31.01 mdea teg therminol stream properties

Simulation Report

Project: MDEA sweetning plant BREMod.pmx

Licensed to USP Trading and Manufacturing Private Limited

Client Name: Multitex

Location: New Delhi

Job: NEEM GAS SKID

ProMax Filename: C:\Users\windows7\Desktop\MDEA sweetning plant BREMod.pmx

ProMax Version: 3.2.11188.0

Simulation Initiated: 1/31/2012 2:37:10 PM

Bryan Research & Engineering, Inc.Chemical Engineering ConsultantsP.O. Box 4747 Bryan, Texas 77805

Office: (979) 776-5220FAX: (979) 776-4818

Report Navigator can be activated via the ProMax Navigator Toolbar.

An asterisk (*), throughout the report, denotes a user specified value.

A question mark (?) after a value, throughout the report, denotes an extrapolated or approximate value.

mailto:[email protected]://www.bre.com/

Bryan Research & Engineering, Inc.

ProMax 3.2®

with

TSWEET & PROSIM® ®

Copyright © BRE Group, Ltd. 2002-2011. All Rights Reserved.

mailto:[email protected]

http://www.bre.com/

1-Sour Feed MDEA Absorber

7

1

2

3

4

5

6

7-Rich AmineMDEA_Flash Drum

10- Flash drum liquid

9-Flash Gas

LR Exchanger

19 MDEA Stripper

10

1

2

5-Sweet Gas to dehydration unit

11-Stripper inlet

NamesStd Vapor Volumetric FlowCO2(Mole Fraction)

Unitsm 3̂/h%

5-Sweet Gas to dehydration unit1.52e+004

0.119

13-Vent Gas2.61e+003

89.7

12-Stripper vapor

MDEA Condensor

13-Vent Gas

14-Reflux back

16-Stripper bottom

MDEA-Reboiler

17-Reboiler vapor

18-Lean Amine

Q-3

Q-Condensor

CompositionCO2(Mole Fraction, Total)

5-Sweet Gas to dehydration unit0.1187 %

Valve

8-Flash Drum inlet

Recycle

6-Recycle 24-Pump outlet 23-Make up outlet

Make up block

21-MDEA

20-Make up inlet

22-Blow down

Q-1

Pump Hp

MDEA Pump

NamesCO2(Mole Fraction)CO2(Mass Flow)

Units%kg/h

1-Sour Feed13.935*4593.7*

5-Sweet Gas to dehydration unit0.1187 33.522

9-Flash Gas65.912 345.81

13-Vent Gas89.72

4357.3

Cross to TEG inlet

3-vapor FEED

4-Heavy liquid

Q-Reboiler MDEA

2-Light liquid

Air side

25-Air n 26-Air out

MDEA-Air Cooler

2 phase seperator

Con-cooler

27-air in Condensor

28-Air out condensor

Reflux Pump15-Reflux

Q- Reflux Pump

Process Streams 1-Sour Feed 2-Light liquid 3-vapor FEEDComposition Status: Solved Solved Solved

From Block: -- 2 phase seperator 2 phase seperator

To Block: 2 phase seperator -- MDEA Absorber

Mole Fraction % % %

Methane 57.5023* 0.0440031 57.5079

Ethane 11.9045* 0.00744175 11.9057

Propane 9.05953* 0.00344060 9.06041

i-Butane 1.26113* 0.000265957 1.26126

n-Butane 3.21113* 0.000957745 3.21144

2,2-Dimethylpropane 0.00483086* 4.59407E-07 0.00483133

i-Pentane 0.701496* 8.27060E-05 0.701565

n-Pentane 0.919256* 0.000132909 0.919346

n-Hexane 0.618814* 3.77057E-05 0.618874

n-Heptane 0.0243401* 6.83768E-07 0.0243425

n-Octane 0.00650307* 1.39844E-07 0.00650371

n-Nonane 0.000836110* 3.51726E-08 0.000836191

n-Decane 0.000557406* 1.24279E-08 0.000557461

Nitrogen 0.419262* 0.000194055 0.419303

CO2 13.9352* 0.177302 13.9365

H2O 0.430318* 99.7661 0.420601

MDEA 0* 0 0

O2 0* 0 0

Mass Flow kg/h kg/h kg/h

Methane 6909.74* 0.000517157 6909.74

Ethane 2681.25* 0.000163932 2681.25

Propane 2992.31* 0.000111147 2992.31

i-Butane 549.045* 1.13246E-05 549.045

n-Butane 1397.99* 4.07812E-05 1397.99

2,2-Dimethylpropane 2.61071* 2.42825E-08 2.61071

i-Pentane 379.105* 4.37153E-06 379.105

n-Pentane 496.788* 7.02506E-06 496.788

n-Hexane 399.437* 2.38045E-06 399.437

n-Heptane 18.2685* 5.01941E-08 18.2685

n-Octane 5.56415* 1.17027E-08 5.56415

n-Nonane 0.803236* 3.30481E-09 0.803236

n-Decane 0.594055* 1.29543E-09 0.594055

Nitrogen 87.9746* 3.98252E-06 87.9746

CO2 4593.71* 0.00571647 4593.71

H2O 58.0679* 1.31672 56.7511

MDEA 0* 0 0

O2 0* 0 0

Process Streams 1-Sour Feed 2-Light liquid 3-vapor FEEDProperties Status: Solved Solved Solved



