Worksheet in Test nozzle - Design.xls

8/10/2019 Worksheet in Test nozzle - Design.xls

1/177

Purpose

Step 1

Select from the dropdown menu the appropriate tool. These tools are based on currently

available sizes, although custom sizes can be produced as needed. The program uses theO.D., I.D. and number of holes in the selected tool for velocity and jet calculations.

Step 2Select from the dropdown menu the O.D. of the casing the HydraJet tool will be cutting

through.

Step 3Select from the dropdown menu the casing grade. The program uses this in the calculations

for jetting through different types of steel.

Step 4Select from the dropdown menu the casing weight. The program uses this to determine the

I.D. of the pipe for the jetting time calculations.

Step 5Enter the desired depth you wish to penetrate past the O.D. of the casing. If unsure of what

number to use, click the "Reset to Default Values" button to enter the default value.

Step 6

From the dropdown menu, select the nozzle size you wish to use. Remember that not all of

the sizes available in the menu are available. Only 1/8", 3/16", and 1/4" nozzles are currently

used.

Step 7

Enter the desired number of nozzles you with to use in the tool. If you choose too many a

warning message will indicate you need to lower the number. It may take several iterations

between nozzle size, number, and pumping rate to get the desired differential pressure for

jetting.

Step 8Enter the discharge coefficient value of your choice. The default value is 0.9 and is based on a

new set of the newly redesigned jet inserts.

Step 9

Enter the flow rate in the tubing. A good beginning guess is 1 BPM / nozzle. Remember,

2,000 - 3,000 psi is good for jetting on a CobraMax job, but around 5,000 psi is needed for a

SurgiFrac procedure.

Step 10Enter the base fluid density of the jetting fluid. The program uses this in the differential

pressure and jetting time calculations.

Step 11 Enter a sand concentration. The default (and most widely used) concentration is 1 lb/gal.

Step 12

From the dropdown menu, select the proppant being used for jetting. Most of the proppants

available in the Materials Library have been entered into this spreadsheet along with the data

for each proppant needed to calculate jet solid velocities, jetting times, fluid densities, etc.

This data has been hidden to protect this data from general release. Sorry, but I had to

promise. If your proppant is not available in the list, choose the next closest proppant in terms

of size, mesh, and density. The calculations should still be close.

Instructions for the Pinpoint Stimulation Design

Spreadsheet

The purpose of the HydraJet Calculations sheet in this workbook is to calculate the jetting time

needed to cut a specified distance into the formation before breakdown. These calculations

include a correlation based on work done by Pekarek, Lowe and Huitt and presented in a paper in

1963 (SPE #421). The correlation relates the velocity of both the fluid and the particles in the

abrasive jet to the impingement velocity and subsequent erosion of the pipe wall and formation

rock. All input cells are highlighted in blue. All results cells are highlighted yellow. The final

results of this sheet are intended to help design the jetting stage size for a CobraMax or SurgiFrac

treatment.

HydraJet Calculations RETURN


2/177

Results

Purpose

Step 1

Enter the Coiled Tubing O.D. If the treatment is being performed down jointed pipe, the O.D.

of this pipe may be entered, but the results do not include velocities around joints.

Step 2 Enter the Coiled Tubing wall thickness. Wall thickness of jointed pipe can also be entered.

Step 3

Enter the I.D. of the Coiled Tubing swivel. This is the inlet port on the Coiled Tubing unit that

allows the unit to move pipe in and out of the well while pumping. If Coiled Tubing is being

used, it is important to know the swivel I.D. Most units have a 2 inch swivel that is normally too

small for fracturing rates. A 3 inch swivel is recommended for SurgiFrac operations.

Step 4

Enter the Coiled Tubing Jetting depth. This is from the reference point on the well at surface

to its run-in depth where the volume calculations are performed. Also note that this depth can

be different than the Perforation Depth so that coil movement is taken into account.

Step 5

Enter the Total Coiled Tubing on Reel. This length is BEFORE running in hole. It is an

important number not only for volumes, but for the friction calculation as well.

Step 6

Enter the Flow Rate Down the Annulus. This is mainly for velocity concerns on a CobraMax

treatment, but is also useful on SurgiFrac and certainly SurgiFrac AP treatments.

Step 7

Enter the I.D. of the Flow Cross Inlets. This is the MINIMUM I.D. of the inlets to the wellhead

configuration on the annular side. This value must be known for accurate calculations.

Step 8

Enter the Number of Inlets. This splits up the velocity equally between inlets in the velocity

calculations.

Step 9

Enter the BOP I.D. This is the MINIMUM I.D. for any wellhead configuration that "sees" fluid

flow.

Step 10 Enter the Depth to the Top of Current Perforations. This is for a total well annular volume.Results

The Results of this sheet include:

Velocities around and through the tubing.*

Velocities through the Coiled Tubing Swivel.*

Velocities around and through the HydraJet Tool assembly.*

Impingement velocity on the Coiled Tubing through the Flow Cross.*

* - Each of the velocity cells will highlight if the recommended limit is exceeded.

Area calculations based on entered data for reference.

Veloci ty Calculations

The purpose of the Velocity Calculations sheet in this workbook is to ensure that the job can be performed

safely and with a minimum of erosion on the treating lines or tubulars. Volumes and areas are also

calculated. All input cells are highlighted blue. All results cells are highlighted yellow. The velocities

calculated and limits are based on current best practices and cannot be changed. If a velocity exceeds its

recommended limit, the cell for velocity will highlight to indicate this. As you progress through the sheets

note that more and more of the data used in a sheet relies on data entered on previous sheets. If, for

instance, the tubing rate needs to be changed on the Velocity Calculations sheet, then you must go back

to the HydraJet Calculations sheet to do so.

The most important things to look at from this sheet are the differential pressure being generated, the

recommended jetting time and the volumes needed. Again, it may take several iterations to achieve the

desired affect. There is also an indicator that lets you know when bridging is likely to occur across the

jets.

RETURN


3/177

Volume Calculations based on entered data for reference.

Purpose

Purpose

Step 1

Enter the Plug Back Total Depth or the Depth of the last Sand Plug. All sand volume

calculations work from this reference depth.

Step 2

Enter the Desired Top of Sand. This is used to calculate the volume required to fill, unless the

override proppant volume is used, in which case this cell blacks out.

Step 3

Enter the Average Proppant Concentration in Well. Typically, you will wish to use the proppant

concentration of the last sand stage in the design. The proppant used in the calculations is the

one selected on the HydraJet Calculations sheet. If you desire to change this you must go

back to the HydraJet Calculations sheet and re-select a proppant type/size.

Step 4 Enter the Current coil depth. This has been added for flexibility and quick calcs.

* If desired, you may enter a rate, pressure response and estimated viscosity of fluid moving

through the proppant plug to estimate it's height. This height is calculated based on the

assumption that the top of the last set of perforations is taking the fluid. You must have a

known treating pressure of this formation and have confidence that you are not displacing the

sand plug into the formation. The GC sand height us using a Gulf Coast correlation while

Darcy is using Darcy's law of flow through a porous media.

** If desired, you may override the calculations by entering a weight of sand in the blue cell

next to the calculated value. This overrides all calculations and gives new estimates for the

height and volume of the plug. The cell below the blue entry cell is the new estimated top of

sand.

Results

Proppant Required for Plug in pounds and also in cubic feet.

The clean volume required to pump the calculated proppant at the desired concentration.

The dirty volume of the sand plug stage.

The height of the sand at ISIP. This is used to indicate that sometimes the tool is still below

sand after shut down. While this usually does not cause a problem, bridging and sticking

could occur. The graphic helps to indicate the possibility. Light brown sand is still in slurry and

before settling. Dark brown is settled sand.

Depth of the last sand stage at ISIP.

Sand Plug Calculations

The purpose of the Sand Plug Calculations sheet is to help determine the size of the last sand stage that

needs to stay in the wellbore in order to set the sand plug required for the next zone's treatment. This

sheet's graphic also indicates when the final proppant stage is above the tool after a shut down and whenthe tool is likely to become stuck during the sand plug setting stage.

Min. Nozzle Dia.

Erosion Graphs

The purpose of the Erosion Graphs sheet is to give a visual demonstration of the jet impingement

calculation and a comparison of the results to empirical data from the Halliburton HydraJet manual. The

Fluid and Proppant Veloci t ies from Centergraph represents the results of the correlation used to

calculate the velocities of both the fluid and aggregate as it moves through the jet, annulus and wellbore

wall. These velocities are then used to calculate the erosion speed and jetting times. The three graphs

below represent the jetting erosion speed calculated from the correlation and are overlaying graphs from

the HydraJetting Manual. Depending on the casing size and differential pressure, the graph closest to the

simulated conditions should closely match with the calculation.

RETURN

RETURN

RETURN


4/177

Purpose

bridging of aggregate on the nozzles. The data is gathered from an article by John E. Smith in

World Oil, June 1991. A certain minimum size orifice is recommended based on both

Purpose

The purpose of the BHA's sheet in this workbook is for a quick reference of part numbers forall tools and tool elements associated with Pinpoint Stimulation.

Purpose

In SurgiFrac operations, the contribution of the annulus rate not assumed to be controlling

leakoff must be taken into account for calculating the proppant concentration actually going

into the formation. This sheet gives a straight calculation based on input estimations for

leakoff rate and annulus and tubing rates based on inputs from other pages.

Step 1

Enter an estimated leakoff rate in the annulus. This number is very hard to estimate and can

only truly be found with a pre-stage injection/step-up test.

Step 2 Enter the proppant concentration you wish to see the dilution calculations for.

