cpf-010 process line sizing attachment_0.xls

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Cover

Calculation Cover Sheet

Calc no (CPF)-CA-PRO-010Project title Melut Basin Oil Development Package A Proj no 4211095Client Petrodar Operating Company Limited Phase/CTR DetailedCalculation title Process Line Sizing Page 1 of 37Calculation objectiveTo determine process line sizes for Al-Jabalayn CPF plant.

Calculation method

Assumptions

References

ConclusionsRefer to the attached summary of selected line sizes.

A 6-Sep-04 Issued for Review KBWREV DATE DESCRIPTION BY CHECKED

The lines were sized based on the criteria presented in Ranhill Worley Design Standard - Line Sizing (086\00589-PR-DS-003) with respect to velocity and pressure drop through the line.

The fluid velocity and pressure drop were calculated for a given line size according to the Standard Line Sizing Spreadsheets (References 1,2).

Refer to Reference 3 for sizing criteria.

1. Standard Calculation PR-CA-002 - Single Phase Pressure Drop2. Standard Calculation PR-CA-001 - Two Phase Pressure Drop3. Ranhill Worley Design Standard - Line Sizing (086\00589-PR-DS-003)

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Checklist

Calculation Checklist

Calc no (CPF)-CA-PRO-010Project title Melut Basin Oil Development Package A Proj no 4211095Client Petrodar Operating Company Limited Phase/CTR DetailedCalculation title Process Line Sizing Page 2 of 37Please check boxes for all applicable items checked or delete if not appropriate:Calculations:

Project title shown.Calculation title shown.Revision history box complete and signed.Index.Appropriate stamp for preliminary issues.Calculation objectives (aims) stated.Calculation method defined or described (including formulae if relevant).Reference made to text, standard or code. Check version/edition with that required for project.

Source of input data stated (with revision number and date if relevant).Assumptions stated.Summary of results or conclusions if appropriate.For software based calculations, reference to software verification if available.Method clear and easy to follow.Input data correct.

Calculation result within expected limits.Calculation tolerances stated if significant.Units used as required by client.Abbreviations correct.Appropriate cross-references.Sketches included and clearly labelled, where required.Attachments included and referenced, as required.

Checking records:Checked and annotated copy of calculation filed (use "Check Print" stamp).Corrections made as required and calculation dated and signed on cover sheet by checker.

Revisions:Changes clouded.Revision history block updated.Calculation re-checked if required.

A 6-Sep-04 Issued for Review KBWREV DATE DESCRIPTION BY CHECKED

Calculation number assigned and registered (usual format is Proj No-CAL-Discipline code-Seq No eg XXXX-CAL-E-001, but format may be varied by Project Manager).

Calculation arithmetically correct OR software previously verified and reference to verification checked.

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Summary

Calculation SheetCalc no (CPF)-CA-PRO-010

Project title Melut Basin Oil Development Package A Proj no 4211095Client Petrodar Operating Company Limited Phase/CTR DetailedCalculation title Process Line Sizing Page 3 of 37Activity Line Sizing Summary File

Line No. Description Phase PWH SCH Rating Velocity [m/s]

Inlet Manifold 1 500 24"-CO-CC-1275-38H 2,082,075 Liquid 600 80 600# 2.7 19.1 2 - 3 90.0

Inlet Manifold 2 500 24"-CO-AC-1000-38H 2,082,075 Liquid 600 STD 150# 2.3 14.1 2 - 3 90.0

Surge Vessel 1 501B 12"-CO-AC-1004-38H 277,610 Liquid 300 20 150# 1.1 24.4 2 - 3 90.0

Surge Vessel 2 503B 12"-CO-AC-1009-38H 277,527 Liquid 300 20 150# 1.1 24.4 2 - 3 90.0

Surge Vessel 3 504B 4"-PW-AC-2000-25PP 39,627 Liquid 100 40 150# 1.4 16.3 1.5 to 2.1 6 to 45

503 24"-CO-AC-1014-38H 2,081,454 Raw Crude Header Liquid 600 STD 150# 2.3 14.0 2 - 3 90.0

503C 8"-CO-AC-1015-38H 154,182 Liquid 200 20 150# 1.4 68.9 2 - 3 90.0

505C 8"-CO-AC-1030-38H 154,182 Liquid 200 20 150# 1.4 15.2 2 - 3 90.0

506C 8"-CO-AC-1045-38H 154,182 Liquid 200 20 150# 1.5 14.2 2 - 3 90.0

507C 138,371 Liquid 200 20 150# 1.3 10.8 2 - 3 90.0

510C Dehydrator Gas Outlet 157 Vapour 50 40 150# 8.7 3.7 20 - 30 1 - 3

512C 3"-PW-AC-2005-25PP 15,811 Liquid 80 40 150# 1.0 10.9 1.5 to 2.1 6 to 45

506C 4"-CO-AC-1109-25H-ET 51,394 Liquid 100 40 150# 2.0 59.3 2 - 3 90.0

508C 8"-CO-AC-1090-38H 138,371 Liquid 200 20 150# 1.3 14.7 2 - 3 90.0

508 24"-CO-AC-1105-38H 1,868,007 Liquid 600 STD 150# 2.1 9.0 2 - 3 90.0

Gas Boot 1 514 24"-CO-AC-1320-38H-ET 1,868,007 Liquid 600 STD 150# 2.1 9.0 2 - 3 90.0

Gas Boot 2 0 8"-G-A-6067 3,593 From Gas Boot 2 (V-5404) to atmosphere Vapour 200 20 150# 17.4 2.0 20 - 40 1 - 3