Property Units

Temperature °C 58.0000000000001* 58.0000000000001 58.0000000000001

Pressure bar 51.0133* 51.0133 51.0133

Mole Fraction Vapor % 99.9902 0 100

Mole Fraction Light Liquid % 0.00978052 100 0

Mole Fraction Heavy Liquid % 0 0 0

Molecular Weight kg/kmol 27.4661 18.0629 27.4671

Mass Density kg/m^3 60.5594 984.505 60.5558

Mass Flow kg/h 20573.3 1.32329 20571.9

Vapor Volumetric Flow m^3/h 339.720 0.00134412 339.719

Liquid Volumetric Flow m^3/h 339.720 0.00134412 339.719

Std Vapor Volumetric Flow m^3/h 17745.1 1.73557 17743.4

Std Liquid Volumetric Flow m^3/h 47.7089 0.00132754 47.7076

Specific Gravity 0.985435 0.948363

Phase: Total

Phase: Total

Enthalpy kcal/h -2.28309E+07 -4957.90 -2.28260E+07

Mass Enthalpy kcal/kg -1109.74 -3746.63 -1109.57

Mass Cp kcal/(kg*°C) 0.531633 1.02001 0.531602

Dynamic Viscosity cP 0.489714 0.0136610

Thermal Conductivity W/(m*°C) 0.639882 0.0352059

Normal Vapor Volumetric Flow Nm^3/h 16789* 1.64205 16787.4

Surface Tension dyne/cm 66.1654




Mole Fraction % %

Methane 57.5079 57.5079

Ethane 11.9057 11.9057

Propane 9.06041 9.06041

i-Butane 1.26126 1.26126

n-Butane 3.21144 3.21144

2,2-Dimethylpropane 0.00483133 0.00483133

i-Pentane 0.701565 0.701565

n-Pentane 0.919346 0.919346

n-Hexane 0.618874 0.618874

n-Heptane 0.0243425 0.0243425

n-Octane 0.00650371 0.00650371

n-Nonane 0.000836191 0.000836191

n-Decane 0.000557461 0.000557461

Nitrogen 0.419303 0.419303

CO2 13.9365 13.9365

H2O 0.420601 0.420601

MDEA 0 0

O2 0 0

Mass Flow kg/h kg/h

Methane 6909.74 6909.74

Ethane 2681.25 2681.25

Propane 2992.31 2992.31

i-Butane 549.045 549.045

n-Butane 1397.99 1397.99

2,2-Dimethylpropane 2.61071 2.61071

i-Pentane 379.105 379.105

n-Pentane 496.788 496.788

n-Hexane 399.437 399.437

n-Heptane 18.2685 18.2685

n-Octane 5.56415 5.56415

n-Nonane 0.803236 0.803236

n-Decane 0.594055 0.594055

Nitrogen 87.9746 87.9746

CO2 4593.71 4593.71

H2O 56.7511 56.7511

MDEA 0 0

O2 0 0




Property Units

Temperature °C 58.0000000000001 58.0000000000001

Pressure bar 51.0133 51.0133

Mole Fraction Vapor % 100 100

Mole Fraction Light Liquid % 0 0

Mole Fraction Heavy Liquid % 0 0

Phase: Vapor

Phase: Vapor

Molecular Weight kg/kmol 27.4671 27.4671

Mass Density kg/m^3 60.5558 60.5558

Mass Flow kg/h 20571.9 20571.9

Vapor Volumetric Flow m^3/h 339.719 339.719

Liquid Volumetric Flow m^3/h 339.719 339.719

Std Vapor Volumetric Flow m^3/h 17743.4 17743.4

Std Liquid Volumetric Flow m^3/h 47.7076 47.7076


Enthalpy kcal/h -2.28260E+07 -2.28260E+07

Mass Enthalpy kcal/kg -1109.57 -1109.57

Mass Cp kcal/(kg*°C) 0.531602 0.531602



Normal Vapor Volumetric Flow Nm^3/h 16787.4 16787.4

Surface Tension dyne/cm




Mole Fraction % %

Methane 0.0440031 0.0440031

Ethane 0.00744175 0.00744175

Propane 0.00344060 0.00344060

i-Butane 0.000265957 0.000265957

n-Butane 0.000957745 0.000957745

2,2-Dimethylpropane 4.59407E-07 4.59407E-07

i-Pentane 8.27060E-05 8.27060E-05

n-Pentane 0.000132909 0.000132909

n-Hexane 3.77057E-05 3.77057E-05

n-Heptane 6.83768E-07 6.83768E-07

n-Octane 1.39844E-07 1.39844E-07

n-Nonane 3.51726E-08 3.51726E-08

n-Decane 1.24279E-08 1.24279E-08

Nitrogen 0.000194055 0.000194055

CO2 0.177302 0.177302

H2O 99.7661 99.7661

MDEA 0 0

O2 0 0

Mass Flow kg/h kg/h

Methane 0.000517157 0.000517157

Ethane 0.000163932 0.000163932

Propane 0.000111147 0.000111147

i-Butane 1.13246E-05 1.13246E-05

n-Butane 4.07812E-05 4.07812E-05

2,2-Dimethylpropane 2.42825E-08 2.42825E-08

i-Pentane 4.37153E-06 4.37153E-06

n-Pentane 7.02506E-06 7.02506E-06

n-Hexane 2.38045E-06 2.38045E-06

n-Heptane 5.01941E-08 5.01941E-08

n-Octane 1.17027E-08 1.17027E-08

n-Nonane 3.30481E-09 3.30481E-09

n-Decane 1.29543E-09 1.29543E-09

Nitrogen 3.98252E-06 3.98252E-06

CO2 0.00571647 0.00571647

H2O 1.31672 1.31672

MDEA 0 0

O2 0 0


Phase: Light Liquid



Property Units

Temperature °C 58.0000000000001 58.0000000000001

Pressure bar 51.0133 51.0133




Molecular Weight kg/kmol 18.0629 18.0629


Mass Flow kg/h 1.32329 1.32329



Std Vapor Volumetric Flow m^3/h 1.73557 1.73557



Enthalpy kcal/h -4957.90 -4957.90

Mass Enthalpy kcal/kg -3746.63 -3746.63

Mass Cp kcal/(kg*°C) 1.02001 1.02001



Normal Vapor Volumetric Flow Nm^3/h 1.64205 1.64205

Surface Tension dyne/cm 66.1654 66.1654

Phase: Light Liquid

4-Heavy liquid 5-Sweet Gas to dehydration unit 6-Recycle 7-Rich Amine 8-Flash Drum inletSolved Solved Solved Solved Solved