Results

Some of the results from the proppant side are:

Clean rate at the blender

Slurry density at the blender

Sand rate at the blender

Proppant concentration in the fracture (after dilution)

Slurry density in the fracture (after dilution)

Purpose

In SurgiFrac operations, the contribution of the annulus rate not assumed to be controlling

leakoff must be taken into account for calculating the concentrations of dilute additives such as

acids and salts actually going into the formation. This sheet is intended to give great flexibility

in salt and acid concentrations both in the annular fluid and tubing fluid. It is based on input

estimations for leakoff rate and annulus and tubing rates based on inputs from other pages.

Step 1

Enter a rough estimation of the bottom hole treating temperature for base fluid density

calculations.

Step 2 Enter the material concentrations for both the annular and tubing fluid.

Results

The results of these density calculations are based on correlations created by Marten Bruijse

for use in the mix.xls spreadsheet to calculate the fluid density for brines and acids. This

spreadsheet goes a step further and does mixing calculations downhole for a Pinpointstimulation treatment. The final fluid concentrations are based on % by weight of solution for

the acids and % by weight of water for the brines. The final concentrations are accurate to

less than .1% and the final density is accurate to less than .01 ppg according to Marten Bruijse

for the following limits:

The assumption is that the HF acid concentration is made using ABF.

The acetic acid concentration is valid for concentrations < 40%

The formic acid concentration is valid for concentrations < 40%

There is no density data for glycolic acid. Therefore, acetic acid properties were assumed.

SurgiF rac Acid Di lu tion

SurgiF rac Proppant Di lution

BHA'sRETURN

RETURN

RETURN


5/177

NH4Cl has a maximum concentration of 24%

NaCl has a maximum concentration of 26%

NaBr has a maximum concentration of 40%

KCl has a maximum concentration of 24%

CaCl2 has a maximum concentration of 40%

AlCl3 has a maximum concentration of 55%

These calculations will also be used in the hydrostatic calculation for treating pressure.

Purpose

The purpose of the Flowback sheet in this workbook is to determine the flowrate of either gas

or fluid through various sizes of chokes and at pressures ranging from 100-10,000 psi.

Step 1 Enter a gas gravity. A beginning estimated range should be between 0.65 - 0.7.

*You may enter a new discharge coefficient and specific heat ratio if they are known.

Step 2 Scroll down to enter a flowback fluid density for the water flowback table.

Results

The results of pressure vs. flowback rate can be seen by scrolling through the tables or down

to the graphs.

Purpose

The purpose of the Design Schedule sheet is to lay out a beginning summary of the job

schedule, by stages for pricing. This sheet incorporates my best efforts at calculating tubing

and annulus treating pressures as well as volumes and proppant weights. A user has the

ability to enter up to 100 stages. A "free" sheet has also been added so that the user can build

a tailored report to fit any need. A job plot has also been added to help visualize the treatment

schedule and give an indication of time. PLEASE NOTE: The friction calculations currently

only work when the sheet is set to "English" units.

Step 1

Enter the base fluid and acid densities for hydrostatic calculations. These densities are

independent for flexibility of the spreadsheet. If the fluid chosen is "fresh water", the density is8.337 lb/gal by default.

Step 2Enter the Tubing schedule. All proppant types per stage can be filled in from the 1st stage as

a reference by hitting the "Fill Down" button.

Step 3

Enter the Annulus schedule. All proppant types per stage can be filled in from the 1st stage as

a reference by hitting the "Fill Down" button. Please note that the volumes for tubing and

annulus are not linked and must be matched using the calculation buttons.

Step 4

Click the appropriate button to calculate the tubing volumes to match the annulus dirty stage

volumes (CobraMax) or to calculate the annulus volumes to match the tubing dirty volumes

(SurgiFrac).

Results

The results from the schedule currently include:

Tubing dirty stage volume.

Tubing Stage Proppant Weight. Tubing Cumulative Proppant Weight.

Maximum Tubing Pressure per Stage. Tubing pressure is dependent on a "best guess" at the

current hydrostatic pressure in the wellbore, the nozzle pressure drop, a "best guess" at tubing

friction, and an entered BHTP gradient. These guesses are made based on tubing and casing

sizes entered on the HydraJet Calculations sheet. Note that this pressure is ONLY a best

guess and should be confirmed using stimulation design software.

Design Schedule

Flowback RETURN

RETURN


6/177

Maximum Nozzle Pressure Drop per Stage. This is the same calculation used on the HydraJet

Calculations sheet, but with the current rate base fluid density and proppant type and

concentration.

Annulus Dirty Stage Volume.

Annulus Stage Proppant Weight.

Annulus Cumulative Proppant Weight.

Maximum Annulus Pressure per Stage. This is base on a "best guess" at annulus friction and

hydrostatic pressure to the top perforation specified in the Velocity Calculations sheet.

Stage Time. Stage time is dependent on the tubing or annulus, whichever has the highest

rate.


7/177


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12/177

HydraJet Calculations

FALSE

HydraJet Tool 3.4 Jet Nozzle Size (in)Casing Size (in) 4.500 Number of Nozzles 8

Casing Grade 2.500 Cd 0.85

Casing Weight (lb/ft) 15.1 Total Tubing Flow Rate (BPM) 8.0 0.187

Desired Penetration Depth into Formation (in) 4 Base Fluid Density (lb/gal) 8.34 2213.458

Prop Concentration (lb/gal) 1.0

Specific Volume of Sand 0.042467948

Internal Diameter of Casing 3.825 in

Drift Diameter 3.700 in

Pipe Wall 0.338 in

Standoff Assume Centralized 0.213 in

Calculated Time to Notch Formation 5.4 min

Flow Rate Total336 gal/min 2,394 lb

Flow Rate Each Nozzle 42.0 gal/min

Density of Fluid with Sand 8.96 lb/gal

Sand Rate 322 lb/min 2394 gal

Flow Rate Base Fluid 322 gal/min 57.00 bbl

Pressure Drop through each Nozzle 2,381 psi 2496 gal

Nozzle Exit Velocity 488.0 ft/s 59.42 bbl

Clean Fluid Volume for Jetting.

Total Jetting Fluid Dirty Volume

RESULTS

min

min

sacks

Recommended Jetting Time of a 1 ppg

Stage to Cut Single Perforations (min)7.4

100 Mesh needed based on the

calculated jet time.20.68

Required Data

Jetting Time to Penetrate Steel (min) 2.1


13/177

Velocity Calculations

8.00 BPM 25.000 BPM

336.0 gpm 2.3394 ft3/s

0.7486 ft3/s 1050.0 gpm

Tool OD 3.400 in ID of flow Cross Inlets 4.160 in

Tool ID 1.2 in Number of Inlets (Dual=2, Quad=4, etc) 2Casing ID 3.825 in BOP I.D. 5.500 inTubing OD 1.750 in Minimum I.D. - Casing Restriction 5.500 in

Tubing Wall thickness 0.175 in Depth to Top of Current Perforations 12000.0 ft

I.D. of Coiled Tubing Swivel 3.00 in

Tubing Jetting Depth 12000.0 ft

Total Coiled Tubing on Reel 15000 ft

Velocity

(ft/s)

Max

Velocity

(ft/s)

Max Rate

(BPM)

Velocity

(ft/s)

Max

Velocity

(ft/s)

Velocity Through Coil ID 70.03 35.0 4.00 Velocity Impinging on the Coil 12.39 20.0

Velocity through Swivel 15.25 35.0 18.36 Velocity through BOP Annulus 15.78 20.0Velocity in ID of Tool 95.32 80.0 6.71 Velocity in Annulus of Casing and CT 37.08 35.0

4.00 Velocity through Restriction by OD of CT 15.78 35.0

Velocity in Annulus by Tools 139.69 60.0

Area through Coiled Tubing ID 1.539 in2 Area through Inlets 27.184 in2

Area through Swivel ID 7.069 in2 Area of Annulus through BOP 21.353 in2

Area through ID of Tool 1.131 in2 Annulus Area between Casing and Coiled Tubing 9.086 in2

Annulus Area between Casing and BHA 2.412 in2

Area of Casing I.D. 11.491 in2

Area of Casing Restriction 21.353 in2

28.56 bbl 134.85 bbl

1199 gal 5663 gal

22.85 bbl 0.01124 bbl/ft

960 gal 11.2371 bbl/1000ft

0.00190 bbl/ft 134.85 bbl

1.9039 bbl/1000ft 5663 gal

35.70 bbl 0.01421 bbl/ft

1499 gal 14.2120 bbl/1000ft

0.00297 bbl/ft

2.9749 bbl/1000ft

Flow Rate Down the AnnulusFlow Rate Down Tubing

Tubing Calculations Annulus Calculations

Dimensions

Areas

Velocities

Volumes

Volume of Annulus between Casing and Coiled

Tubing to Tubing Reference Depth

Volume of Annulus + Casing to Top of Current

Perforation Depth

Maximum Rate Through Coiled Tubing

Maximum Treatment Rate Based on Velocity

Volume of Coiled Tubing ID

from surface to Reference

Depth

Volume of Coiled Tubing OD

to Reference Depth

Total Coiled Tubing Volume


14/177

Figure 1 is a velocity profile of both the base fluid and proppant, demonstrating how they ac

8

9

10

(in)

0

100

200

300

400

500

600

0 1 2

Veloc

ity(ft/s)

Distanc

Fluid and Proppant VeloHELP


15/177

Figure 2 is an overlay comparing the theoretically derived penetration rate to emperical data

This example is for 1.5 ppg sand in jelled water at 2,000 psi pressure drop through 1/4 in no

3

4

5

6

7

0 2 4 6 8 10 12 14 16 18

Penetratio

nDept

Time

5

6

7

8

9

10

enetration

Depth(in)


16/177


This example is for 1ppg sand in jelled water at 1,000 psi pressure drop through 3/16 in noz


3

4

0 10 20 30 4Time (

2

3

4

5

6

7

8

9

10

0 10

Penetration

Depth(in)

Time (min)


17/177

This example is for 1.5 ppg sand in jelled water at 3,000 psi pressure drop through 3/16 in n


18/177

elerate throught the nozzle and slow at different rates.