515 (1) 24"-CO-AC-1148, 1242-38H-ET 1,114,424 Liquid 600 STD 150# 1.3 3.7 1.8 to 5 2 - 7

515 (2) 32"-CO-AC-1258-38H-ET 2,228,849 Sales Oil Header Liquid 800 20 150# 1.4 3.1 1.8 to 5 2 - 7

515 (1) 24"-CO-AC-1150-38H-ET 742,950 Liquid 600 STD 150# 0.8 1.8 1.8 to 5 2 - 7

515 (2) 16"-CO-AC-1153-38H-ET 742,950 Liquid 400 20 150# 1.9 12.9 1.8 to 5 35 - 45

515 (1) 24"-CO-AC-1213-38H-ET 2,228,849 Liquid 600 STD 150# 2.5 12.3 5.0 35 - 45

515 (2) 10"-CO-AC-1158-38H-ET 249,133 Liquid 250 20 150# 1.5 13.4 5.0 35 - 45

515 12"-CO-AC-1158-38H-ET 747,398 Liquid 300 20 150# 3.1 38.3 5.0 35 - 45

0 8"-CO-AC-1269-25H-ET 69,225 Pump Station Yo-Yo Operation Oil Header Liquid 200 20 150# 0.6 30.8 2 - 3 90.0

0 (1) 4"-CO-AC-1265-25H-ET 22,244 Liquid 100 40 150# 0.8 15.4 2 - 3 90.0

0 (2) 8"-CO-AC-1165-38H-ET 560,549 Meter Prover Skid (MP-5401) Liquid 200 20 150# 5.2 163.9 2 - 3 90.0

Off Spec Oil 1 0 (1) 16"-CO-AC-1173-38H-ET 1,387,638 Liquid 400 20 150# 3.6 40.6 2 - 3 90.0

Off Spec Oil 1 0 (2) 12"-CO-AC-1174-38H-ET 90,060 Off Spec Oil Pumps (P-5404A/B) suction line Liquid 300 20 150# 0.4 0.9 1.8 2 - 7

Off Spec Oil 2 0 (1) 8"-CO-AC-1176-38H-ET 90,060 Liquid 200 20 150# 0.8 4.9 4.3 35 - 45

Off Spec Oil 2 0 (2) 6"-CO-AC-1179-25H-ET 54,036 Liquid 150 40 150# 0.9 9.5 3.0 23 - 35

0 (1) 16"-PW-AC-2023-50PP 560,000 Produced Water Header Liquid 400 20 150# 1.3 3.2 3.7 to 4.6 6 to 45

0 (2) 8"-PW-AC-2024-38PP 280,000 Liquid 200 20 150# 2.3 20.7 2.5 to 3 6 to 45

0 (1) 4"-CO-AC-1186-25H-ET 13,650 Liquid 100 40 150# 0.5 33.3 1.5 to 2.1 6 to 45

0 (2) 8"-PW-AC-2028-50PP 280,000 Liquid 200 20 150# 2.3 20.7 2.5 to 3 6 to 45

0 (1) 8"-PW-AC-2041 197,648 Liquid 200 20 150# 1.7 10.2 2.5 to 3 6 to 45

0 (2) 8"-PW-CC-2017 197,648 Liquid 200 80 600# 1.9 14.1 2.5 to 3 6 to 45

0 3"-PW-CC-2032 59,295 Liquid 100 40 600# 3.5 141.9 1.5 to 2.3 6 to 45

Skimmed Oil 1 0 6"-CO-AC-1188-25H-ET 4,550 Skimmed Oil Pumps (P-5430A/B) suction line Liquid 150 40 150# 0.1 2.1 1.0 1 - 5

Skimmed Oil 2 0 2"-CO-AC-1190-25H-ET 4,550 Skimmed Oil Pumps (P-5430A/B) discharge line Liquid 80 40 150# 0.3 31.7 1.8 23 - 35

Slop Oil 1 0 10"-CO-AC-1124-25H-ET 225,150 Slop Oil Header to Slop Oil Tank (T-5402) Liquid 250 20 150# 1.3 12.1 2 - 3 90.0

Slop Oil 2 0 6"-CO-AC-1182-25H-ET 9,006 Slop Oil Pumps (P-5403A/B) suction line Liquid 150 40 150# 0.1 1.6 1.4 1 - 5

Slop Oil 3 0 3"-CO-AC-1185-25H-ET 9,006 Slop Oil Pumps (P-5403A/B) discharge line Liquid 80 40 150# 0.6 24.1 1.8 23 - 35

PFD Stream No.

Design Flow Rate (kg/h)

Pressure Drop [kPa/100m]

Design Velocity

[m/s]Design Pressure Drop [kPa/100m]

From Inlet Manifold to Surge Vessels (A-1V-5401A~E), ie. inlet header

From Inlet Manifold to Surge Vessels (A-1V-5401A~E), ie. inlet header

From Inlet Header to Surge Vessels (A-1V-5401A~E)

From Surge Vessels (A-1V-5401A~E) to Raw Crude Header

From Surge Vessels (A-1V-5401A~E) to Produced Water Skim Tank (T-5430A/B)

Raw Crude Manifold

Crude-Crude Exchanger 1

From Raw Crude Header to Crude/Crude Exchanger (1~9E-5401)


From Crude/Crude Exchanger (1~9E-5401) to Crude Oil Heater Exchanger (1~9E-5402)

