proposal

4 Pump Design Report Approval Prior to Fabrication

5 Fabrication, Inspection, and Test Plan Approval Prior to Fabrication

6 Welder Performance Qualifications Approval Prior to Fabrication

7 WPSs, PQRs, SWPSs, and SWPS Demonstration Records Approval Prior to Fabrication

8 CWI and CAWI Certifications Approval Prior to Fabrication

9 NDE Personnel Certification Records Approval Prior to Fabrication

10 Test Procedures Approval Prior to Testing

11 Certified Test Data and Reports Approval Prior to Shipment

12 Inspections and Examination Results Approval Prior to Shipment

13 Radiography Film & Associated Reader Sheets. Approval Prior to Shipment

14 Certificate of Conformance and Suspect Counterfeit Items

Statement

Approval Prior to Shipment

15 Installation, Operation, and Maintenance Manuals Review/Information Prior to Shipment

16 Preservation, Packaging, Shipping, Storage and Lifting

Plan


17 Nonconformance reports, if applicable Approval Prior to Shipment

18 Final Pump Data Package with As-Builts and Spare Parts

List


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5-3

5.1 APPROVAL OF SUBMITTALS

All submittals transmitted shall include the designation in the Master Submittal Register (MSR)

per TOC Vendor Processes stated in TFC-BSM-IRM_DC-C-07. Submittals are divided into two

types: 1) those requiring “approval” (e.g., approval data or pre-purchase evaluation data); and 2)

those “not requiring approval” (e.g., vendor information data). Submittals “not requiring

approval” will be reviewed to verify completeness and adequacy for their intended purposes. A

submittal requiring approval that is not approved is identified as: 1) “Not Approved Revise and

Resubmit.” The submittal is considered technically deficient, or incomplete, and therefore

unacceptable. Resubmittal is required, hence the fabrication, procurement, or performance of

procedures shall not proceed; or 2) “Approved with Exception.” Fabrication, procurement, and

performance may proceed, and resubmittal is required to verify incorporation of the exception.

Submittals “not requiring approval” that are determined to be incomplete or inadequate will be

marked “Resubmit.” An explanation of the deficiencies will be included for corrective action by

the Seller.

Approval by the Buyer does not relieve the Seller of responsibility for accuracy or adequacy of

design under this Specification.

If any revision has been made to previously submitted items, the Seller shall resubmit updated

versions of said items for approval, in addition to the items listed above.

Certified data shall be defined to mean that the design adequacy of a given item (document,

drawing, calculation, etc.) be verified by persons other than those who prepared the item. Each

deliverable (drawing, calculation, etc.) shall have at least an originator's/preparer's signature and

a checked-by or approved-by signature.

5.2 LIST OF SUBMITTALS

This list of submittals along with relevant dates shall be kept as part of the MSR.

Identify each submittal by the purchase order number and Seller’s identification number.

1. Schedule.

a. Design/Fabrication Schedule: Submit a schedule showing design, fabrication,

assembly, testing and shipment of the equipment after receipt of the order.

2. Proposal Data

a. Work Plan: Submit a work plan showing design & fabrication approach.

3. Quality Assurance Program Certification

4. Pump Design Report. At a minimum, the following information shall be included in the

Pump Design Report:

a. Pump Performance Data: Information shall include impeller type and size,

predicted head/flow curve, and estimates of bhp @ maximum specific gravity,

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5-4

efficiency, and NPSHR. Information shall include high- and low-end allowable

operating regions and any limitations of operation.

b. 3-dimensional computer aided design solid body model of the pump.

c. General arrangement drawing(s): Detailed, dimensioned drawings, including bill

of materials, with Specification information.

d. Motor Driver Data, including certified driver outline and dimensional drawings.

e. Cross-Sectional/Outline Drawing(s)

f. Electrical and instrumentation wiring diagrams, elementaries, and instrumentation

data sheets.

g. Seismic Analysis (See Section 3.4.1).

h. Rotor Dynamic Analysis (See Section 3.4.2).

i. Critical Speed Analysis (See Section 3.4.3).

j. Lifting Analysis (See Section 6.3).

k. Transportation Calculations (See Section 3.4.4.3).