2 phase seperator MDEA Absorber MDEA-Air Cooler MDEA Absorber Valve

-- Cross to TEG inlet MDEA Absorber Valve MDEA_Flash Drum

% % % % %

66.7966 0 0.109950 0.109950

13.7885 0 0.0363493 0.0363493

10.5110 0 0.0216573 0.0216573

1.46510 0 0.00236778 0.00236778

3.72611 0 0.00750409 0.00750409

0.00562654 0 4.21856E-06 4.21856E-06

0.817081 0 0.000598363 0.000598363

1.06988 0 0.00106740 0.00106740

0.720312 0 0.000684452 0.000684452

0.0283785 0 1.13329E-05 1.13329E-05

0.00757903 0 4.04457E-06 4.04457E-06

0.000972120 0 1.30596E-06 1.30596E-06

0.000648814 0 6.22548E-07 6.22548E-07

0.488892 0 0.000172415 0.000172415

0.118704 0.00337061 5.45768 5.45768

0.454204 86.8632 81.9703 81.9703

0.000399861 13.1335 12.3917 12.3917

0 0 0 0

kg/h kg/h kg/h kg/h kg/h

0 6876.23 0 33.5080 33.5080

0 2660.49 0 20.7633 20.7633

0 2974.17 0 18.1418 18.1418

0 546.431 0 2.61436 2.61436

0 1389.71 0 8.28555 8.28555

0 2.60493 0 0.00578195 0.00578195

0 378.285 0 0.820116 0.820116

0 495.325 0 1.46298 1.46298

0 398.317 0 1.12049 1.12049

0 18.2470 0 0.0215723 0.0215723

0 5.55537 0 0.00877663 0.00877663

0 0.800055 0 0.00318189 0.00318189

0 0.592372 0 0.00168269 0.00168269

0 87.8829 0 0.0917532 0.0917532

0 33.5224 2.65883 4562.84 4562.84

0 52.5070 28048.7 28053.0 28053.0

0 0.305754 28051.4 28051.1 28051.1

0 0 0 0 0




58.0000000000001 63.7935 ### 84.6623 83.6064

51.0133 50.656 50.656 50.8628 6.8*

100 0 0 0.627535

0 100 100 99.3725

0 0 0 0

24.8110 31.3003 31.9810 31.9810

52.8597 1024.59 1084.58 568.598

0 15921.0 56102.7 60753.7 60753.7

301.193 54.7561 56.0157 106.848

301.193 54.7561 56.0157 106.848

0 15201.9 42462.9 45004.3 45004.3

0 41.8873 55 60.8203 60.8203

0.856657 1.02556 1.08561

0 -1.29412E+07 -1.29660E+08 -1.39544E+08 -1.39544E+08

-812.841 -2311.11 -2296.89 -2296.89

0.600699 0.869221 0.889184 0.880059

0.0128466 2.59016 1.82337

0.0376236 0.354928 0.321862

0 14382.8 40175.0 42579.5 42579.5

54.8253 47.9955?