Crude Oil Exchanger

From Crude Oil Heater Exchanger (1~9E-5402A) to Electrostatic Dehydrator (1~9V-5402)

Electrostatic Dehydrator 1

8"-CO-AC-1075-38H, 1125-38H-ET

From Electrostatic Dehydrator (1~9V-5402) to Crude/Crude Exchanger (1~9E-5401), Offspec Oil

Tank (T-5402)


From Electrostatic Dehydrator (1~9V-5402) to Cold Vent Header


From Electrostatic Dehydrator (1~9V-5402) to Produced Water Skim Tank (T-5430A/B)


From Electrostatic Dehydrator (1~9V-5402) to Slop Oil Tank (T-5402)


From Crude/Crude Exchanger (1~9E-5401A/B) to Treated Crude Oil Discharge Manifold

Treated Crude Manifold

From Treated Crude Oil Discharge Manifold to Gas Boot (V-5404)

From Gas Boot (V-5404) to Sales Oil Storage Tanks (T-5401A/B/C/D)

Sales Oil Booster Pump 1

From Sales Oil Storage Tanks (T-5401A/B/C/D) to Sales Oil Header



Sales Oil Booster Pumps (P-5401A/B/C/D) suction line


Sales Oil Booster Pumps (P-5401A/B/C/D) discharge line


Sales Oil Booster Pumps (P-5401A/B/C/D) discharge header


Sales Oil Booster Pumps (P-5401A/B/C/D) minimum flow recycle line


Sales Oil Booster Pumps (P-5401A/B/C/D) minimum flow recycle header

Yo-Yo Operation 1

Yo-Yo Operation 2

From Yo-yo Operation Oil Header to Sales Oil Storage Tanks (T-5401A/B/C/D)

Yo-Yo Operation 2

Off Spec Oil from Treated Crude Oil Manifold to Off Spec Oil Tank (T-5403)

Off Spec Oil Pumps (P-5404A/B) discharge line to Raw Crude Oil Manifold

Off Spec Oil Pumps (P-5404A/B) minimum recycle flow line

Produced Water 1

Produced Water 1

From Produced Water Header to Produced Water Skim Tank (T-5430A/B)

Produced Water 2

From Produced Water Skim Tank (T-5430A/B) to Skimmed Oil Tank (T-5432)

Produced Water 2

From Produced Water Skim Tank (T-5430A/B) to Produced Water Surge Tank (T-5434)

Produced Water 3

Produced Water Transfer Pumps (P-5431A/B) suction line

Produced Water 3

Produced Water Transfer Pumps (P-5431A/B) discharge line

Produced Water 4

Produced Water Transfer Pumps (P-5431A/B) minimum flow recycle line

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls

PIPE ID FOR WELDED & SEAMLESS STEEL PIPESCHEDULE

OUTSIDE STANDARD EXTRA XX SCH SCH SCH SCH SCH SCH SCH SCH SCH SCHDIAMETER STRONG STRONG 10 20 30 40 60 80 100 120 140 160

DN mm25 33.4 26.64 24.3 15.22 - - - 26.64 - 24.3 - - - 22.2850 60.3 52.48 49.22 38.16 - - - 52.48 - 49.22 - - - 42.8280 88.9 77.92 73.66 58.42 - - - 77.92 - 73.66 - - - 66.64

100 114.3 102.26 97.18 80.06 - - - 102.26 - 97.18 - 92.04 - 87.32150 168.3 154.08 146.36 124.4 - - - 154.08 - 146.36 - 139.76 - 131.78200 219.1 202.74 193.7 174.64 - 206.4 205.02 202.74 198.48 193.7 188.92 182.58 177.86 173.08250 273.1 254.56 247.7 222.3 - 260.4 257.5 254.56 247.7 242.92 236.58 230.22 222.3 215.94300 323.9 304.84 298.5 273.1 - 311.2 307.14 303.28 295.36 288.94 281.02 273.1 266.74 257.26350 355.6 336.54 330.2 - 342.9 339.76 336.54 333.34 325.42 317.5 307.94 300.02 292.1 284.18400 406.4 387.34 381 - 393.7 390.56 387.34 381 373.08 363.52 354.02 344.48 333.34 325.42450 457 437.94 431.6 - 444.3 441.16 434.74 428.46 418.9 409.34 398.28 387.14 377.66 366.52500 508 488.94 482.6 - 495.3 488.94 482.6 477.82 466.76 455.62 442.92 431.8 419.1 407.98550 559 539.94 533.6 - 546.3 539.94 533.6 - 514.54 501.84 489.14 476.44 463.74 451.04600 610 590.94 584.6 - 597.3 590.94 581.46 575.04 560.78 548.08 532.22 517.96 505.26 490.92650 660 640.94 634.6 - 644.16 634.6 - - - - - - - -700 711 691.94 685.6 - 695.16 685.6 679.24 - - - - - - -750 762 742.94 736.6 - 746.16 736.6 730.24 - - - - - - -800 813 793.94 787.6 - 797.16 787.6 781.24 778.04 - - - - - -850 864 844.94 838.6 - 848.16 838.6 832.24 829.04 - - - - - -900 914 894.94 888.6 - 898.16 888.6 882.24 875.9 - - - - - -

1050 1067 1047.94 1041.6 - - - - - - - - - - -

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Inlet Manifold 1

CALCULATION SHEET

Calc no (CPF)-CA-PRO-010Project title Melut Basin Oil Development Package A Proj no 4211095Client Petrodar Operating Company Limited Phase/CTR DetailedCalculation title Process Line Sizing Page 4 of 37Activity File