5. Fabrication, Inspection, and Test Plan which include Welds Maps.

6. Welder Performance Qualifications.

7. Certified Weld Inspector Certifications including current Eye Test.

8. Welding Procedure Specifications and Applicable Procedure Qualification Records.

9. NDE Personnel Certification Records including current Eye Test.

10. Test Procedures. The following information shall be submitted:

a. Megger Test (See Section 3.4.3).

b. Pump Motor Driver Testing (See Section 3.4.4).

c. Hydrostatic Testing (See Section 3.4.5).

d. Pre-Pump Run-in Performance Test (See Section 3.4.6),

e. Pump Run-in Test (See Section 3.4.7).

f. Pump Sealing System Leak Inspection (See Section 3.4.8).

g. Post-Pump Run-in Performance Test (See Section 3.4.9).

11. Certified Test Data and Reports. The test data and reports shall be submitted. Once

approved, the test results shall become part of the Final Pump Data Package:

a. Megger Test Results (See Section 3.4.3).

b. Pump Motor Driver Test Results (See Section 3.4.4).

c. Hydrostatic Test Results (See Section 3.4.5).

d. Pre-Pump Run-in Performance Test Results (See Section 3.4.6),

e. Pump Run-in Test Results (See Section 3.4.7).

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5-5

f. Pump Sealing System Leak Inspection Results (See Section 3.4.8).

g. Post-Pump Run-in Performance Test Results (See Section 3.4.9).

h. Certified Material Test Reports.

12. Inspection and Examination Results, including:

a. Weld Inspection and Examination Results (See Section 4.3.1). See submittal 13

for Radiography Film & Associated Reader Sheets.

b. M&TE Calibration Reports.

13. Radiography Film & Associated Reader Sheets. A copy of all RT film associated with

this procurement shall be sent to Buyer.

14. Certificate of Conformance and Suspect Counterfeit Items Statement

15. Installation, Operation, and Maintenance Manuals

16. Preservation, Packaging, Shipping, Storage and Lifting Plan.

17. Nonconformance Reports, if applicable.

18. Final Pump Data Package, including approved Items 3 through 17, shall include the

complete documentation and record of P-B-1 Pump. Final Pump Data Package shall

include:

a. Final detailed, dimensioned drawings, including bill of materials with

Specification information, with all redlines incorporated.

b. 3-dimensional computer aided design solid body model of the pump.

c. Completed FIT Plans.

d. Critical dimension verification.

e. NDE Records/Reports.

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6-1

6.0 PREPARATION FOR DELIVERY

6.1 PRESERVATION AND PACKAGING

a) All items shall be dried and cleaned to protect against rust and corrosion.

b) All items shall be protected from dirt, soil, and moisture and packaged for long-term

storage in a indoors/temperature controlled facility.

c) All items shall be packaged, as required, to eliminate damage during shipping, handling,

and storage. Temporary bracing, fixtures, or hardware installed to stabilize furnished

items during shipment or handling (excluding packaging materials) shall be tagged or

otherwise identified so that it can be removed before installation or operation of the item.

Electrical cable ends shall be sealed and secured to prevent moisture entry into cable.

6.2 MARKING

Prior to shipment, all packages shall be clearly and suitably tagged to identify, at a minimum:

! The Buyer’s name with destination address

! The Seller’s name with return address

! Package numbers showing the Purchase Order Number followed by the packagenumber

and the total number of packages

! Procurement Specification Number

! Package contents description

! Weight of package

! Center of gravity

! Parts list (for each package)

! Handling instructions (e.g., Fragile, Center of Gravity, Keep Dry, This Side Up, Sling

Here, Do Not Freeze) and stacking limitations, as appropriate

! Special Handling instructions.

6.3 SHIPPING AND HANDLING

a) The Seller shall submit to the Buyer for review and approval a Shipping and Handling

Plan that includes pump assembly preservation, packaging, shipping, storage, and lifting

procedures. Buyer approval of the plan is required before packaging and shipment. If a

special type of transportation to protect equipment is required, those devices shall be part

of the Seller’s package and identified as special equipment.

b) The entire pump shipping assembly shall be protected during shipping.

c) Other components being shipped shall be boxed or crated in a manner to prevent damage

during shipment and to permit handling by forklift or hoist while in storage or during

installation.

