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COMPARISON OF LINE PACK CALCULATION USING ASPEN PLUS DYNAMICS AND BY USING MANUAL CALCULATIONS PREPARED BY: MUHAMMAD WAQAS MANZOOR PROCESS ENGINEER Contact: [email protected]

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Page 1: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

COMPARISON OF LINE PACK CALCULATION USING ASPEN PLUS DYNAMICS AND BY USING MANUAL

CALCULATIONSPREPARED BY:

MUHAMMAD WAQAS MANZOOR

PROCESS ENGINEER

Contact: [email protected]

Page 2: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

LINE PACK

• The quantity of natural gas contained in a certain segment of a pipeline is known as line pack.

• It is typically measured in MMSCF.

Page 3: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

CALCULATION USING ASPEN PLUS DYNAMICS

• First of all, build a steady statesimulation of the pipe linesegment, in Aspen PLUS

Page 4: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF PIPE SEGMENT IN ASPEN PLUS

Page 5: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF PIPE SEGMENT IN ASPEN PLUS

Page 6: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF VALVE ‘BV-1’ IN ASPEN PLUS

Page 7: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF VALVE ‘BV-1’ IN ASPEN PLUS

Page 8: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF VALVE ‘BV-2’ IN ASPEN PLUS

Page 9: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF VALVE ‘BV-2’ IN ASPEN PLUS

Page 10: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SPECIFICATIONS OF INLET STREAM ‘NG-1’ IN ASPEN PLUS

Page 11: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

EXPORTING SIMULATION TO ASPEN PLUS DYNAMICS

• After that, set ‘Input mode’ to ‘dynamic’ from ‘steady state’.

Page 12: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

EXPORTING SIMULATION TO ASPEN PLUS DYNAMICS

• After that, click on ‘File Menu’, and select ‘Pressure Driven’ from ‘Update Aspen PLUS Dynamics Menu’.

Page 13: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

EXPORTING SIMULATION TO ASPEN PLUS DYNAMICS

• These 03 files and a folder are created in the same folder where Aspen PLUS ‘.bkp‘ file was previously stored.

Page 14: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

SNAPSHOT OF ASPEN PLUS DYNAMICS WINDOW

Page 15: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

INITIAL BOUNDARY CONDITIONS IN ASPEN PLUS DYNAMICS

Page 16: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

FINAL BOUNDARY CONDITIONS IN ASPEN PLUS DYNAMICS

Page 17: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

CONFIGURATION OF PIPE SEGMENT IN ASPEN PLUS DYNAMICS

Page 18: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

CALCULATION USING ASPEN PLUS DYNAMICS

Page 19: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

CALCULATION OF LINE PACK FROM SIMULATION RESULTS OF ASPEN PLUS DYNAMICS• Molar concentration of gas within the pipe segment = 0.160589 lbmol/cf

• Actual volume of pipe segment = 3.14 x {(14.314/12)^2} /4 x 528000 ft = 590042.558 cf

• Number of Moles of gas contained in the pipe segment = 0.160589 lbmol/cf x 590042.558 cf = 94754.344 lbmol

Calculation of Molar Volume at Standard Conditions:• Molar Volume (Vmn) of any gas at normal conditions i.e. 0 C & 1 atm, is given by,

• Vmn = 22.414 Nm3 / kgmole = 22.414 Nm3 x (1 ft /0.3048 m)^3 x 0.454 kgmol/lbmol

• Vmn = 359.360 Ncf/lbmol

• Molar volume (Vms) at standard conditions i.e. 60 F (15.55 C) and 14.7 psia (1 atm), is given by

• 359.360 cf x 14.7 psi / 492 F = Vms x 14.7 / 520 F

• Or, Vms = 379.811 Scf/lbmol

Calculated Line Pack = 94754.344 lbmol x 379.811 Scf/lbmol = 35.988 MMSCF

Page 20: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

EQUATIONS USED FOR MANUAL CALCULATION OF LINE PACK

• Here Vb represents Line Pack,calculated for a pipe segmenthaving an internal diameter D,length L, and containing naturalgas at an average pressure andtemperature of Pavg, and Tavg,respectively.

• Tb, and Pb represent thr basetemperature and base pressure,respectively.

Ref: ‘Gas Pipeline Hydraulics’ by E. Shashi Menon

Page 21: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

CALCULATION OF COMPRESSIBILITY FACTOR

Ref: ‘Gas Pipeline Hydraulics’ by E. Shashi Menon

Page 22: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

CALCULATION OF AVERAGE PRESSURE AND AVERAGE TEMPERATURE

• Here P1 and P2 are in absolutepressure units.

• Average Temperature istypically calculated by takingarithmetic mean of inlet andout temperatures (in absoluteunits) of the pipe segment.

Ref: ‘Gas Pipeline Hydraulics’ by E. Shashi Menon

Page 23: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

MANUAL CALCULATION OF LINE PACK• Molecular Mass of gas used in Aspen PLUS simulation = 16.0427 lb/lbmol

• Specific gravity of gas = 16.0427 / 29 = 0.5531

• Pressure of gas at Inlet of pipe segment = 898.093 psia

• Pressure of gas at Outlet of pipe segment = 702.895 psia

• Average Pressure of gas across the pipe segment = 898.093 + 702.895 − . × .. .

= 804.460 psia = 789.76 psig (1 atm = 14.7 psia)

• Temperature of gas at Inlet of pipe segment = 74.1135 F = 534.1135 R

• Temperature of gas at Outlet of pipe segment = 63.44 F = 523.44 R

• Average Temperature of gas across the pipe segment = . . = 528.776 R

• Average compressibility of gas across the pipe segment = . × × . × .

. .

= 0.90807

Page 24: Presentation on Calculation of Line Pack of Natural Gas Pipe using Aspen PLUS Dynamics and using Manual Calculations

MANUAL CALCULATION OF LINE PACK• Base Temperature = 60 F = 520 R

• Base Pressure = 14.7 psia

• Internal Diameter of pipe segment = 14.314 inches

• Total Length of pipe segment = 100 miles = 528000 ft

• Line Pack (Vb) calculated using CNGA* method is given by,

• Vb = 28.798 × .

× . . × .

× 14.314 × 100푚푖푙푒푠

• Vb = 34.969 MMSCF

• Line pack calculated using Aspen PLUS Dynamics = 35.988 MMSCF

• The calculated Line Pack ‘Vb’ closely matches with the line pack calculated using Aspen PLUS Dynamics.

• The difference between the two, may be attributed to the difference in physical properties calculationmethods and computational methods in Aspen PLUS Dynamics. However, results of Aspen PLUS Dynamicsare more accurate.

* California Natural Gas Association