REVISION DATE BY CHECKED APPROVED REVISION DATE BY CHECKED APPROVED

A 6-Sep-04 0 10-Feb-05 PWH

SINGLE PHASE PRESSURE DROP (LIQUID OR GAS)ACCORDING TO CRANE AND CHURCHILL (SI UNITS)Standard Calculation 086/00589-PR-CA-002, Rev. 0, "Issued for Use", 18-Feb-99

INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2101-1)Line Number 24"-CO-CC-1275-38H 24"-CO-CC-1275-38H From Receiver to PY-090 (24"-CO-AC-1000-38H)

Mass & Energy Balance Stream No. 500 500

PROCESS DATA

Phase Liquid Liquid

Temperature, T [C] 45 45

Pressure, P [kPaa] 933 933

Mass Flowrate [kg/h] 2,082,075 720,239 Plant design capacity is 300,000 bbl/d Oil. Heat

Design Margin 0% 0% & Material Balance shows production of

Design Flow [kg/h] 2,082,075 720,239 200,000 bbl/d Oil. Hence, mass flowrate is

Actual Density [kg/m] 921.55 921.90 prorated to plant design capacity.

Actual Viscosity [cP] 672 666

LINE SPECIFICATION

Nominal Diameter [mm] 600 600

Piping Specification CC CC

ANSI Rating 600# 600#

Pipe Schedule 80 80

Pipe Internal Diameter [mm] 548.1 548.1

User Input Pipe ID [mm]

Material of Construction CS CS

Pipe Roughness [mm] 0.046 0.046

OUTPUT

Pipe Cross-sectional Area [m] 0.23593 0.23593

Fluid Velocity [m/s] 2.66 0.92

Reynolds Number 2,000 700

Darcy Friction Factor 0.032 0.091

Pressure Drop [kPa/100m] 19.06 6.51

Velocity Design Range [m/s] 2 - 3 2 - 3

DP Design Range [kPa/100m] 90.0 90.0

CONCLUSIONS

Therefore the recommended line size for 24"-CO-AC-1000-38H is 600 mm NB

REFERENCES

1) Crane, "Flow of Fluids through Valves, Fittings, and Pipe", 1992, Metric Edition - SI Units

2) Churchill S.W., "Friction-factor equation spans all fluid-flow regimes", Chem. Eng., 7-Nov-77

Note: You can copy this worksheet by using Edit/Move or Copy Worksheet

Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Inlet Manifold 2

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2101-1)Line Number 24"-CO-AC-1000-38H 24"-CO-AC-1000-38H From Inlet Manifold too Surge Vessels

Mass & Energy Balance Stream No. 500 500 (A-1V-5401A~E), ie. inlet header

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0% & Material Balance shows plant production of




LINE SPECIFICATION


Piping Specification AC AC


Pipe Schedule STD STD





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Surge Vessel 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2102-1)Line Number 12"-CO-AC-1004-38H 12"-CO-AC-1004-38H From Inlet Header to Surge Vessels

Mass & Energy Balance Stream No. 501B 501B (A-1V-5401A~E)

PROCESS DATA

Phase Liquid Liquid



Mass Flowrate [kg/h] 277,610 96,032

Design Margin 0% 0%

Design Flow [kg/h] 277,610 96,032

Actual Density [kg/m] 921.36 921.72


LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT



Reynolds Number 470 160





CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2102-1)Line Number 12"-CO-AC-1009-38H 12"-CO-AC-1009-38H From Surge Vessels (A-1V-5401A~E) to Raw

Mass & Energy Balance Stream No. 503B 503B Crude Header

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%

Design Flow [kg/h] 277,527 95,965



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 KBW 0 10-Feb-05 PWH GRT


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2102-1)Line Number 4"-PW-AC-2000-25PP 4"-PW-AC-2000-25PP From Surge Vessels (A-1V-5401A~E) to

Mass & Energy Balance Stream No. 504B 504B Produced Water Skim Tank (T-5430A/B)

PROCESS DATA

Phase Liquid Liquid



Mass Flowrate [kg/h] 83 67

Design Margin 0% 0%

Design Flow [kg/h] 39,627 1,734


Actual Viscosity [cP] 0.595 0.595

LINE SPECIFICATION




Pipe Schedule 40 40





OUTPUT



Reynolds Number 230,340 10,080



Velocity Design Range [m/s] 1.5 to 2.1 1.5 to 2.1

DP Design Range [kPa/100m] 6 to 45 6 to 45

CONCLUSIONS

Therefore the recommended line size for 4"-PW-AC-2000-25PP is 100 mm NB

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Raw Crude Manifold

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2106-1)Line Number 24"-CO-AC-1014-38H 24"-CO-AC-1014-38H Raw Crude Header

Mass & Energy Balance Stream No. 503 503

PROCESS DATA

Phase Liquid Liquid








LINE SPECIFICATION









OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Crude-Crude Exchanger 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2106-1)Line Number 8"-CO-AC-1015-38H 8"-CO-AC-1015-38H From Raw Crude Header to Crude/Crude

Mass & Energy Balance Stream No. 503C 503C Exchanger (1~9E-5401)

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%

Design Flow [kg/h] 154,182 53,314



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2107-1)Line Number 8"-CO-AC-1030-38H 8"-CO-AC-1030-38H From Crude/Crude Exchanger (1~9-E-5401)

Mass & Energy Balance Stream No. 505C 505C to Crude Oil Heater (1~9E-5402)