% %

66.7966 16.7792

13.7885 5.33423

10.5110 3.20021

1.46510 0.352844

3.72611 1.09668

0.00562654 0.000648255

0.817081 0.0918705

1.06988 0.161629

0.720312 0.103036

0.0283785 0.00175553

0.00757903 0.000617450

0.000972120 0.000184135

0.000648814 8.95549E-05

0.488892 0.0272406

0.118704 65.9123

0.454204 6.93549

0.000399861 0.00198378

0 0

kg/h kg/h

6876.23 32.0894

2660.49 19.1210

2974.17 16.8226

546.431 2.44480

1389.71 7.59870

2.60493 0.00557563

378.285 0.790176

495.325 1.39017

398.317 1.05850

18.2470 0.0209703

5.55537 0.00840806

0.800055 0.00281534

0.592372 0.00151900

87.8829 0.0909707

33.5224 345.805

52.5070 14.8949

0.305754 0.0281807

0 0




63.7935 83.6064

50.656 6.8

100 100

0 0

0 0

24.8110 37.0915

52.8597 8.65685

15921.0 442.174

301.193 51.0780

301.193 51.0780

15201.9 282.418

41.8873 0.655175

0.856657 1.28067

-1.29412E+07 -844714

-812.841 -1910.37

0.600699 0.284258

0.0128466 0.0162511

0.0376236 0.0256866

14382.8 267.201




% % %

0 0.109950 0.00468414

0 0.0363493 0.00289332

0 0.0216573 0.00158481

0 0.00236778 0.000154533

0 0.00750409 0.000625996

0 4.21856E-06 1.51482E-07

0 0.000598363 2.19820E-05

0 0.00106740 5.34622E-05

0 0.000684452 3.81050E-05

0 1.13329E-05 3.18277E-07

0 4.04457E-06 1.70925E-07

0 1.30596E-06 1.51395E-07

0 6.22548E-07 6.09423E-08

0 0.000172415 1.47968E-06

0.00337061 5.45768 5.07591

86.8632 81.9703 82.4441

13.1335 12.3917 12.4699

0 0 0

kg/h kg/h kg/h

0 33.5080 1.41856

0 20.7633 1.64234

0 18.1418 1.31923

0 2.61436 0.169554

0 8.28555 0.686849

0 0.00578195 0.000206317

0 0.820116 0.0299394

0 1.46298 0.0728153

0 1.12049 0.0619886

0 0.0215723 0.000602044

0 0.00877663 0.000368577

0 0.00318189 0.000366550

0 0.00168269 0.000163687

0 0.0917532 0.000782493

2.65883 4562.84 4217.04

28048.7 28053.0 28038.1

28051.4 28051.1 28051.0

0 0 0




58.0000000000001 84.6623 83.6064

50.656 50.8628 6.8

0 0 0

100 100 100

0 0 0

31.3003 31.9810 31.9487

1024.59 1084.58 1081.43

56102.7 60753.7 60311.5

54.7561 56.0157 55.7703

54.7561 56.0157 55.7703

42462.9 45004.3 44721.9

55 60.8203 60.1651

1.02556 1.08561 1.08245

-1.29660E+08 -1.39544E+08 -1.38700E+08

-2311.11 -2296.89 -2299.72

0.869221 0.889184 0.884427

2.59016 1.82337 1.83960

0.354928 0.321862 0.324842

40175.0 42579.5 42312.3

54.8253 47.9955? 63.2491?

9-Flash Gas 10- Flash drum liquid 11-Stripper inlet 12-Stripper vapor 13-Vent GasSolved Solved Solved Solved Solved

MDEA_Flash Drum MDEA_Flash Drum LR Exchanger MDEA Stripper MDEA Condensor

-- LR Exchanger MDEA Stripper MDEA Condensor --

% % % % %

16.7792 0.00468414 0.00468414 0.00142211 0.0802609

5.33423 0.00289332 0.00289332 0.000878758 0.0495904

3.20021 0.00158481 0.00158481 0.000480917 0.0271515

0.352844 0.000154533 0.000154533 4.68435E-05 0.00264591

1.09668 0.000625996 0.000625996 0.000189933 0.0107235

0.000648255 1.51482E-07 1.51482E-07 4.58817E-08 2.59268E-06

0.0918705 2.19820E-05 2.19820E-05 6.66047E-06 0.000376315

0.161629 5.34622E-05 5.34622E-05 1.62041E-05 0.000915375

0.103036 3.81050E-05 3.81050E-05 1.15409E-05 0.000652197

0.00175553 3.18277E-07 3.18277E-07 9.63573E-08 5.44632E-06

0.000617450 1.70925E-07 1.70925E-07 5.17430E-08 2.92467E-06

0.000184135 1.51395E-07 1.51395E-07 4.58658E-08 2.59162E-06

8.95549E-05 6.09423E-08 6.09423E-08 1.84551E-08 1.04300E-06

0.0272406 1.47968E-06 1.47968E-06 4.48502E-07 2.53329E-05

65.9123 5.07591 5.07591 1.63723 89.7196

6.93549 82.4441 82.4441 98.3597 10.1081

0.00198378 12.4699 12.4699 8.61515E-06 1.63049E-13

0 0 0 0 0


32.0894 1.41856 1.41856 1.42336 1.42090

19.1210 1.64234 1.64234 1.64854 1.64553

16.8226 1.31923 1.31923 1.32305 1.32123

2.44480 0.169554 0.169554 0.169864 0.169709

7.59870 0.686849 0.686849 0.688737 0.687804

0.00557563 0.000206317 0.000206317 0.000206528 0.000206427

0.790176 0.0299394 0.0299394 0.0299808 0.0299618

1.39017 0.0728153 0.0728153 0.0729399 0.0728812

1.05850 0.0619886 0.0619886 0.0620486 0.0620224

0.0209703 0.000602044 0.000602044 0.000602381 0.000602236

0.00840806 0.000368577 0.000368577 0.000368753 0.000368670

0.00281534 0.000366550 0.000366550 0.000367007 0.000366804

0.00151900 0.000163687 0.000163687 0.000163823 0.000163764

0.0909707 0.000782493 0.000782493 0.000783864 0.000783138

345.805 4217.04 4217.04 4495.38 4357.33

14.8949 28038.1 28038.1 110552 200.954

0.0281807 28051.0 28051.0 0.0640489 2.14409E-11

0 0 0 0 0




83.6064 83.6064 98.8889* 118.103 58.889*

6.8 6.8 6.45526 1.89722 1.89722

100 0 1.94406 100 100

0 100 98.0559 0 0

0 0 0 0 0

37.0915 31.9487 31.9487 18.4412 41.3552

8.65685 1081.43 263.521 1.09029 2.86263

442.174 60311.5 60311.5 115053 4563.70

51.0780 55.7703 228.868 105525 1594.23

51.0780 55.7703 228.868 105525 1594.23

282.418 44721.9 44721.9 147803 2614.33

0.655175 60.1651 60.1651 116.182 5.55235

1.28067 1.08245 0.636724 1.42788

-844714 -1.38700E+08 -1.37406E+08 -3.59477E+08 -9.92217E+06

-1910.37 -2299.72 -2278.27 -3124.44 -2174.15

0.284258 0.884427 0.909609 0.453493 0.222830

0.0162511 1.83960 0.0134645 0.0165345

0.0256866 0.324842 0.0285610 0.0193041

267.201 42312.3 42312.3 139839 2473.47

63.2491?