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6-2

d) The boxed or crated components shall be blocked and securely fastened to prevent

shifting, crushing, or bumping during handling.

e) All packages shall be suitably marked on the outside to facilitate identification on the

purchase order, the package contents, and any special handling instructions. Procedures

for marking for shipment shall be included in the Seller's packing plan.

f) The pump and seal water system shall be protected from freezing during shipment.

g) Material not shipped in a weatherproof vehicle shall be protected from weather by a

second sealed envelope or in a manner acceptable to the Buyer. Shipping procedures shall

define the method of protecting components from the weather.

h) Shipping dunnage, tie-downs, etc., shall be such that the system components cannot be

damaged or unduly stressed in any manner from carrier vibration or acceleration-

deceleration.

i) Buyer equipment provided to the Seller for use during testing shall be returned to the

Buyer with the pump shipment.

6.4 TRANSPORTATION

The Seller shall be responsible for delivery of the pump to the Hanford on-site storage

warehouse to be off-loaded. The Buyer shall be responsible for off-loading of the pumps

utilizing the stand designated lifting points provided by the Seller (See Section 3.4.4). The Seller

shall recommend the preferred transportation method and provide protection of the equipment

during transit. The Seller shall be responsible for all equipment damage ocurring as a result of

improper transportation. All components, unless specified otherwise in this section or related

sections, shall be compatible with being transported by public roadway to the contract specified

destination unless otherwise specified or allowed by equipment specific design documents. Items

shall either be self-supporting or provided with packing and dunnage to ensure their stability and

protection from damage.

The Seller shall provide instructions and diagrams for securing all shipping packages including

handling instructions be made available for the off-loading of the item. The pump assembly shall

be shipped in accordance with the applicable DOT standards and in an orientation ready for

lifting. Additional handling of the equipment to orientate it for lifting is not acceptable. Transport

and tie-down instructions and diagrams shall be provided. Lift points shall not be used for

transport tie-downs. Transport tie-down points shall be identified on the equipment. Calculations

to include requirements of 49 CFR 393, Subpart I, Protection Against Shifting and Falling

Cargo, shall be required for the design of all transport tie-down attachment points.

Offloading at The Buyer’s designated delivery site will be performed by the Buyer or a Buyer-

designated representative.

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7-1

7.0 NOTES

7.1 LIST OF ACRONYMS

AISC American Institute of Steel Construction

ANSI American National Standards Institute

API American Petroleum Institute

ASCE American Society of Civil Engineers

ASME American Society of Mechanical Engineers

ASNT American Society of for Nondestructive Testing

ASTM American Society for Testing and Materials

AWS American Welding Society

BTH below-the-hook

CAWI Certified Associate Welding Inspector

GFE government furnished equipment

CFR Code of Federal Regulations

CMTR Certified Material Test Reports

COR Code of Record

CWI Certified Weld Inspector

DOT Department of Transportation

FIT fabrication, inspection, and test plan

HI Hydraulic Institute

IEEE Institute of Electrical and Electronics Engineers

IOM Installation, Operation and Maintenance

ISO International Organization for Standardization

NCR nonconformance reports

NDE nondestructive examination

NEMA National Electrical Manufacturers Association

NIST National Institute of Standards and Technology

NPSH net positive suction head

M&TE measuring and test equipment

MCS monitor and control system

MSR master submittal report

QAP quality assurance plan

RT Radiographic examination

SWPS Standard Welder Procedure Specifications

TOC tank operations contractor

WPS Welding Procedure Specifications

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7-2

7.2 UNITS

“ inch

°F degrees Fahrenheit

cP centipoise

ft. foot or feet

g gravity

g/L or gm/L gram per liter

gpm gallon per minute

HP horsepower

Hz hertz

M molar

mol/l moles per liter

ppm parts per million

psia pounds per square inch absolute

psig pounds per square inch gauge

R/hr Rad/hour

rpm rotations per minute

V volts

Vol % volume percent

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8-1

8.0 APPENDICES

8.1 APPENDIX A – PUMP CURVE FOR FACILITY PUMP

2 3 3 4 5 3 6 7 4 8 9 : ; < 2 = > ? @ @ A A B : B 9 @ A C 4 : D ; A E F I ; G H I 8

RP

P-S

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2735, R

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8-2

Fig

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8-1

PU

MP

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P-B

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8-3

8.2 APPENDIX B – MOTOR DATA SHEET

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8-4

-

Figure 8-2. Motor Data Sheet

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