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%

Design Flow [kg/h] 154,182 53,314



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Crude Oil Exchanger

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2108-1)Line Number 8"-CO-AC-1045-38H 8"-CO-AC-1045-38H From Crude Oil Heater (1~9E-5402)

Mass & Energy Balance Stream No. 506C 506C to Electrostatic Dehydrator (1~9V-5402)

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%

Design Flow [kg/h] 154,182 53,314



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Electrostatic Dehydrator 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2112-1)Line Number From Electrostatic Dehydrator (1~9V-5402)

Mass & Energy Balance Stream No. 507C 507C to Crude/Crude Exchanger (1~9E-5401),

PROCESS DATA Offspec Oil Tank (T-5402)

Phase Liquid Liquid




Design Margin 0% 0%

Design Flow [kg/h] 138,371 47,842



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT








CONCLUSIONS

Therefore the recommended line size for 8"-CO-AC-1075-38H, 1125-38H-ET is 200 mm NB

REFERENCES



8"-CO-AC-1075-38H, 1125-38H-ET

8"-CO-AC-1075-38H, 1125-38H-ET


Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2112-1)Line Number Dehydrator Gas Outlet Dehydrator Gas Outlet From Electrostatic Dehydrator (1~9V-5402)

Mass & Energy Balance Stream No. 510C 510C to Cold Vent Header

PROCESS DATA

Phase Vapour Vapour



Mass Flowrate [kg/h] 157 154 HYSYS predicted zero flow through this line.

Design Margin 0% 0% Flowrate (67.97m/hr) is taken from instrument

Design Flow [kg/h] 157 154 datasheet where it was estimated based on

Actual Density [kg/m] 2.31 2.26 fluid velocity of ~10m/s in the 2 inch piping.


LINE SPECIFICATION




Pipe Schedule 40 40





OUTPUT







DP Design Range [kPa/100m] 1 - 3 1 - 3

CONCLUSIONS

Though velocity is high, the line will be normally no flow and the calculated DP is low.

Therefore the selected line size for Dehydrator Gas Outlet is 50 mm NB. Part of vendor scope.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH GRT


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2112-1)Line Number 3"-PW-AC-2005-25PP 3"-PW-AC-2005-25PP From Electrostatic Dehydrator (1~9V-5402)

Mass & Energy Balance Stream No. 512C 512C Produced Water Skim Tank (T-5430A/B)

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%




LINE SPECIFICATION




Pipe Schedule 40 40





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2112-1)Line Number 4"-CO-AC-1109-25H-ET 4"-CO-AC-1109-25H-ET From Electrostatic Dehydrator (1~9V-5402)

Mass & Energy Balance Stream No. 506C 506C to Slop Oil Tank (T-5402)

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%




LINE SPECIFICATION

Nominal Diameter [mm] 100.0 100.0



Pipe Schedule 40 40





OUTPUT








CONCLUSIONS

Assuming 1/3 of the inlet flow to Electrostatic Dehydrator is the interface layer drawn off to slop oil tank. Therefore the

recommended line size for 4"-CO-AC-1109-25H-ET is 100 mm NB

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2107-1)Line Number 8"-CO-AC-1090-38H 8"-CO-AC-1090-38H From Crude/Crude Exchanger (1~9E-5401)

Mass & Energy Balance Stream No. 508C 508C Treated Crude Oil Discharge Manifold

PROCESS DATA

Phase Liquid Liquid




Design Margin 0% 0%

Design Flow [kg/h] 138,371 47,842



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Treated Crude Manifold

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2126-1)Line Number 24"-CO-AC-1105-38H 24"-CO-AC-1105-38H From Treated Crude Oil Discharge Manifold

Mass & Energy Balance Stream No. 508 508 to Gas Boot (V-5404)

PROCESS DATA

Phase Liquid Liquid








LINE SPECIFICATION









OUTPUT








CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Gas Boot 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2126-1)Line Number 24"-CO-AC-1320-38H-ET 24"-CO-AC-1320-38H-ET From Gas Boot (V-5404) to Sales Oil Storage

Mass & Energy Balance Stream No. 514 514 Tanks (T-5401A/B/C/D)

PROCESS DATA

Phase Liquid Liquid








LINE SPECIFICATION









OUTPUT








CONCLUSIONS

Therefore the recommended line size for 24"-CO-AC-1140-38H-ET is 600 mm NB

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Gas Boot 2

CALCULATION SHEET





INPUT Year 2005 Year 2014 (P&ID: JAB-CPF1-PID-2127-1)Line Number 8"-G-A-6067 8"-G-A-6067 Gas Boot (V-5404) to atmosphere

Mass & Energy Balance Stream No. 0

PROCESS DATA

Phase Vapour Vapour

Temperature, T [C] 75 75 Properties from HYSYS model predict zero,

Pressure, P [kPaa] 101 101 Actual flow to be disgned by Gas Boot Vendor

Mass Flowrate [kg/h] 3,593 3,593 Assuming a high rate of 1.5 MMscfd

Design Margin 0% 0%




LINE SPECIFICATION


Piping Specification A A


Pipe Schedule 20 20





OUTPUT






Velocity Design Range [m/s] 20 -40 20 - 40


CONCLUSIONS

Therefore the recommended line size for 8"-G-A-6067 is 200 mm NB

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Sales Oil Booster Pump 1

CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2128-1)Line Number (1) 24"-CO-AC-1148, 1242-38H-ET (2) 32"-CO-AC-1258-38H-ET 1. From Sales Oil Storage Tanks (T-5401A/B/C/D)

Mass & Energy Balance Stream No. 515 515 to Sales Oil Header

PROCESS DATA Sales Oil Storage Tanks (T-5410A/B/C/D) have

Phase Liquid Liquid 2 outlet nozzles on each tank. 3 pumps are

Temperature, T [C] 75 75 online at the same time. Hence, flowrate is

Pressure, P [kPaa] 101 101 half of 3 835m/hr.