3 4 5

from Center (in)

cities from Center

VL VP


19/177

from the Halliburton HydraJet Manual.

zzles.

0 22 24 26 28 30 32 34 36 38 40(min)


20/177


zles.


50 60 70 80min)

20 30 40


21/177

ozzles.


22/177

Sand Plug Calculations

PBTD or Depth of Last Plug 12680 ft Proppant Type

Desired Top of Sand Plug 11800 ft Absolute Volume 0.04247 gal/lbAverage Proppant Concentration in Well 8.00 lb/gal Bulk Density 115.8 lb/gal

CURRENT Coil Tubing Depth 11000.00 ft

Tubing Size 1.750 in Top Perforation Depth 12000 ft

Tbg Vol Factor 0.01069 ft3/ft End of Tbg ( EOT ) 11000 ft

Casing Size 4.5 in 70.22 ft3

Casing Volume Factor 0.07979 ft3/ft 8128 lb 0 9381

Annulus Volume Factor 0.06309 ft3/ft 1016 gal 11800 9381

24.2 bbl 9381

Pump Rate through Sand Plug at

Pressure 3.1449 BPM1361 gal

11000

P - Estimated Differential Pressure

Across Sand Plug 218 psi32.4 bbl

11000

Estimated Fluid Viscosity in Sand Plug 2 cp Height of Sand at ISIP 2619 ft 11000

GC Estimated Sand Height Above

Perforations 0.0 ft

Depth of Last Sand

Stage/Flush at ISIP9381 ft

12000

Darcies Equation Height Estimate 0.1 ft Volume of Flush 4427 gal

Required Data Proppant Data

Plug M aterial Requirements

Clean Plug Volume

100 Mesh

Estimated Particl e Settling Based On SPE 26121

Dirty Plug Volume

Estimated Sand Height Above Perforations

Proppant Required for

Plug


23/177

BHA's Halliburton Confidential

Description

Tool Part No. 100071122 101310839 101312314 100071144 101317095 101215821 101327409 10130206

OD (in.) 2.594 3.2 2.88 2.75 3.2 3.09 3.09 3.2

ID (in.) 1.5 1.5 1.38 1.75 1.75 1.99 1.38 1.75

Makeup Length (in.) 13.32 8.91 9.53 13.85 9.77 14.24 11.23 10.39

Bottom Connection2 3/8-in. EUE, 8-rd

Tubing Pin2 3/8 -in. IF Pin 2 3/8-in. PAC Pin

2 3/8 -in. EUE, 8-rd

Tubing Pin

2 3/8 -in. IF

Pin

23/8 -in.EUE, 8-rd

Tubing Pin

23/8 -in.

PAC Pin

23/8 -in.

Pin

Service Rating H2S Std. H2S H2S Std. H2S H2S Std.

Tensile Rating (lb) 52,000 63,000 63,000 55,000 70,000 81,000 81,600 134,000

Pressure Rating (psi) 10,000 17,000 12,900 7,500 17,000 8,200 8,200 15,000

Torque Rating (lb/ft) 1,270 1,270 1,270 1,800 1,800 1,800 2,380 2,600

Nut 698.24592 698.24592 698.24592 698.24603 698.24603 698.24645 698.24645 1013020

Center Sub 698.24582 698.24582 698.24582 698.24632 698.24632 698.24644 698.24644 1013020

Bottom Sub 698.24583 101310837 101311984 698.24633 101317141 101215765 101327412 1013020

Lock Ring 698.24593 698.24593 698.24593 698.24504 698.24504 698.24643 698.24643 1000711

O-ring 600.34021 600.34021 600.34021 600.34023 600.34023 600.33974 600.33974 600.3397

Backup Ring 698.24594 698.24594 698.24594 698.20053 698.20053 N/A N/A N/A

Nut Thread 23/16-in.-14UN 23/16-in.-14UN 23/16-in.-14UN 21/2-in.-12UN21/2-in.-

12UN

213/16-in.-

10-stub

ACME

213/16-in.-

10-stub

ACME

2 7/8-in.-

stub ACM

Nut OD 2.44 2.44 2.44 2.75 2.75 3.09 3.09 3.2

Redress Kit Part No.a 698.24581 698.24581 698.24581 698.24631 698.24631 698.24641 698.24641 698.2464

SAP No. 101308640 101298 95367

OD (in.) 3.2 2.94 3.63

ID (in.) 1.75 1.96 2.441

Make-Up Length (in.) 9.37 12.49 12.35

Top Connection 2 3/8 -in. API IF box

2 3/8 -in. EUE

8 rd box

2 7/8 -in. EUE 8

rd box

Bottom Connection 2 3/8 -in. API IF pin2 3/8 -in. EUE

8 rd in

2 7/8 -in. EUE 8

rd in

Shear Screw Part No. 100005755 100005755 100005755

Max. No. of Screws 10 8 8

O-Ring Part No. 100001988 100006583 100006587

Fishin Profile 3 1/2 GS internal Overshot onl Overshot onl

Part No. Casing Size (in.) Max. OD (in.) ID (in.) Make-Up Length (in.)Thread

Connections

101301835 4.5 3.85 1.75 8.132 3/8 - in.

API IF

101309111 4.5 3.85 1.75 24.132 3/8 - in.

API IF

97680 4.5 3.942 1.937 8.35 2 3/8 - in.EUE 8rd

129850 4.5 3.852 1.937 8.352 3/8 -in.

EUE 8rd

101308525 5.5 4.75 1.75 8.132 3/8 - in.

API IF

101310885 5.5 4.75 1.75 24.132 3/8 - in.

API IF

99415 5.5 4.862 2.375 10.612 7/8 - in.

EUE 8rd

Double Sl ip Connector

aRedress kits include O-rings, backup rings, and lock rings.

bThis connector has a 5 internal taper in the top of the nut.

Shear Di sconnect

Centralizer

2 3/8-in. CT OD2-in. CT OD1 3/4-in. CT OD

HELP


24/177


97679 5.5 4.742 2.375 10.612 7/8 - in.

EUE 8rd

90370 7 6.216 2.75 11.613 1/2 - in.

EUE 8 rd

Part No. OD (in.) ID (in.)

Make-Up

Length (in.) Tensile Rating (lb)

Articulation

Angle

Pressure

Rating (psi)

Thread

Connections

101304461 3.20 1.75 11.56 110,000 5 15,0002 3/8 - in.

API IF

Part No. OD (in.) ID (in.)Make-up

Length (in.)Thread Connections

101306763 3.20 1.75 12.0 2 3/8- in. API IF

101301748 3.20 1.75 24.0 2 3/8 - in. API IF

101306626 3.20 1.75 48.0 2 3/8 - in. API IF

99756 2.94 1.92 39.3 2 3/8- in. EUE 8rd

95434 3.63 2.44 39.3 2 7/8 - in. EUE 8rd

Part No. OD (in.) ID (in.) Make-UpLength

Thread Connections

(in.)

101301434 3.20 1.88 12.002 3/8 - 2 3/8- in. API

IF box in. NU 10rd box

101303833 3.20 1.88 12.002 3/8- 2 7/8 - in. API

IF box in. NU 10rd box

125812 3.063 1.966 18.12

2 3/8-in. EUE 8rd box

2 3/8 -in. NU 10rd

box

125813 3.705 2.350 18.25

2 7/8-in. EUE 8rd box

2 7/8 -in. NU 10rd

box

Part No. Casing Size (in.)Mandrel OD

(in.)Mandrel ID (in.) Make-Up Length (in.)

Thread

Connections

101309169a,b,c 4.5 3.50 1.285 16.062 3/8 - in.

API IF

101309199a,c,d 5.5 4.40 1.75 16.062 3/8 - in.

API IF

95382e 4.5 3.668 1.937 18.02 3/8-in. EUE

8rd

95344 5.5 4.625 2.38 18.02 7/8-in. EUE

8rd

aPacker rings are sold

separately. See Table

11.8.B.

bO-ring is sold

separately. Order SAP

No. 100001960.

cCups are sold

separately. See

Table 11.8.C.

dO-ring is sold

separately. Order

SAP No.

100001961.

eOptional 90 durometer

cup for this packer is

Part No. 186958.

Casing Size (in.) Casing Weight (lb/ft) OD (in.) Packer Ring

50 Duro 70 Duro 80 Duro 90 Duro

9.5 to 10.5 3.71 N/A (696.50034)100070000

(696.50022)

100012497

(696.50018)

11.6 to 13.5 3.54 N/A (696.51034)100009397

(696.51022)

100004002

(696.51018)

13 to 14

Knuckle Joint

Blast Joint

Ported Sub

Top Cup Packer

Packer ri ng selection

4 1/2


25/177


15.5

17

20 to 23 4.4 100070094

(696.53725)

100012531

(696.53723)

Casing Size Casing Weight Cup

(in.) (lb/ft) 70 Duro 85 Duro

9.5 to 10.5 100009387(694.94011)

100009390(694.94064)

11.6 to 13.5100003936

(694.94012)

100009388

(694.94013)

13 to 14100009389

(694.94019)N/A (694.94065)

15.5100003939

(694.94023)

100003938

(694.94022)

17

20 to 23

Part No. Casing Size (in.)Weight Range

(lb/ft)Max. OD (in.) Make-Up Length (in.)

aPacker

Elementb

101207099 4.5 9.5 to 11.6 3.75 46.97

101251733c 5.5 13 to 23 4.67 46.24

aMake-up length does

not include the ported

sub length.

bPacker rings must be

ordered separately. See

Table 11.9.B.

Packer Ring

(1 req.)