% % % %

16.7792 0.237075 0.00142211 0.0802609

5.33423 0.144174 0.000878758 0.0495904

3.20021 0.0790619 0.000480917 0.0271515

0.352844 0.00772239 4.68435E-05 0.00264591

1.09668 0.0311574 0.000189933 0.0107235

0.000648255 7.68314E-06 4.58817E-08 2.59268E-06

0.0918705 0.00111750 6.66047E-06 0.000376315

0.161629 0.00270265 1.62041E-05 0.000915375

0.103036 0.00191672 1.15409E-05 0.000652197

0.00175553 1.62076E-05 9.63573E-08 5.44632E-06

0.000617450 8.64094E-06 5.17430E-08 2.92467E-06

0.000184135 7.40988E-06 4.58658E-08 2.59162E-06

8.95549E-05 3.00707E-06 1.84551E-08 1.04300E-06

0.0272406 7.58998E-05 4.48502E-07 2.53329E-05

65.9123 86.3947 1.63723 89.7196

6.93549 13.0942 98.3597 10.1081

0.00198378 0.00604459 8.61515E-06 1.63049E-13

0 0 0 0

kg/h kg/h kg/h kg/h

32.0894 1.39577 1.42336 1.42090

19.1210 1.59097 1.64854 1.64553

16.8226 1.27944 1.32305 1.32123

2.44480 0.164722 0.169864 0.169709

7.59870 0.664599 0.688737 0.687804

0.00557563 0.000203434 0.000206528 0.000206427

0.790176 0.0295892 0.0299808 0.0299618

1.39017 0.0715609 0.0729399 0.0728812

1.05850 0.0606176 0.0620486 0.0620224

0.0209703 0.000596007 0.000602381 0.000602236

0.00840806 0.000362237 0.000368753 0.000368670

0.00281534 0.000348773 0.000367007 0.000366804

0.00151900 0.000157018 0.000163823 0.000163764

0.0909707 0.000780304 0.000783864 0.000783138

345.805 1395.37 4495.38 4357.33

14.8949 86.5720 110552 200.954

0.0281807 0.264340 0.0640489 2.14409E-11

0 0 0 0




83.6064 98.8889 118.103 58.889

6.8 6.45526 1.89722 1.89722

100 100 100 100

0 0 0 0

0 0 0 0

37.0915 40.5314 18.4412 41.3552

8.65685 8.60595 1.09029 2.86263

442.174 1487.47 115053 4563.70

51.0780 172.842 105525 1594.23

51.0780 172.842 105525 1594.23

282.418 869.421 147803 2614.33

0.655175 1.80950 116.182 5.55235

1.28067 1.39944 0.636724 1.42788

-844714 -3.23851E+06 -3.59477E+08 -9.92217E+06

-1910.37 -2177.19 -3124.44 -2174.15

0.284258 0.239667 0.453493 0.222830

0.0162511 0.0182999 0.0134645 0.0165345

0.0256866 0.0229324 0.0285610 0.0193041

267.201 822.576 139839 2473.47




% %

0.00468414 7.67582E-05

0.00289332 9.22972E-05

0.00158481 4.87463E-05

0.000154533 4.49203E-06

0.000625996 2.06809E-05

1.51482E-07 2.15869E-09

2.19820E-05 2.62163E-07

5.34622E-05 9.39297E-07

3.81050E-05 8.59522E-07

3.18277E-07 3.25504E-09

1.70925E-07 2.99838E-09

1.51395E-07 7.48811E-09

6.09423E-08 2.53243E-09

1.47968E-06 4.22285E-09

5.07591 3.46368

82.4441 83.8191

12.4699 12.7170

0 0

kg/h kg/h

1.41856 0.0227938

1.64234 0.0513723

1.31923 0.0397885

0.169554 0.00483287

0.686849 0.0222502

0.000206317 2.88297E-06

0.0299394 0.000350124

0.0728153 0.00125445

0.0619886 0.00137107

0.000602044 6.03744E-06

0.000368577 6.33989E-06

0.000366550 1.77774E-05

0.000163687 6.66972E-06

0.000782493 2.18974E-06

4217.04 2821.67

28038.1 27951.5

28051.0 28050.8

0 0




83.6064 98.8889

6.8 6.45526

0 0

100 100

0 0

31.9487 31.7785

1081.43 1049.94

60311.5 58824.1

55.7703 56.0261

55.7703 56.0261

44721.9 43852.5

60.1651 58.3556

1.08245 1.05093

-1.38700E+08 -1.34167E+08

-2299.72 -2280.82

0.884427 0.926549

1.83960 1.25189

0.324842 0.330843?

42312.3 41489.7

63.2491? 46.9195

14-Reflux back 15-Reflux 16-Stripper bottom 17-Reboiler vapor 18-Lean Amine 19Solved Solved Solved Solved Solved Solved

MDEA Condensor Reflux Pump MDEA Stripper MDEA-Reboiler MDEA-Reboiler LR Exchanger