Mass Flowrate [kg/h] 1,114,424 2,228,849 2. Sales Oil Header

Design Margin 0% 0% Flowrate is 3 835m/hr.

Design Flow [kg/h] 1,114,424 2,228,849 Properties taken from Sales Oil Booster Pumps

Actual Density [kg/m] 889.76 889.76 (P-5401A/B/C/D) datasheet.


LINE SPECIFICATION




Pipe Schedule STD 20





OUTPUT


Fluid Velocity [m/s] 1.27 1.43 Pump suction




Velocity Design Range [m/s] 1.8 to 5 1.8 to 5


CONCLUSIONS

Therefore the recommended line size for 24"-CO-AC-1148, 1242-38H-ET is 600 mm NB.

Selected size for 32"-CO-AC-1258-38H-ET is 800 mm NB.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2129-1)Line Number (1) 24"-CO-AC-1150-38H-ET (2) 16"-CO-AC-1153-38H-ET 1. Sales Oil Booster Pumps (P-5401A/B/C/D)

Mass & Energy Balance Stream No. 515 515 suction line

PROCESS DATA 2. Sales Oil Booster Pumps (P-5401A/B/C/D)

Phase Liquid Liquid discharge line

Temperature, T [C] 75 75 Pump rated capacity is 835m/hr.

Pressure, P [kPaa] 101 1153 Properties taken from Sales Oil Booster Pumps

Mass Flowrate [kg/h] 742,950 742,950 (P-5401A/B/C/D) datasheet.

Design Margin 0% 0%

Design Flow [kg/h] 742,950 742,950



LINE SPECIFICATION









OUTPUT








CONCLUSIONS

Therefore the recommended line size for 24"-CO-AC-1150-38H-ET is 600 mm NB.


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT 1 2 (P&ID: JAB-CPF1-PID-2129-1)Line Number (1) 24"-CO-AC-1213-38H-ET (2) 10"-CO-AC-1158-38H-ET 1. Sales Oil Booster Pumps (P-5401A/B/C/D)

Mass & Energy Balance Stream No. 515 515 discharge header

PROCESS DATA Flowrate is 3 835m/hr.

Phase Liquid Liquid 2. Sales Oil Booster Pumps (P-5401A/B/C/D)

Temperature, T [C] 75 75 minimum flow recycle line

Pressure, P [kPaa] 1153 1153 Minimum flow is 280m/hr (vendor data).

Mass Flowrate [kg/h] 2,228,849 249,133 Properties taken from Sales Oil Booster Pumps

Design Margin 0% 0% (P-5401A/B/C/D) datasheet.

Design Flow [kg/h] 2,228,849 249,133



LINE SPECIFICATION









OUTPUT






Velocity Design Range [m/s] 5.0 5.0


CONCLUSIONS



REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT (P&ID: JAB-CPF1-PID-2129-1)Line Number 12"-CO-AC-1158-38H-ET Sales Oil Booster Pumps (P-5401A/B/C/D)

Mass & Energy Balance Stream No. 515 minimum flow recycle header

PROCESS DATA

Phase Liquid Liquid Minimum flow is 280m/hr (vendor data).

Temperature, T [C] 75

Pressure, P [kPaa] 1153 Properties taken from Sales Oil Booster Pumps

Mass Flowrate [kg/h] 747,398 (P-5401A/B/C/D) datasheet.

Design Margin 0% 0%

Design Flow [kg/h] 747,398 0

Actual Density [kg/m] 889.76

Actual Viscosity [cP] 59.68

LINE SPECIFICATION

Nominal Diameter [mm] 300



Pipe Schedule 20 20

Pipe Internal Diameter [mm] 311.2




OUTPUT

Pipe Cross-sectional Area [m] 0.07606 #VALUE!

Fluid Velocity [m/s] 3.07 #DIV/0!

Reynolds Number 14,230 #DIV/0!

Darcy Friction Factor 0.029 #DIV/0!

Pressure Drop [kPa/100m] 38.35 #DIV/0!



CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Yo-Yo Operation 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT (P&ID: JAB-CPF1-PID-2130-1)Line Number 8"-CO-AC-1269-25H-ET Pump Station Yo-Yo Operation Oil Header

Mass & Energy Balance Stream No.

PROCESS DATA Yo-Yo Operation capacity is 75m/hr.

Phase Liquid Liquid

Temperature, T [C] 75 Properties taken from Yo-Yo Operation Pumps

Pressure, P [kPaa] 1153 (P-5407) datasheet.

Mass Flowrate [kg/h] 69,225

Design Margin 0% 0%




LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT



Reynolds Number 180 #DIV/0!





CONCLUSIONS

Hence, selected line size for 8"-CO-AC-1269-25H-ET is 200 mm NB.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Yo-Yo Operation 2

CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2130-1)Line Number (1) 4"-CO-AC-1265-25H-ET (2) 8"-CO-AC-1165-38H-ET 1. From Yo-yo Operation Oil Header to Sales Oil

Mass & Energy Balance Stream No. Storage Tanks (T-5401A/B/C/D). Assuming 1

PROCESS DATA Sales Oil Storage Tank is on maintenance, ie.