50 Duro

4 1/2 9.5 to 11.6 3.75100005025

(838.95217)

100077733

(838.95222)

100005026

(838.95226)

100005024

(838.95211)

100014066

(838.95216

)

5 1/2 13 to 23 4.42

100014058

(838.93531)

100014057

(838.93511)

100077696

(838.93516)

10125158

(838.93514

Part No. OD (in.) Min. ID (in.)Make-Up Length

(in.)Number of Holes Phasing

Thread

ConnectionsMin. OH

ID

Min. Line

ID

101252146 3.06 1 14.25 10 Helical2 3/8 -in.

EUE 8rd 3.3 3.6

101252136 3.06 1 17.25 9 1202 3/8 -in.

EUE 8rd

101252143 3.06 1.1 22.25 10 1802 3/8 -in.

EUE 8rd

101330284 3.4 1.2 14.25 10 Helical2 3/8 -in.

EUE 8rd 3.75 3.9

101330285 3.4 1.2 13.13 10 Helical 2 3/8 - in.API IF

101252127 3.66 1.5 14.25 16 902 7/8 - in.

EUE 8rd 4 4.25

101323841 3.66 1.5 13.13 16 902 3/8- in. API

IF

101252133 3.66 1.5 20.25 15 1202 7/8 - in.

EUE 8rd

100012394

(694.94025)

cFor work inside 17- to 23-lb/ft

casing, order shoe SAP No.

100014056 and wedge SAP No.

Casing Size (in.) Casing Weight (lb/ft) OD (in.)

(695.08195)5 1/2

85 Duro 95 Duro

4.6 (695.08201)

Packer r ing selection

75 Duro

(695.08199)

60 Duro

SurgiF rac Jet Bodies

65 Duro

Cup Selection

RR4-EV Packer Specif ications

4 1/2

5 1/2


26/177


101252130 3.66 1.5 28.25 16 1802 7/8 - in.

EUE 8rd

101323995 4.5 2.25 16.63 25 722 7/8 - in.

API IF

101247141 4.5 2.25 18 25 723 1/2- in.

EUE 8rd 5.3 5.5

101252120 4.5 2.25 28 21 1203 1/2- in.

EUE 8rd

101252123 4.5 2.25 33 20 180 3 1/2- in.EUE 8rd

101300991 7.5 3.75 27.63 21 Helical4 1/2 - in.

API IF

Part No. Nozzle Size (in.) Thread * Assumes Centraliz

101247257 3/16 ** More than 20,000

101268612 1/4 *** Less than 20,000

101268616 Blank (no hole) **** Larger sizes can

Part No. OD (in.) Min. ID (in.) Ball Size (in.) Make-Up Length (in.)Thread

Connections

101247256a 3.06 1.19 1.375 10.25

2 3/8 - in.

EUE 8rd

101251668b 3.66 0.94 1.375 10.25

2 7/8 - in.

EUE 8rd

101251672c 4.5 1.5 2.125 10

3 1/2 - in.

EUE 8rd

101331279d 3.2 1.06 1.375 13.48

2 3/8 - in.

API IF

aBall cage (SAP No.

101247249) and ball

(SAP No. 101313175)

must be ordered

separately.

bBall cage (SAP No.

101247250) and ball

(SAP No. 101313175)

must be ordered

separately.

cBall cage (SAP

No.

101251973) and

ball (SAP No.

101313167)

must be ordered

separately.

dTool comes

complete with the

ball cage and ball.

101252004

101252003

101252005

101251998

101313175

101313167

1012472493.06 in OD sizes for 4.0

to 4.5 in Casing

1012472503.66 in OD sizes for 4.5

to 5.5 in Casing101251973

4.50 in OD size for 6.0

to 7.625 in Casing

Ball Checks

1.00-12UNF

male

HydraJetting Nozzles

2.175 Ceramic Ball

Ball Cages

The jet configuratio

erosion of the tool b

1.00" OD Steel Ball

1.375" OD Steel Ball

2.25" OD Steel Ball

1.375 Ceramic Ball

0.80" OD Steel Ball

Bal l Sub Specif ications


27/177

Leakoff rate in Annulus 2.0000 BPM

Proppant Concentration 8.00 lb/gal

Tubing Rate 8.000 BPM

Rate on Annulus 25.000 BPMBase Fluid Density 8.34 lb/gal

Absolute Volume Factor of Proppant 0.04247 gal/lb

Proppant

Conc's. Vs.

Ann Rates

1.00 2.00 3.00

Slurry Factor 1.00Negative Annulus

Rate!1.00 0.88

Clean Rate at the Blender 5.9713 BPM 2.00Negative Annulus

Rate!2.00 1.76

Sand Rate at the Blender 2.0287 BPM 3.00Negative Annulus

Rate!3.00 2.63

Density of the Slurry at the Blender 12.20 lb/gal 4.00Negative Annulus

Rate!4.00 3.49

5.00Negative Annulus

Rate!5.00 4.34

Annulus Fluid commingling in

fracutre23.0000 BPM 6.00

Negative Annulus

Rate!6.00 5.19

Slurry Rate in Fracture 31.0000 BPM 7.00Negative Annulus

Rate!7.00 6.02

8.00Negative Annulus

Rate!8.00 6.85

Slurry Factor in the Fracture 9.00Negative Annulus

Rate!9.00 7.67

Proppant Concentration in the

Fracture1.65 lb/gal 10.00

Negative Annulus

Rate!10.00 8.49

ProppantConcen

tration(lb/gal)

SurgiF rac Proppant Di luti on

1.3397

1.0700

0.00

2.00

4.00

6.00

8.00

10.00

12.00

1 2 3 4 5 6 7 8

AnnulusRate

Proppant Concentration

HELP


28/177

Density of Slurry in Fracture 9.34 lb/gal


29/177

4.00 5.00 6.00 7.00 8.00 9.00 10.00

0.79 0.72 0.66 0.61 0.56 0.52 0.49

1.57 1.42 1.30 1.19 1.10 1.03 0.96

2.34 2.11 1.92 1.76 1.63 1.51 1.41

3.09 2.78 2.52 2.31 2.13 1.98 1.84

3.84 3.44 3.11 2.84 2.62 2.43 2.26

4.57 4.08 3.69 3.36 3.09 2.86 2.66

5.29 4.71 4.25 3.87 3.55 3.28 3.05

5.99 5.32 4.79 4.35 3.99 3.68 3.42

6.69 5.93 5.32 4.83 4.42 4.07 3.78

7.37 6.52 5.84 5.29 4.83 4.45 4.12

Annulus Rate (BPM)

9 10


30/177

60 F 8.3314 lb/gal Tubing Rate 0.500 BPM

15.6 C 0.9990 S.G.

35.000 BPM

Leakoff Rate 2.000 BPM

Material % Material % Material

HCl 0.0 HCl 0.0 HCl 0.00

HF 0.0 HF 0.0 HF 0.00

Acetic 0.0 By Weight Acetic 0.0 By Weight Acetic 0.00 By Weight

Formic 0.0 Of Solution Formic 0.0 Of Solution Formic 0.00 Of Solution

Glycolic 0.0 Glycolic 0.0 Glycolic 0.00

Citric 0.0 Citric 0.0 Citric 0.00

NH4Cl 0.0 NH4Cl 0.0 NH4Cl 0.00

NaCl 0.0 NaCl 0.0 NaCl 0.00

NaBr 0.0 By Weight NaBr 0.0 By Weight NaBr 0.00 By Weight

KCl 0.0 Of Water KCl 4.0 Of Water KCl 3.94 Of Water

CaCl2 0.0 CaCl2 0.0 CaCl2 0.00

AlCl3 0.0 AlCl3 0.0 AlCl3 0.00

8.328 lb/gal 8.544 lb/gal 8.541 lb/gal

0.999 kg/liter 1.025 kg/liter 1.024 kg/liter

Density

********** Density and Mixing Volumes for Acid/Brine Mixtures **************

Fluid

Temperature

Mixture in Fracture

Tubing Fluid

Density

water

Density

Annulus Fluid

HELP


31/177

Gas Gravity 0.650

Discharge Coefficient 0.865

Ratio specific heats 1.270

0 0 0 0 0 0 0

200 67.5 86 106 128 153 178

400 135 172 212 256 306 356

600 202.5 258 318 384 459 534

800 270 344 424 512 612 712

1000 337.5 430 530 640 765 890

1200 405 516 636 768 918 10681400 472.5 602 742 896 1071 1246

1600 540 688 848 1024 1224 1424

1800 607.5 774 954 1152 1377 1602

2000 675 860 1060 1280 1530 1780

2200 742.5 946 1166 1408 1683 1958

2400 810 1032 1272 1536 1836 2136

2600 877.5 1118 1378 1664 1989 2314

2800 945 1204 1484 1792 2142 2492

3000 1012.5 1290 1590 1920 2295 2670

3200 1080 1376 1696 2048 2448 28483400 1147.5 1462 1802 2176 2601 3026

3600 1215 1548 1908 2304 2754 3204

3800 1282.5 1634 2014 2432 2907 3382

4000 1350 1720 2120 2560 3060 3560

4200 1417.5 1806 2226 2688 3213 3738

4400 1485 1892 2332 2816 3366 3916

4600 1552.5 1978 2438 2944 3519 4094

4800 1620 2064 2544 3072 3672 4272

5000 1687.5 2150 2650 3200 3825 4450

* Critical Flow can be assumed if the pressure downstream of the choke is less tha

8.42 lb/gal

P

ressure(psi)