Reflux Pump MDEA Stripper MDEA-Reboiler MDEA Stripper LR Exchanger Recycle

% % % % % %

2.50898E-06 2.50898E-06 0 0 0 0

1.63504E-06 1.63504E-06 0 0 0 0

6.74157E-07 6.74157E-07 0 0 0 0

4.34832E-08 4.34832E-08 0 0 0 0

2.62030E-07 2.62030E-07 0 0 0 0

2.29197E-11 2.29197E-11 0 0 0 0

4.31176E-09 4.31176E-09 0 0 0 0

1.32838E-08 1.32838E-08 0 0 0 0

4.95313E-09 4.95313E-09 0 0 0 0

2.35046E-11 2.35046E-11 0 0 0 0

1.18539E-11 1.18539E-11 0 0 0 0

2.58272E-11 2.58272E-11 0 0 0 0

6.73006E-12 6.73006E-12 0 0 0 0

4.22581E-10 4.22581E-10 0 0 0 0

0.0511802 0.0511802 0.0198023 0.0237119 0.00337886 0.00337886

99.9488 99.9488 97.3776 99.8883 86.8308 86.8308

8.77028E-06 8.77028E-06 2.60258 0.0879704 13.1658 13.1658

0 0 0 0 0 0

kg/h kg/h kg/h kg/h kg/h kg/h

0.00246676 0.00246676 0 0 0 0

0.00301306 0.00301306 0 0 0 0

0.00182186 0.00182186 0 0 0 0

0.000154890 0.000154890 0 0 0 0

0.000933368 0.000933368 0 0 0 0

1.01344E-07 1.01344E-07 0 0 0 0

1.90653E-05 1.90653E-05 0 0 0 0

5.87367E-05 5.87367E-05 0 0 0 0

2.61591E-05 2.61591E-05 0 0 0 0

1.44340E-07 1.44340E-07 0 0 0 0

8.29839E-08 8.29839E-08 0 0 0 0

2.03007E-07 2.03007E-07 0 0 0 0

5.86850E-08 5.86850E-08 0 0 0 0

7.25497E-07 7.25497E-07 0 0 0 0

138.041 138.041 81.0384 78.3796 2.65876 2.65876

110351 110351 163128 135159 27969.0 27969.0

0.0640489 0.0640489 28838.4 787.345 28051.0 28051.0

0 0 0 0 0 0




58.889 58.8906 123.039 126.029 126.029 102.335

1.89722 2* 2.12406 2.07406 2.07406 1.72932

0 0 0 100 0 0

100 100 100 0 100 100

0 0 0 0 0 0

18.0286 18.0286 20.6529 18.1104 31.3330 31.3330

983.506 983.507 951.996 1.14823 966.365 988.950

110490 110490 192048 136025 56022.7 56022.7

112.343 112.342 201.732 118464 57.9727 56.6487

112.343 112.342 201.732 118464 57.9727 56.6487

145189 145189 220294 177936 42358.1 42358.1

110.629 110.629 191.064 136.144 54.9199 54.9199

0.984435 0.984436 0.952896 0.625304 0.967278 0.989884

-4.14701E+08 -4.14701E+08 -6.25251E+08 -4.28085E+08 -1.25850E+08 -1.27144E+08

-3753.31 -3753.30 -3255.71 -3147.11 -2246.40 -2269.50

1.02208 1.02208 1.05966 0.466217 0.996040 0.953004

0.481944 0.481942 0.294926 0.0135386 0.675749 0.978330

0.645390 0.645391 0.564328 0.0293893 0.342763 0.348770

137366 137366 208424 168348 40075.8 40075.8

66.1239 66.1235 51.4101 44.1145 48.0463




%

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0.0237119

99.8883

0.0879704

0

kg/h

0

0

0

0

0

0

0

0

0

0

0

0

0

0

78.3796

135159

787.345

0




126.029

2.07406

100

0

0

18.1104

1.14823

136025

118464

118464

177936

136.144

0.625304

-4.28085E+08

-3147.11

0.466217

0.0135386

0.0293893

168348




% % % % %

2.50898E-06 2.50898E-06 0 0 0

1.63504E-06 1.63504E-06 0 0 0

6.74157E-07 6.74157E-07 0 0 0

4.34832E-08 4.34832E-08 0 0 0

2.62030E-07 2.62030E-07 0 0 0

2.29197E-11 0 0 0 0

4.31176E-09 0 0 0 0

1.32838E-08 1.32838E-08 0 0 0

4.95313E-09 0 0 0 0

2.35046E-11 0 0 0 0

1.18539E-11 0 0 0 0

2.58272E-11 0 0 0 0

6.73006E-12 0 0 0 0

4.22581E-10 0 0 0 0

0.0511802 0.0511802 0.0198023 0.00337886 0.00337886

99.9488 99.9488 97.3776 86.8308 86.8308

8.77028E-06 8.77028E-06 2.60258 13.1658 13.1658

0 0 0 0 0


0.00246676 0.00246676 0 0 0

0.00301306 0.00301306 0 0 0

0.00182186 0.00182186 0 0 0

0.000154890 0.000154890 0 0 0

0.000933368 0.000933368 0 0 0

1.01344E-07 0 0 0 0

1.90653E-05 0 0 0 0

5.87367E-05 5.87367E-05 0 0 0

2.61591E-05 0 0 0 0

1.44340E-07 0 0 0 0

8.29839E-08 0 0 0 0

2.03007E-07 0 0 0 0

5.86850E-08 0 0 0 0

7.25497E-07 0 0 0 0

138.041 138.041 81.0384 2.65876 2.65876

110351 110351 163128 27969.0 27969.0

0.0640489 0.0640489 28838.4 28051.0 28051.0

0 0 0 0 0




58.889 58.8906 123.039 126.029 102.335

1.89722 2 2.12406 2.07406 1.72932

0 0 0 0 0

100 100 100 100 100

0 0 0 0 0

18.0286 18.0286 20.6529 31.3330 31.3330

983.506 983.507 951.996 966.365 988.950

110490 110490 192048 56022.7 56022.7

112.343 112.342 201.732 57.9727 56.6487

112.343 112.342 201.732 57.9727 56.6487

145189 145189 220294 42358.1 42358.1

110.629 110.629 191.064 54.9199 54.9199

0.984435 0.984436 0.952896 0.967278 0.989884

-4.14701E+08 -4.14701E+08 -6.25251E+08 -1.25850E+08 -1.27144E+08

-3753.31 -3753.30 -3255.71 -2246.40 -2269.50

1.02208 1.02208 1.05966 0.996040 0.953004

0.481944 0.481942 0.294926 0.675749 0.978330

0.645390 0.645391 0.564328 0.342763 0.348770

137366 137366 208424 40075.8 40075.8

66.1239 66.1235 51.4101 44.1145 48.0463

20-Make up inlet 21-MDEA 22-Blow down 23-Make up outlet 24-Pump outlet 25-Air nSolved Solved Solved Solved Solved Solved