Phase Liquid Liquid Yo-yo operation oil is fed to 3 storage tanks

Temperature, T [C] 75 75 with 25m/hr each.

Pressure, P [kPaa] 1153 1153 2. From Custody Transfer Metering Skid (A-5401)

Mass Flowrate [kg/h] 22,244 560,549 to Meter Prover Skid (MP-5401)

Design Margin 0% 0%

Design Flow [kg/h] 22,244 560,549

Actual Density [kg/m] 889.76 889.76 Properties taken from Sales Oil Booster Pumps

Actual Viscosity [cP] 59.68 59.68 (P-5401A/B/C/D) datasheet.

LINE SPECIFICATION




Pipe Schedule 40 20





OUTPUT








CONCLUSIONS

Thus, recommended line size for 12"-CO-AC-1216-38H-ET is 100 mm NB.

Though velocity and pressure drop are high, vendor selected line size for 8"-CO-AC-1165-38H-ET is 200 mm NB.

This line is for intermittent operation and the client has already accepted a line size of 8" on the metering skid itself.

REFERENCES



Meter Prover Skid capacity is 560 630 m/hr.


Vapour Criteria

Liquid Criteria

PIPE ID

0

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Off Spec Oil 1

CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2132-1)Line Number (1) 16"-CO-AC-1173-38H-ET (2) 12"-CO-AC-1174-38H-ET 1. Off Spec Oil from Treated Crude Oil Manifold

Mass & Energy Balance Stream No. to Off Spec Oil Tank (T-5403)

PROCESS DATA Flowrate taken from Stream 506C of HMB 9.

Phase Liquid Liquid Properties taken from Off Spec Oil Pumps

Temperature, T [C] 75 75 (P-5404A/B)

Pressure, P [kPaa] 427 101 2. Off Spec Oil Pumps (P-5404A/B) suction line

Mass Flowrate [kg/h] 1,387,638 90,060 Pump rated capacity is 100m/hr.

Design Margin 0% 0% Properties taken from Off Spec Oil Pumps

Design Flow [kg/h] 1,387,638 90,060 (P-5404A/B)



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT






Velocity Design Range [m/s] 2 - 3 1.8

DP Design Range [kPa/100m] 90.0 2 - 7

CONCLUSIONS


Selected line size for 12"-CO-AC-1174-38H-ET is 300 mm NB.

This line is intermittent operation therefore a line velocity slightly higher than guideline is considered acceptable

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Off Spec Oil 2

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT 1 2 (P&ID: JAB-CPF1-PID-2133-1)Line Number (1) 8"-CO-AC-1176-38H-ET (2) 6"-CO-AC-1179-25H-ET 1. Off Spec Oil Pumps (P-5404A/B) discharge

Mass & Energy Balance Stream No. line to raw crude manifold

PROCESS DATA Pump rated capacity is 100m/hr.

Phase Liquid Liquid Properties taken from Off Spec Oil Pumps

Temperature, T [C] 75 75 (P-5404A/B)

Pressure, P [kPaa] 1109 1109 2. Off Spec Oil Pumps (P-5404A/B) minimum

Mass Flowrate [kg/h] 90,060 54,036 flow recycle line.

Design Margin 0% 0% Min recycle flow is 60m/hr (vendor data)

Design Flow [kg/h] 90,060 54,036 Properties taken from Off Spec Oil Pumps

Actual Density [kg/m] 900.60 900.60 (P-5404A/B)


LINE SPECIFICATION




Pipe Schedule 20 40





OUTPUT








CONCLUSIONS


Selected line size for 6"-CO-AC-1179-25H-ET is 150 mm NB.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Produced Water 1

CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2134-1)Line Number (1) 16"-PW-AC-2023-50PP (2) 8"-PW-AC-2024-38PP 1. Produced Water Header

Mass & Energy Balance Stream No. Tank datasheet specified filling rate of

PROCESS DATA 280m/hr. Header flowrate is 280m/hr 2.

Phase Liquid Liquid 2. From Produced Water Header to Produced

Temperature, T [C] 50 50 Water Skim Tank (T-5430A/B)

Pressure, P [kPaa] 101 101 Tank filling rate is 280m/hr.

Mass Flowrate [kg/h] 560,000 280,000 Properties taken from Produced Water Skim

Design Margin 0% 0% Tank (T-5430A/B) datasheet

Design Flow [kg/h] 560,000 280,000



LINE SPECIFICATION




Pipe Schedule 20 20





OUTPUT






Velocity Design Range [m/s] 3.7 to 4.6 2.5 to 3


CONCLUSIONS

Therefore the recommended line size for 16"-PW-AC-2023-50PP is 400 mm NB.


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2134-1)Line Number (1) 4"-CO-AC-1186-25H-ET (2) 8"-PW-AC-2028-50PP 1. From Produced Water Skim Tank (T-5430A/B)

Mass & Energy Balance Stream No. to Skimmed Oil Tank (T-5432)

PROCESS DATA Skimmed Oil Tank (T-5430A/B) filling rate

Phase Liquid Liquid is 15m/hr

Temperature, T [C] 75 50 Properties taken from Skimmed Oil Pump

Pressure, P [kPaa] 101 101 (P-5430A/B)

Mass Flowrate [kg/h] 13,650 280,000 2. From Produced Water Skim Tank (T-5430A/B)

Design Margin 0% 0% Produced Water Surge Tank (T-5434)

Design Flow [kg/h] 13,650 280,000 Tank withdrawal rate is 280m/hr.