Flowback Fluid Density

Flow of Water through Chokes

Flow

8 9 10 11 12 13

HELP


32/177

6 8 10 12 14 16

0.00 0.00 0.00 0.00 0.00 0.00 0.00

100.00 0.05 0.09 0.14 0.20 0.27 0.35

200.00 0.07 0.13 0.20 0.28 0.38 0.50

300.00 0.09 0.15 0.24 0.34 0.47 0.61

400.00 0.10 0.18 0.28 0.40 0.54 0.71

500.00 0.11 0.20 0.31 0.45 0.61 0.79

600.00 0.12 0.22 0.34 0.49 0.66 0.87

700.00 0.13 0.23 0.37 0.53 0.72 0.94

800.00 0.14 0.25 0.39 0.56 0.77 1.00

900.00 0.15 0.27 0.41 0.60 0.81 1.06

1000.00 0.16 0.28 0.44 0.63 0.86 1.12

1100.00 0.17 0.29 0.46 0.66 0.90 1.17

1200.00 0.17 0.31 0.48 0.69 0.94 1.23

1300.00 0.18 0.32 0.50 0.72 0.98 1.28

1400.00 0.19 0.33 0.52 0.74 1.01 1.32

1500.00 0.19 0.34 0.54 0.77 1.05 1.37

1600.00 0.20 0.35 0.55 0.80 1.08 1.42

1700.00 0.21 0.36 0.57 0.82 1.12 1.46

1800.00 0.21 0.38 0.59 0.84 1.15 1.50

1900.00 0.22 0.39 0.60 0.87 1.18 1.54

2000.00 0.22 0.40 0.62 0.89 1.21 1.58

2100.00 0.23 0.41 0.63 0.91 1.24 1.62

2200.00 0.23 0.41 0.65 0.93 1.27 1.66

2300.00 0.24 0.42 0.66 0.95 1.30 1.70

2400.00 0.24 0.43 0.68 0.98 1.33 1.73

2500.00 0.25 0.44 0.69 1.00 1.35 1.77

2600.00 0.25 0.45 0.70 1.01 1.38 1.80

2700.00 0.26 0.46 0.72 1.03 1.41 1.84

2800.00 0.26 0.47 0.73 1.05 1.43 1.87

2900.00 0.27 0.48 0.74 1.07 1.46 1.91

3000.00 0.27 0.48 0.76 1.09 1.48 1.94

3100.00 0.28 0.49 0.77 1.11 1.51 1.97

3200.00 0.28 0.50 0.78 1.13 1.53 2.00

3300.00 0.29 0.51 0.79 1.14 1.56 2.03

3400.00 0.29 0.52 0.81 1.16 1.58 2.06

3500.00 0.29 0.52 0.82 1.18 1.60 2.09

3600.00 0.30 0.53 0.83 1.19 1.63 2.12

3700.00 0.30 0.54 0.84 1.21 1.65 2.15

3800.00 0.31 0.55 0.85 1.23 1.67 2.18

3900.00 0.31 0.55 0.86 1.24 1.69 2.21

4000.00 0.31 0.56 0.87 1.26 1.71 2.24


33/177

4100.00 0.32 0.57 0.89 1.27 1.73 2.27

4200.00 0.32 0.57 0.90 1.29 1.76 2.29

4300.00 0.33 0.58 0.91 1.31 1.78 2.32

4400.00 0.33 0.59 0.92 1.32 1.80 2.35

4500.00 0.33 0.59 0.93 1.34 1.82 2.37

4600.00 0.34 0.60 0.94 1.35 1.84 2.40

4700.00 0.34 0.61 0.95 1.36 1.86 2.43

4800.00 0.34 0.61 0.96 1.38 1.88 2.45

4900.00 0.35 0.62 0.97 1.39 1.90 2.48

5000.00 0.35 0.63 0.98 1.41 1.92 2.50

5100.00 0.36 0.63 0.99 1.42 1.93 2.53

5200.00 0.36 0.64 1.00 1.44 1.95 2.55

5300.00 0.36 0.64 1.01 1.45 1.97 2.58

5400.00 0.37 0.65 1.02 1.46 1.99 2.60

5500.00 0.37 0.66 1.03 1.48 2.01 2.62

5600.00 0.37 0.66 1.03 1.49 2.03 2.65

5700.00 0.38 0.67 1.04 1.50 2.05 2.67

5800.00 0.38 0.67 1.05 1.52 2.06 2.69

5900.00 0.38 0.68 1.06 1.53 2.08 2.72

6000.00 0.39 0.69 1.07 1.54 2.10 2.74

6100.00 0.39 0.69 1.08 1.55 2.12 2.76

6200.00 0.39 0.70 1.09 1.57 2.13 2.79

6300.00 0.39 0.70 1.10 1.58 2.15 2.81

6400.00 0.40 0.71 1.11 1.59 2.17 2.83

6500.00 0.40 0.71 1.11 1.60 2.18 2.85

6600.00 0.40 0.72 1.12 1.62 2.20 2.876700.00 0.41 0.72 1.13 1.63 2.22 2.90

6800.00 0.41 0.73 1.14 1.64 2.23 2.92

6900.00 0.41 0.73 1.15 1.65 2.25 2.94

7000.00 0.42 0.74 1.16 1.67 2.27 2.96

7100.00 0.42 0.75 1.16 1.68 2.28 2.98

7200.00 0.42 0.75 1.17 1.69 2.30 3.00

7300.00 0.43 0.76 1.18 1.70 2.31 3.02

7400.00 0.43 0.76 1.19 1.71 2.33 3.04

7500.00 0.43 0.77 1.20 1.72 2.35 3.06

7600.00 0.43 0.77 1.21 1.74 2.36 3.087700.00 0.44 0.78 1.21 1.75 2.38 3.11

7800.00 0.44 0.78 1.22 1.76 2.39 3.13

7900.00 0.44 0.79 1.23 1.77 2.41 3.15

8000.00 0.45 0.79 1.24 1.78 2.42 3.16

8100.00 0.45 0.80 1.24 1.79 2.44 3.18

8200.00 0.45 0.80 1.25 1.80 2.45 3.20

Pressure(psi)


34/177

8300.00 0.45 0.81 1.26 1.81 2.47 3.22

8400.00 0.46 0.81 1.27 1.82 2.48 3.24

8500.00 0.46 0.82 1.27 1.84 2.50 3.26

8600.00 0.46 0.82 1.28 1.85 2.51 3.28

8700.00 0.46 0.83 1.29 1.86 2.53 3.30

8800.00 0.47 0.83 1.30 1.87 2.54 3.32

8900.00 0.47 0.83 1.30 1.88 2.56 3.34

9000.00 0.47 0.84 1.31 1.89 2.57 3.36

9100.00 0.47 0.84 1.32 1.90 2.58 3.38

9200.00 0.48 0.85 1.33 1.91 2.60 3.39

9300.00 0.48 0.85 1.33 1.92 2.61 3.41

9400.00 0.48 0.86 1.34 1.93 2.63 3.43

9500.00 0.49 0.86 1.35 1.94 2.64 3.45

9600.00 0.49 0.87 1.35 1.95 2.65 3.47

9700.00 0.49 0.87 1.36 1.96 2.67 3.49

9800.00 0.49 0.88 1.37 1.97 2.68 3.50

9900.00 0.50 0.88 1.38 1.98 2.70 3.52

10000.00 0.50 0.88 1.38 1.99 2.71 3.54

R

15000

20000

25000

30000

35000

40000

45000

FlowR

ate(M

scf/day)

Gas Flow throu


35/177

0

5000

Pres

0

5

10

15

20

25

30

0

500

1000

1500

2000

Rate(BPM

)

Pres

Water Flow thro


36/177


37/177

0 0 0 0 0 0 0 0

207 238 270 342 425 515 610 715

414 476 540 684 850 1030 1220 1430

621 714 810 1026 1275 1545 1830 2145

828 952 1080 1368 1700 2060 2440 2860

1035 1190 1350 1710 2125 2575 3050 3575

1242 1428 1620 2052 2550 3090 3660 42901449 1666 1890 2394 2975 3605 4270 5005

1656 1904 2160 2736 3400 4120 4880 5720

1863 2142 2430 3078 3825 4635 5490 6435

2070 2380 2700 3420 4250 5150 6100 7150

2277 2618 2970 3762 4675 5665 6710 7865

2484 2856 3240 4104 5100 6180 7320 8580

2691 3094 3510 4446 5525 6695 7930 9295

2898 3332 3780 4788 5950 7210 8540 10010

3105 3570 4050 5130 6375 7725 9150 10725

3312 3808 4320 5472 6800 8240 9760 114403519 4046 4590 5814 7225 8755 10370 12155

3726 4284 4860 6156 7650 9270 10980 12870

3933 4522 5130 6498 8075 9785 11590 13585

4140 4760 5400 6840 8500 10300 12200 14300

4347 4998 5670 7182 8925 10815 12810 15015

4554 5236 5940 7524 9350 11330 13420 15730

4761 5474 6210 7866 9775 11845 14030 16445

4968 5712 6480 8208 10200 12360 14640 17160

5175 5950 6750 8550 10625 12875 15250 17875

60% of the upstream pressure.