Recycle -- Make up block Make up block MDEA Pump --

Make up block Make up block -- MDEA Pump MDEA-Air Cooler Air side

% % % % % %

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 78*

0.00337895 0 0.00337061 0.00337061 0.00337061 0.5*

86.8308 99.9379 86.8632 86.8632 86.8632 0.5*

13.1658 0.0620614 13.1335 13.1335 13.1335 0*

0 0 0 0 0 21*


0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 0*

0 0 0 0 0 3.57975E+06*

2.65883 0 0 2.65883 2.65883 36050.3*

27969.1 79.6108 0 28048.7 28048.7 14757.2*

28051.0 0.327010 0 28051.4 28051.4 0*

0 0 0 0 0 1.10089E+06*




102.335 25* 102.217 103.337 48*

1.72932 2* 1.72932 1.72932 51* 1.01325*

0 0 0 0 100

100 100 100 100 0

0 0 0 0 0

31.3330 18.0781 31.3003 31.3003 31.3003 28.8803

988.949 996.918 989.031 989.427 1.09606

56022.8 79.9378 0 56102.7 56102.7 4.73145E+06

56.6488 0.0801850 56.7250 56.7022 4.31679E+06

56.6488 0.0801850 56.7250 56.7022 4.31679E+06

42358.1 104.755 0 42462.9 42462.9 3.88119E+06

54.9200 0.0800030 0 55* 55 5464.52

0.989884 0.997860 0.989966 0.990362 0.997159

-1.27144E+08 -301954 0 -1.27446E+08 -1.27343E+08 -9.81758E+07

-2269.50 -3777.36 -2269.50 -2271.65 -2269.82 -20.7496

0.953005 0.980317 0.952953 0.951669 0.242617

0.978320 0.923814 0.977999 0.974342 0.0192061

0.348770 0.603890 0.349152 0.348937 0.0273423

40075.9 99.1105 0 40175.0 40175.0 3.67207E+06

48.0463 72.7191 48.0830 47.9779




%

0

0

0

0

0

0

0

0

0

0

0

0

0

78

0.5

0.5

0

21

kg/h

0

0

0

0

0

0

0

0

0

0

0

0

0

3.57975E+06

36050.3

14757.2

0

1.10089E+06




48

1.01325

100

0

0

28.8803

1.09606

4.73145E+06

4.31679E+06

4.31679E+06

3.88119E+06

5464.52

0.997159

-9.81758E+07

-20.7496

0.242617

0.0192061

0.0273423

3.67207E+06




% % % %

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0.00337895 0 0.00337061 0.00337061