Actual Density [kg/m] 910.00 1000.00 Properties taken from Produced Water Skim

Actual Viscosity [cP] 211 1.000 Tank (T-5430A/B) datasheet

LINE SPECIFICATION




Pipe Schedule 40 20





OUTPUT



Reynolds Number 220 479,790



Velocity Design Range [m/s] 1.5 to 2.1 2.5 to 3


CONCLUSIONS



REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET





INPUT 1 2 (P&ID: JAB-CPF1-PID-2134-3)Line Number (1) 8"-PW-AC-2041 (2) 8"-PW-CC-2017 1. Produced Water Transfer Pumps (P-5431A/B)

Mass & Energy Balance Stream No. suction line

PROCESS DATA 2. Produced Water Transfer Pumps (P-5431A/B)

Phase Liquid Liquid discharge line

Temperature, T [C] 50 50 Pump rated capacity is 200m/hr

Pressure, P [kPaa] 101 5229 Properties taken from Produced Water Transfer

Mass Flowrate [kg/h] 197,648 197,648 Pumps (P-5431A/B)

Design Margin 0% 0%

Design Flow [kg/h] 197,648 197,648



LINE SPECIFICATION


Piping Specification AC CC


Pipe Schedule 20 80





OUTPUT








CONCLUSIONS


Therefore the recommended line size for 8"-PW-CC-2017 is 200 mm NB.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID


CALCULATION SHEET





INPUT (P&ID: JAB-CPF1-PID-2134-3)Line Number 3"-PW-CC-2032 4"-PW-CC-2032 Produced Water Transfer Pumps (P-5431A/B)

Mass & Energy Balance Stream No. minimum flow recycle line

PROCESS DATA Pump rated capacity is 200m/hr. Min recycle

Phase Liquid Liquid flow is assumed to be 30% of rated capacity.

Temperature, T [C] 50 50 Properties taken from Produced Water Transfer

Pressure, P [kPaa] 5229 5229 Pumps (P-5431A/B)


Design Margin 0% 0%




LINE SPECIFICATION


Piping Specification CC CC


Pipe Schedule 40 40





OUTPUT








CONCLUSIONS

Selected line size for 3"-PW-CC-2032 is 100 mm NB becausethe calculated DP for 3" line is significantly higher

than the design range.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Skimmed Oil 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT (P&ID: JAB-CPF1-PID-2135-1)Line Number 3"-CO-AC-1188-25H-ET 6"-CO-AC-1188-25H-ET Skimmed Oil Pumps (P-5430A/B) suction line

Mass & Energy Balance Stream No. Pump rated capacity is 5m/hr.

PROCESS DATA Properties taken from Skimmed Oil Pumps

Phase Liquid Liquid (P-5430A/B) datasheet.




Design Margin 0% 0%




LINE SPECIFICATION




Pipe Schedule 40 40





OUTPUT








CONCLUSIONS

DP for 3" line is too high. Thus, selected line size for 3"-CO-AC-1188-25H-ET is 150 mm NB.

REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Skimmed Oil 2

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT (P&ID: JAB-CPF1-PID-2135-1)Line Number 2"-CO-AC-1190-25H-ET Skimmed Oil Pumps (P-5430A/B) discharge line

Mass & Energy Balance Stream No. Pump rated capacity is 5m/hr.

PROCESS DATA Properties taken from Skimmed Oil Pumps

Phase Liquid Liquid (P-5430A/B) datasheet.


Pressure, P [kPaa] 101


Design Margin 0% 0%



Actual Viscosity [cP] 211

LINE SPECIFICATION




Pipe Schedule 40 40





OUTPUT



Reynolds Number 100 #DIV/0!



Velocity Design Range [m/s] 1.8

DP Design Range [kPa/100m] 23 - 35

CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Slop Oil 1

CALCULATION SHEET



A 6-Sep-04 0 10-Feb-05 PWH


INPUT (P&ID: JAB-CPF1-PID-2136-1)Line Number 10"-CO-AC-1124-25H-ET Slop Oil Header to Slop Oil Tank (T-5402)

Mass & Energy Balance Stream No. Slop Oil Tank (T-5402) filling rate is 250m/hr.

PROCESS DATA Properties taken from Slop Oil Pumps (5403A/B)

Phase Liquid Liquid datasheet.


Pressure, P [kPaa] 101


Design Margin 0% 0%




LINE SPECIFICATION

Nominal Diameter [mm] 250.0



Pipe Schedule 20 -





OUTPUT



Reynolds Number 3,900 #DIV/0!



Velocity Design Range [m/s] 2 - 3

DP Design Range [kPa/100m] 90.0

CONCLUSIONS


REFERENCES




Vapour Criteria

Liquid Criteria

PIPE ID

file:///var/www/apps/conversion/tmp/scratch_7/293701781.xls 293701781.xls Slop Oil 2

CALCULATION SHEET





INPUT (P&ID: JAB-CPF1-PID-2136-1)Line Number 4"-CO-AC-1182-25H-ET 6"-CO-AC-1182-25H-ET Slop Oil Pumps (P-5403A/B) suction line

Mass & Energy Balance Stream No. Slop Oil Pumps (P-5403A/B) rated capacity is

PROCESS DATA 10m/hr.

Phase Liquid Liquid Properties taken from Slop Oil Pumps (5403A/B)

Temperature, T [C] 75 75 datasheet.



Design Margin 0% 0%



cpf-010 process line sizing attachment_0.xls

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