Choke Size (x/64)

Choke Size (x/64th)

Rate in Mscf/D

2618 20 22 24

f Gas through Chokes for Critical Flow*

14 15 16


38/177

18 20 22 24 28 32 40 48

0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

0.45 0.55 0.67 0.80 1.08 1.42 2.21 3.18

0.63 0.78 0.95 1.13 1.53 2.00 3.13 4.50

0.78 0.96 1.16 1.38 1.88 2.45 3.83 5.52

0.90 1.11 1.34 1.59 2.17 2.83 4.42 6.37

1.00 1.24 1.50 1.78 2.42 3.16 4.95 7.12

1.10 1.35 1.64 1.95 2.65 3.47 5.42 7.80

1.18 1.46 1.77 2.11 2.87 3.74 5.85 8.43

1.27 1.56 1.89 2.25 3.07 4.00 6.26 9.01

1.34 1.66 2.01 2.39 3.25 4.25 6.63 9.55

1.42 1.75 2.12 2.52 3.43 4.48 6.99 10.07

1.49 1.83 2.22 2.64 3.59 4.69 7.34 10.56

1.55 1.92 2.32 2.76 3.75 4.90 7.66 11.03

1.61 1.99 2.41 2.87 3.91 5.10 7.97 11.48

1.68 2.07 2.50 2.98 4.05 5.30 8.27 11.92

1.73 2.14 2.59 3.08 4.20 5.48 8.57 12.33

1.79 2.21 2.68 3.18 4.33 5.66 8.85 12.74

1.85 2.28 2.76 3.28 4.47 5.84 9.12 13.13

1.90 2.35 2.84 3.38 4.60 6.01 9.38 13.51

1.95 2.41 2.92 3.47 4.72 6.17 9.64 13.88

2.00 2.47 2.99 3.56 4.85 6.33 9.89 14.24

2.05 2.53 3.07 3.65 4.97 6.49 10.13 14.59

2.10 2.59 3.14 3.73 5.08 6.64 10.37 14.94

2.15 2.65 3.21 3.82 5.20 6.79 10.61 15.27

2.19 2.71 3.28 3.90 5.31 6.93 10.83 15.60

2.24 2.76 3.35 3.98 5.42 7.08 11.06 15.92

2.28 2.82 3.41 4.06 5.53 7.22 11.28 16.24

2.33 2.87 3.48 4.14 5.63 7.35 11.49 16.55

2.37 2.93 3.54 4.21 5.73 7.49 11.70 16.85

2.41 2.98 3.60 4.29 5.84 7.62 11.91 17.15

2.45 3.03 3.66 4.36 5.94 7.75 12.11 17.44

2.49 3.08 3.72 4.43 6.03 7.88 12.31 17.73

2.53 3.13 3.78 4.50 6.13 8.01 12.51 18.02

2.57 3.18 3.84 4.57 6.23 8.13 12.70 18.29

2.61 3.22 3.90 4.64 6.32 8.25 12.90 18.57

2.65 3.27 3.96 4.71 6.41 8.37 13.08 18.84

2.69 3.32 4.01 4.78 6.50 8.49 13.27 19.11

2.72 3.36 4.07 4.84 6.59 8.61 13.45 19.37

2.76 3.41 4.12 4.91 6.68 8.73 13.63 19.63

2.80 3.45 4.18 4.97 6.77 8.84 13.81 19.89

2.83 3.50 4.23 5.04 6.85 8.95 13.99 20.14


39/177

2.87 3.54 4.28 5.10 6.94 9.06 14.16 20.39

2.90 3.58 4.34 5.16 7.02 9.17 14.33 20.64

2.94 3.63 4.39 5.22 7.11 9.28 14.50 20.88

2.97 3.67 4.44 5.28 7.19 9.39 14.67 21.12

3.00 3.71 4.49 5.34 7.27 9.49 14.84 21.36

3.04 3.75 4.54 5.40 7.35 9.60 15.00 21.60

3.07 3.79 4.59 5.46 7.43 9.70 15.16 21.83

3.10 3.83 4.64 5.52 7.51 9.81 15.32 22.06

3.13 3.87 4.68 5.57 7.59 9.91 15.48 22.29

3.17 3.91 4.73 5.63 7.66 10.01 15.64 22.52

3.20 3.95 4.78 5.69 7.74 10.11 15.79 22.74

3.23 3.99 4.82 5.74 7.81 10.21 15.95 22.97

3.26 4.03 4.87 5.80 7.89 10.30 16.10 23.18

3.29 4.06 4.92 5.85 7.96 10.40 16.25 23.40

3.32 4.10 4.96 5.90 8.04 10.50 16.40 23.62

3.35 4.14 5.01 5.96 8.11 10.59 16.55 23.83

3.38 4.17 5.05 6.01 8.18 10.69 16.70 24.04

3.41 4.21 5.09 6.06 8.25 10.78 16.84 24.25

3.44 4.25 5.14 6.12 8.32 10.87 16.99 24.46

3.47 4.28 5.18 6.17 8.39 10.96 17.13 24.67

3.50 4.32 5.23 6.22 8.46 11.05 17.27 24.87

3.53 4.35 5.27 6.27 8.53 11.14 17.41 25.08

3.55 4.39 5.31 6.32 8.60 11.23 17.55 25.28

3.58 4.42 5.35 6.37 8.67 11.32 17.69 25.48

3.61 4.46 5.39 6.42 8.74 11.41 17.83 25.68

3.64 4.49 5.44 6.47 8.80 11.50 17.97 25.873.67 4.53 5.48 6.52 8.87 11.59 18.10 26.07

3.69 4.56 5.52 6.57 8.94 11.67 18.24 26.26

3.72 4.59 5.56 6.61 9.00 11.76 18.37 26.45

3.75 4.63 5.60 6.66 9.07 11.84 18.50 26.64

3.77 4.66 5.64 6.71 9.13 11.93 18.64 26.83

3.80 4.69 5.68 6.76 9.20 12.01 18.77 27.02

3.83 4.72 5.72 6.80 9.26 12.09 18.90 27.21

3.85 4.76 5.75 6.85 9.32 12.18 19.02 27.40

3.88 4.79 5.79 6.90 9.38 12.26 19.15 27.58

3.90 4.82 5.83 6.94 9.45 12.34 19.28 27.763.93 4.85 5.87 6.99 9.51 12.42 19.41 27.95

3.96 4.88 5.91 7.03 9.57 12.50 19.53 28.13

3.98 4.91 5.95 7.08 9.63 12.58 19.66 28.31

4.01 4.95 5.98 7.12 9.69 12.66 19.78 28.48

4.03 4.98 6.02 7.17 9.75 12.74 19.90 28.66

4.06 5.01 6.06 7.21 9.81 12.82 20.03 28.84


40/177

4.08 5.04 6.09 7.25 9.87 12.90 20.15 29.01

4.10 5.07 6.13 7.30 9.93 12.97 20.27 29.19

4.13 5.10 6.17 7.34 9.99 13.05 20.39 29.36

4.15 5.13 6.20 7.38 10.05 13.13 20.51 29.53

4.18 5.16 6.24 7.43 10.11 13.20 20.63 29.70

4.20 5.19 6.28 7.47 10.17 13.28 20.75 29.87

4.22 5.22 6.31 7.51 10.22 13.35 20.86 30.04

4.25 5.25 6.35 7.55 10.28 13.43 20.98 30.21

4.27 5.27 6.38 7.59 10.34 13.50 21.10 30.38

4.30 5.30 6.42 7.64 10.39 13.58 21.21 30.55

4.32 5.33 6.45 7.68 10.45 13.65 21.33 30.71

4.34 5.36 6.49 7.72 10.51 13.72 21.44 30.88

4.37 5.39 6.52 7.76 10.56 13.80 21.56 31.04

4.39 5.42 6.55 7.80 10.62 13.87 21.67 31.20

4.41 5.45 6.59 7.84 10.67 13.94 21.78 31.37

4.43 5.47 6.62 7.88 10.73 14.01 21.89 31.53

4.46 5.50 6.66 7.92 10.78 14.08 22.01 31.69

4.48 5.53 6.69 7.96 10.84 14.15 22.12 31.85

te in BPM

gh Chokes /64th


41/177

ure (psi)

2500

3000

3500

4000

4500

5000

sure si

gh Chokes /64th


42/177


43/177

0 0 0 0 0

835 950 1080 1365 1685

1670 1900 2160 2730 3370

2505 2850 3240 4095 5055

3340 3800 4320 5460 6740

4175 4750 5400 6825 8425

5010 5700 6480 8190 101105845 6650 7560 9555 11795

6680 7600 8640 10920 13480

7515 8550 9720 12285 15165

8350 9500 10800 13650 16850

9185 10450 11880 15015 18535

10020 11400 12960 16380 20220

10855 12350 14040 17745 21905

11690 13300 15120 19110 23590

12525 14250 16200 20475 25275

13360 15200 17280 21840 2696014195 16150 18360 23205 28645

15030 17100 19440 24570 30330

15865 18050 20520 25935 32015

16700 19000 21600 27300 33700

17535 19950 22680 28665 35385

18370 20900 23760 30030 37070

19205 21850 24840 31395 38755

20040 22800 25920 32760 40440

20875 23750 27000 34125 42125

36 4028 30 32


44/177

54

0.00

4.03

5.70

6.98

8.06

9.01

9.87

10.66

11.40

12.09

12.75

13.37

13.96

14.53

15.08

15.61

16.12

16.62

17.10

17.57

18.03

18.47

18.91

19.33

19.75

20.15

20.55

20.94

21.33

21.71

22.08

22.44

22.80

23.15

23.50

23.85

24.18

24.52

24.85

25.17

25.49


45/177

25.81

26.12

26.43

26.74

27.04

27.34

27.63

27.92

28.21

28.50

28.78

29.07

29.34

29.62

29.89

30.16

30.43

30.70

30.96

31.22

31.48

31.74

31.99

32.24

32.50

32.7432.99

33.24

33.48

33.72

33.96

34.20

34.44

34.67

34.91

35.1435.37

35.60

35.82

36.05

36.28

36.50


46/177

36.72

36.94

37.16

37.38

37.60

37.81

38.02

38.24

38.45

38.66

38.87

39.08

39.29

39.49

39.70

39.90

40.10

40.31

8

10

12

14

16

1820

24

28

30


47/177

36

40

6

8

10

12

14

1618

20

22

24

28

3240

48

54


48/177


49/177

Base Fluid Density (lb/gal)

8.34

Acid Density (lb/gal) Tubing Tubing Tubing Stage Tubing

9.20 Proppant Type Rate Volume Fluid

Stage Type Begin End BPM Gallons Type Begin E

1 2 0.0 0.0 0.04247 2.0 11000 0

2 3 1.0 1.0 0.04247 3.0 1200 0

3 4 0.0 0.0 0.04247 3.0 4000 0

4 17 1.0 1.0 0.04247 3.0 1200 0

5 4 0.0 0.0 0.04247 3.0 6000 0

6 7 0.0 0.0 0.04247 3.0 500 0

7 8 0.0 0.0 0.04247 3.0 1500 0

8 9 0.0 0.0 0.04247 3.0 315 0

9 10 0.0 0.0 0.04247 0.5 800 0

10 11 0.0 0.0 0.04247 0.5 519 1

11 11 0.0 0.0 0.04247 0.5 269 2

12 11 0.0 0.0 0.04247 0.5 185 3

13 11 0.0 0.0 0.04247 0.5 479 4 4

14 11 0.0 0.0 0.04247 0.5 198 5

15 12 0.0 0.0 0.04247 0.5 54 8

16 13 0.0 0.0 0.04247 0.5 136 0

17 14 0.0 0.0 0.04247 0.0 0 0

18 2 0.0 0.0 0.04247 2.0 11000 0

19 3 1.0 1.0 0.04247 3.0 1200 0

20 4 0.0 0.0 0.04247 3.0 4000 0

21 6 1.0 1.0 0.04247 3.0 1200 0

22 4 0.0 0.0 0.04247 3.0 6000 0

23 7 0.0 0.0 0.04247 3.0 500 0

24 8 0.0 0.0 0.04247 3.0 1500 0

25 9 0.0 0.0 0.04247 3.0 315 0

26 10 0.0 0.0 0.04247 0.5 86 1

27 11 0.0 0.0 0.04247 0.5 269 2

28 11 0.0 0.0 0.04247 0.5 278 3

29 11 0.0 0.0 0.04247 0.5 192 4 4

3011

0.0 0.0 0.04247 0.5 396 5

Tubing

Prop Conc (lb/gal)

Annulus

Prop Conc (lb/g

Fil l Down

HELP HydraJet Velocity Calculate Annu lar Volumes from Tubing Calculate T


50/177

31 11 0.0 0.0 0.04247 0.5 217 8

32 12 0.0 0.0 0.04247 0.5 42 0

33 13 0.0 0.0 0.04247 0.5 136 0

34 14 0.0 0.0 0.04247 0.0 0 0

35 1 0.0 0.0 0.04247 0.0 0 0

36 1 0.0 0.0 0.04247 0.0 0 0

37 1 0.0 0.0 0.04247 0.0 0 0

38 1 0.0 0.0 0.04247 0.0 0 0

39 1 0.0 0.0 0.04247 0.0 0 0

40 1 0.0 0.0 0.04247 0.0 0 0

41 1 0.0 0.0 0.04247 0.0 0 042 1 0.0 0.0 0.04247 0.0 0 0

43 1 0.0 0.0 0.04247 0.0 0 0

44 1 0.0 0.0 0.04247 0.0 0 0

45 1 0.0 0.0 0.04247 0.0 0 0

46 1 0.0 0.0 0.04247 0.0 0 0

47 1 0.0 0.0 0.04247 0.0 0 0

48 1 0.0 0.0 0.04247 0.0 0 0

49 1 0.0 0.0 0.04247 0.0 0 0

50 1 0.0 0.0 0.04247 0.0 0 0

51 1 0.0 0.0 0.04247 0.0 0 0

52 1 0.0 0.0 0.04247 0.0 0 0

53 1 0.0 0.0 0.04247 0.0 0 0

54 1 0.0 0.0 0.04247 0.0 0 0

55 1 0.0 0.0 0.04247 0.0 0 0

56 1 0.0 0.0 0.04247 0.0 0 0

57 1 0.0 0.0 0.04247 0.0 0 0

58 1 0.0 0.0 0.04247 0.0 0 0

59 1 0.0 0.0 0.04247 0.0 0 0

60 1 0.0 0.0 0.04247 0.0 0 0

61 1 0.0 0.0 0.04247 0.0 0 0

62 1 0.0 0.0 0.04247 0.0 0 0

63 1 0.0 0.0 0.04247 0.0 0 0

64 1 0.0 0.0 0.04247 0.0 0 0

65 1 0.0 0.0 0.04247 0.0 0 0


51/177

66 1 0.0 0.0 0.04247 0.0 0 0

67 1 0.0 0.0 0.04247 0.0 0 0

68 1 0.0 0.0 0.04247 0.0 0 0

69 1 0.0 0.0 0.04247 0.0 0 0

70 1 0.0 0.0 0.04247 0.0 0 0

71 1 0.0 0.0 0.04247 0.0 0 0

72 1 0.0 0.0 0.04247 0.0 0 0

73 1 0.0 0.0 0.04247 0.0 0 0

74 1 0.0 0.0 0.04247 0.0 0 0

75 1 0.0 0.0 0.04247 0.0 0 0

76 1 0.0 0.0 0.04247 0.0 0 077 1 0.0 0.0 0.04247 0.0 0 0

78 1 0.0 0.0 0.04247 0.0 0 0

79 1 0.0 0.0 0.04247 0.0 0 0

80 1 0.0 0.0 0.04247 0.0 0 0

81 1 0.0 0.0 0.04247 0.0 0 0

82 1 0.0 0.0 0.04247 0.0 0 0

83 1 0.0 0.0 0.04247 0.0 0 0

84 1 0.0 0.0 0.04247 0.0 0 0

85 1 0.0 0.0 0.04247 0.0 0 0

86 1 0.0 0.0 0.04247 0.0 0 0

87 1 0.0 0.0 0.04247 0.0 0 0

88 1 0.0 0.0 0.04247 0.0 0 0

89 1 0.0 0.0 0.04247 0.0 0 0

90 1 0.0 0.0 0.04247 0.0 0 0

91 1 0.0 0.0 0.04247 0.0 0 0

92 1 0.0 0.0 0.04247 0.0 0 0

93 1 0.0 0.0 0.04247 0.0 0 0

94 1 0.0 0.0 0.04247 0.0 0 0

95 1 0.0 0.0 0.04247 0.0 0 0

96 1 0.0 0.0 0.04247 0.0 0 0

97 1 0.0 0.0 0.04247 0.0 0 0

98 1 0.0 0.0 0.04247 0.0 0 0

99 1 0.0 0.0 0.04247 0.0 0 0

100 1 0.0 0.0 0.04247 0.0 0 0


52/177


53/177


54/177


55/177


56/177


57/177


58/177


59/177


60/177


61/177


62/177


63/177


64/177


65/177


66/177


67/177


68/177


69/177


70/177


71/177


72/177


73/177


74/177


75/177


76/177


77/177


78/177


79/177


80/177


81/177


82/177


83/177


84/177


85/177


86/177


87/177

Tubing Tubing Tubing Max Tubing Max Nozz

Annulus Annulus Ann. Stage Annulus BHTP Stage Dirty Stage Prop Cum Prop Pressure Pressure Dr

Proppant Type Rate (BPM) Volume (gal) Fluid Gradient Volume (gal) Weight (lbs) Weight (lbs) (psi) (psi)

BPM Gallons Type psi/ft

0.037437012 0 0 0.91 11000 0 0 8096 139

0.037437012 0 0 0.91 1251 1200 1200 10043 335

0.037437012 0 0 0.91 4000 0 1200 10009 312

0.037437012 0 0 0.91 1251 1200 2400 10043 335

0.037437012 0 0 0.91 6000 0 2400 10009 312

0.037437012 0 0 0.91 500 0 2400 9761 3440.037437012 0 0 0.91 1500 0 2400 10009 312

0.037437012 30 3150 0.91 315 0 2400 10009 312

0.037437012 30 48000 0.91 800 0 2400 7322 9

0.037437012 30 30000 0.91 519 0 2400 6132 9

0.037437012 30 15000 0.91 269 0 2400 6132 9

0.037437012 30 10000 0.91 185 0 2400 6132 9

0.037437012 30 25000 0.91 479 0 2400 6132 9

0.037437012 30 10000 0.91 198 0 2400 6132 9

0.037437012 30 2500 0.91 54 0 2400 6132 9

0.037437012 30 8187 0.91 136 0 2400 6132 9

0.037437012 0 0 0.91 0 0 2400 5720 0

0.037437012 0 0 0.86 11000 0 2400 7496 1390.037437012 0 0 0.86 1251 1200 3600 9443 335

0.037437012 0 0 0.86 4000 0 3600 9409 312

0.037437012 0 0 0.86 1251 1200 4800 9443 335

0.037437012 0 0 0.86 6000 0 4800 9409 312

0.037437012 0 0 0.86 500 0 4800 9161 344

0.037437012 0 0 0.86 1500 0 4800 9409 312

0.037437012 30 3150 0.86 315 0 4800 9409 312

0.037437012 30 5000 0.86 86 0 4800 8848 9

0.037437012 30 15000 0.86 269 0 4800 8047 9

0.037437012 30 15000 0.86 278 0 4800 5532 9

0.037437012 30 10000 0.86 192 0 4800 5532 9

0.037437012 30 20000 0.86 396 0 4800 5532 9

Fill Down

Volumes fr om Annulus


88/177

0.037437012 30 10000 0.7 217 0 4800 3612 9

0.037437012 30 2500 0.7 42 0 4800 3612 9

0.037437012 30 8187 0.7 136 0 4800 3612 9

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 00.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0


89/177

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 00.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.7 0 0 4800 3200 0

0.037437012 0 0 0.86 0 0 4800 5120 0


90/177


91/177


92/177


93/177


94/177


95/177


96/177


97/177


98/177


99/177


100/177


101/177


102/177


103/177


104/177


105/177


106/177


107/177


108/177


109/177


110/177


111/177


112/177


113/177


114/177


115/177


116/177


117/177


118/177


119/177


120/177


121/177


122/177


123/177


124/177


125/177

Annulus Annulus Annulus Annulus Stage Cum

Stage Dirty Stage Prop Cum Prop Pressure Time Time

Volume (gal) Weight (lbs) Weight (lbs) (psi) (min) (min) Rate

0 NoRate TI

0 0 0 5720 131.0 131.0 0 TRUE

0 0 0 5720 9.5 140.5 0 TRUE

0 0 0 5720 31.7 172.2 0 TRUE

0 0 0 5720 9.5 181.7 0 TRUE

0 0 0 5720 47.6 229.4 0 TRUE

0 0 0 5720 4.0 233.3 0 TRUE

0 0 0 5720 11.9 245.2 0 TRUE

3150 0 0 7029 2.5 247.7 0 TRUE

48000 0 0 8074 38.1 285.8 0 TRUE

31123 30000 30000 7896 23.8 309.6 0 TRUE

16123 30000 60000 7746 11.9 321.5 0 TRUE

11123 30000 90000 7623 7.9 329.5 0 TRUE

28744 100000 190000 7523 19.8 349.3 0 TRUE

11872 50000 240000 7444 7.9 357.3 0 TRUE

3249 20000 260000 7729 2.0 359.2 0 TRUE

8187 0 260000 8074 6.5 365.7 0 TRUE

0 0 260000 5720 0.0 365.7 1 FALSE

0 0 260000 5120 131.0 496.7 1 TRUE

0 0 260000 5120 9.5 506.2 1 TRUE

0 0 260000 5120 31.7 538.0 1 TRUE

0 0 260000 5120 9.5 547.5 1 TRUE

0 0 260000 5120 47.6 595.1 1 TRUE

0 0 260000 5120 4.0 599.1 1 TRUE

0 0 260000 5120 11.9 611.0 1 TRUE

3150 0 260000 6429 2.5 613.5 1 TRUE

5187 5000 265000 7554 4.0 617.5 1 TRUE

16123 30000 295000 7146 11.9 629.4 1 TRUE

16685 45000 340000 7023 11.9 641.3 1 TRUE

11497 40000 380000 6923 7.9 649.2 1 TRUE

23744 100000 480000 6844 15.9 665.1 1 TRUE


126/177

12995 80000 560000 4796 7.9 673.0 1 TRUE

2500 0 560000 4051 2.0 675.0 1 TRUE

8187 0 560000 5554 6.5 681.5 1 TRUE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE


127/177

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 3200 0.0 681.5 2 FALSE

0 0 560000 5120 0.0 681.5 2 FALSE


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Tubing RateTubing PresTubing Pro AnnRate AnnPress AnnProp1

2.0 8096 0.0 0 5720 0 2.0

2.0 8096 0.0 0 5720 0 3.0

3.0 10043 1.0 0 5720 0 3.0

3.0 10043 1.0 0 5720 0 3.0

3.0 10009 0.0 0 5720 0 3.0

3.0 10009 0.0 0 5720 0 3.0

3.0 10043 1.0 0 5720 0 3.0

3.0 10043 1.0 0 5720 0 3.0

3.0 10009 0.0 0 5720 0 3.0

3.0 10009 0.0 0 5720 0 3.0

3.0 9761 0.0 0 5720 0 3.0

3.0 9761 0.0 0 5720 0 3.0

3.0 10009 0.0 0 5720 0 3.0

3.0 10009 0.0 0 5720 0 3.0

3.0 10009 0.0 0 7029 0 3.0

3.0 10009 0.0 30 7029 0 0.5

0.5 7322 0.0 30 8074 0 0.5

0.5 7322 0.0 30 8074 0 0.5

0.5 6132 0.0 30 7896 1 0.5

0.5 6132 0.0 30 7896 1 0.5

0.5 6132 0.0 30 7746 2 0.5

0.5 6132 0.0 30 7746 2 0.5

0.5 6132 0.0 30 7623 3 0.5

0.5 6132 0.0 30 7623 3 0.5

0.5 6132 0.0 30 7523 4 0.5

0.5 6132 0.0 30 7523 4 0.5

0.5 6132 0.0 30 7444 5 0.5

0.5 6132 0.0 30 7444 5 0.5

0.5 6132 0.0 30 7729 8 0.5

0.5 6132 0.0 30 7729 8 0.5


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0.5 6132 0.0 30 8074 0 0.5

0.5 6132 0.0 30 8074 0 0.0

0.0 5720 0.0 30 5720 0 0.0

0.0 5720 0.0 0 5720 0 2.0

2.0 7496 0.0 0 5120 0 2.0

2.0 7496 0.0 0 5120 0 3.0

3.0 9443 1.0 0 5120 0 3.0

3.0 9443 1.0 0 5120 0 3.0

3.0 9409 0.0 0 5120 0 3.0

3.0 9409 0.0 0 5120 0 3.0

3.0 9443 1.0 0 5120 0 3.03.0 9443 1.0 0 5120 0 3.0

3.0 9409 0.0 0 5120 0 3.0

3.0 9409 0.0 0 5120 0 3.0

3.0 9161 0.0 0 5120 0 3.0

3.0 9161 0.0 0 5120 0 3.0

3.0 9409 0.0 0 5120 0 3.0

3.0 9409 0.0 0 5120 0 3.0

3.0 9409 0.0 0 6429 0 3.0

3.0 9409 0.0 30 6429 0 0.5

0.5 8848 0.0 30 7554 1 0.5

0.5 8848 0.0 30 7554 1 0.5

0.5 8047 0.0 30 7146 2 0.5

0.5 8047 0.0 30 7146 2 0.5

0.5 5532 0.0 30 7023 3 0.5

0.5 5532 0.0 30 7023 3 0.5

0.5 5532 0.0 30 6923 4 0.5

0.5 5532 0.0 30 6923 4 0.5

0.5 5532 0.0 30 6844 5 0.5

0.5 5532 0.0 30 6844 5 0.5

0.5 3612 0.0 30 4796 8 0.5

0.5 3612 0.0 30 4796 8 0.5

0.5 3612 0.0 30 4051 0 0.5

0.5 3612 0.0 30 4051 0 0.0

0.5 3612 0.0 30 5554 0 0.0


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0.5 3612 0.0 30 5554 0 0.0

0.0 3200 0.0 30 3200 0 0.0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.00.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0


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0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.00.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 00.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0


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0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.00.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 00.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0


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0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0 0.0

0.0 3200 0.0 0 3200 0

0.0 3200 0.0 0 3200 0

0.0 5120 0.0 0 5120 0

0.0 5120 0.0 0 5120 0

0.0 0 0.0 0 5120 0

0.0 0 0.0 0


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0.0

5.0

10

15

20

25

30

35

0

2000

4000

6000

8000

10000

12000

0.0 100.0 200.0 300.0 400.0 500.0 600.0 700.0 800.0

Pressure

Time

Total Job Plot

Tubing Pressure AnnPress Tubing Rate AnnRate Tubing Proppant Concentration AnnProp1


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tage # Stage Description

Stage Clean

Volume Fluid Rate Begin End

Stage Clean

Volume Fluid Rate Beg

1 Load well / Circ to next zone 11000 30# WaterFrac-G 2 0 0 0 0 0

2 1st Cutting Stage 1200 30# WaterFrac-G 3 1 1 0 0 0

3 Spacer 4000 30# WaterFrac-G 3 0 0 0 0 0

4 Step-Down Test 1200 30# WaterFrac-G 3 1 1 0 0 0


6 ACID 500 30# WaterFrac-G 3 0 0 0 0 0

7 Displace Acid while Jetting 1500 30# WaterFrac-G 3 0 0 0 0 0

8 Breakdown and Establish Injection 315 30# WaterFrac-G 3 0 0 3150 40# Hybor-G 30 0

9 PAD 800 30# WaterFrac-G 0.5 0 0 48000 40# Hybor-G 30 0

10 SLF 519 30# WaterFrac-G 0.5 0 0 30000 40# Hybor-G 30 1





15 Screen-out Slug 54 30# WaterFrac-G 0.5 0 0 2500 40# Hybor-G 30 8

16 Flush 136 30# WaterFrac-G 0.5 0 0 8187 30# WaterFrac-G 30 0

17 POOH to next interval 0 30# WaterFrac-G 0 0 0 0 0 0

18 Load well / Circ to next zone 11000 30# WaterFrac-G 2 0 0 0 0 0

19 1st Cutting Stage 1200 30# WaterFrac-G 3 1 1 0 0 020 Spacer 4000 30# WaterFrac-G 3 0 0 0 0 0

21 2nd Cutting Stage 1200 30# WaterFrac-G 3 1 1 0 0 0


23 ACID 500 30# WaterFrac-G 3 0 0 0 0 0

24 Displace Acid while Jetting 1500 30# WaterFrac-G 3 0 0 0 0 0

25 Breakdown and Establish Injection 315 30# WaterFrac-G 3 0 0 3150 40# Hybor-G 30 0

26 PAD 86 30# WaterFrac-G 0.5 0 0 5000 40# Hybor-G 30 1






32 Screen-out Slug 42 30# WaterFrac-G 0.5 0 0 2500 40# Hybor-G 30 0

33 Flush 136 30# WaterFrac-G 0.5 0 0 8187 30# WaterFrac-G 30 0

34 POOH to next interval 0 30# WaterFrac-G 0 0 0 0 30# WaterFrac-G 0 0

Tubing AnnulusP

Co

Proppant

Concentration

Company Name

Well Name11/10/2014

Job Pumping Summary


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35 Not Used 0 30# WaterFrac-G 0 0 0 0 30# WaterFrac-G 0



38 Not Used 0 30# WaterFrac-G 0 0 0


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End

0

0

0

00

0

0

0

0

1

2

3

4

5

8

0

0

0

0

0

0

0

0

0

0

1

2

3

4

5

8

0

0

0

nt

ation


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0

0

0


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Worksheet in Test nozzle - Design.xls

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