86.8308 99.9379 86.8632 86.8632

13.1658 0.0620614 13.1335 13.1335

0 0 0 0

kg/h kg/h kg/h kg/h

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

0 0 0 0

2.65883 0 2.65883 2.65883

27969.1 79.6108 28048.7 28048.7

28051.0 0.327010 28051.4 28051.4

0 0 0 0




102.335 25 102.217 103.337

1.72932 2 1.72932 51

0 0 0 0

100 100 100 100

0 0 0 0

31.3330 18.0781 31.3003 31.3003

988.949 996.918 989.031 989.427

56022.8 79.9378 56102.7 56102.7

56.6488 0.0801850 56.7250 56.7022

56.6488 0.0801850 56.7250 56.7022

42358.1 104.755 42462.9 42462.9

54.9200 0.0800030 55 55

0.989884 0.997860 0.989966 0.990362

-1.27144E+08 -301954 -1.27446E+08 -1.27343E+08

-2269.50 -3777.36 -2271.65 -2269.82

0.953005 0.980317 0.952953 0.951669

0.978320 0.923814 0.977999 0.974342

0.348770 0.603890 0.349152 0.348937

40075.9 99.1105 40175.0 40175.0

48.0463 72.7191 48.0830 47.9779

26-Air out 27-air in Condensor 28-Air out condensorSolved Solved Solved

Air side -- Con-cooler

-- Con-cooler --

% % %

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

78 78* 78

0.5 0.5* 0.5

0.5 0.5* 0.5

0 0* 0

21 21* 21

kg/h kg/h kg/h

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

0 0* 0

3.57975E+06 6.77005E+07* 6.77005E+07

36050.3 681786* 681786

14757.2 279089* 279089

0 0* 0

1.10089E+06 2.08202E+07* 2.08202E+07



-- Con-cooler --

50* 48* 51*

0.91325 1.01325* 1.01049

100 100 100

0 0 0

0 0 0

28.8803 28.8803 28.8803

0.981747 1.09606 1.08294

4.73145E+06 8.94816E+07 8.94816E+07

4.81942E+06 8.16395E+07 8.26286E+07

4.81942E+06 8.16395E+07 8.26286E+07

3.88119E+06 7.34015E+07 7.34015E+07

5464.52 103346 103346

0.997159 0.997159 0.997159

-9.58592E+07 -1.85671E+09 -1.79156E+09

-20.2600 -20.7496 -20.0216

0.242617 0.242617 0.242667

0.0192908 0.0192061 0.0193350

0.0274745 0.0273423 0.0275472

3.67207E+06 6.94466E+07 6.94466E+07



-- Con-cooler --

% % %

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

78 78 78

0.5 0.5 0.5

0.5 0.5 0.5

0 0 0

21 21 21

kg/h kg/h kg/h

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

0 0 0

3.57975E+06 6.77005E+07 6.77005E+07

36050.3 681786 681786

14757.2 279089 279089

0 0 0

1.10089E+06 2.08202E+07 2.08202E+07



-- Con-cooler --

50 48 51

0.91325 1.01325 1.01049

100 100 100

0 0 0

0 0 0

28.8803 28.8803 28.8803

0.981747 1.09606 1.08294

4.73145E+06 8.94816E+07 8.94816E+07

4.81942E+06 8.16395E+07 8.26286E+07

4.81942E+06 8.16395E+07 8.26286E+07

3.88119E+06 7.34015E+07 7.34015E+07

5464.52 103346 103346

0.997159 0.997159 0.997159

-9.58592E+07 -1.85671E+09 -1.79156E+09

-20.2600 -20.7496 -20.0216

0.242617 0.242617 0.242667

0.0192908 0.0192061 0.0193350

0.0274745 0.0273423 0.0275472

3.67207E+06 6.94466E+07 6.94466E+07



-- Con-cooler --



-- Con-cooler --

TEG Reboiler

TEG Condenser

TEG Regenerator

3

1

2

TEG Contactor

3

1

2

Q-Recycle

Q

TEG Recycle

TEG Reflux Coil

Gas/Glycol HEX

TEG Cross Exchanger

TEG Rich Flash

Valve

TEG Pump

17-Reboiler vapor

16-Regenerator bottom

13-overhead vapor

14-Reflux

1-TEG-feed gas

20-TEG

6-Rich TEG 78-Rich Flash in

11-inlet cross exchanger

12- Regenerator inlet

18-Lean TEG

19-to Makeup Tank

22-Makeup outlet23-Pump out245-Recycle

4-Dry Gas 25-Dry Gas

9-Flash Gas

15-Water Vapor

10-Flash Liquid

21-Blowdown

Q-Condenser

Q Reboiler

Q-Reflux Coil

Pump Hp

Basic Glycol Dehydration Unit

TEG Feed Cooler

3-Cool feed

Q-Cooler

Cross to TEG inlet

CompositionH2O(Mole Fraction, Total)

25-Dry Gas0.0023476 %

2-TEG-feed gas

TEG Make up block

26-Propane in

27-Propane out

Q-Reboiler TEG

NamesEnergy Rate

Unitskcal/h

Pump Hp5804.4

Q Reboiler1.7954e+005

Q-Condenser6422.8

Q-Cooler9.3438e+005

Q-Reflux Coil6424.7

Propane side

MULT-1

Process Streams 1-TEG-feed gas 2-TEG-feed gas 3-Cool feed 4-Dry GasComposition Status: Solved Solved Solved Solved

From Block: Cross to TEG inlet MultiplierMixer-O-1 TEG Feed Cooler TEG Contactor

To Block: MultiplierMixer-I-1 TEG Feed Cooler TEG Contactor Gas/Glycol HEX

Mole Fraction % % % %

Methane 66.7969 66.7969 66.7969 67.1607

Ethane 13.7885 13.7885 13.7885 13.8457

Propane 10.5111 10.5111 10.5111 10.5418

i-Butane 1.46511 1.46511 1.46511 1.46892

n-Butane 3.72613 3.72613 3.72613 3.72984

2,2-Dimethylpropane 0.00562656 0.00562656 0.00562656 0.00564072

i-Pentane 0.817084 0.817084 0.817084 0.816157

n-Pentane 1.06989 1.06989 1.06989 1.06696

n-Hexane 0.720315 0.720315 0.720315 0.714833

n-Heptane 0.0283786 0.0283786 0.0283786 0.0278627

n-Octane 0.00757906 0.00757906 0.00757906 0.00736423

n-Nonane 0.000972123 0.000972123 0.000972123 0.000925569

n-Decane 0.000648817 0.000648817 0.000648817 0.000598915

Nitrogen 0.488894 0.488894 0.488894 0.491779

CO2 0.118704 0.118704 0.118704 0.118497

H2O 0.454205 0.454205 0.454205 0.00234763

TEG 0 0 0 1.15395E-05

O2 0 0 0 0

Mass Flow kg/h kg/h kg/h kg/h

Methane 6876.37 13342.4 13342.4 13334.4

Ethane 2660.54 5162.32 5162.32 5152.54

Propane 2974.22 5770.98 5770.98 5753.05

i-Butane 546.441 1060.28 1060.28 1056.64

n-Butane 1389.73 2696.54 2696.54 2682.99


i-Pentane 378.292 734.012 734.012 728.768

n-Pentane 495.334 961.112 961.112 952.720

n-Hexane 398.325 772.881 772.881 762.385

n-Heptane 18.2473 35.4058 35.4058 34.5530

n-Octane 5.55548 10.7795 10.7795 10.4109

n-Nonane 0.800070 1.55240 1.55240 1.46916

n-Decane 0.592383 1.14942 1.14942 1.05463

Nitrogen 87.8845 170.525 170.525 170.499

CO2 33.5231 65.0458 65.0458 64.5418

H2O 52.5080 101.883 101.883 0.523428

TEG 0 0 0 0.0214469

O2 0 0 0 0

Process Streams 1-TEG-feed gas 2-TEG-feed gas 3-Cool feed 4-Dry GasProperties Status: Solved Solved Solved Solved



Property Units

Temperature °C 63.7935 63.7935 30* 20.2820

Pressure bar 50.656 50.656 50.556 50.356

Mole Fraction Vapor % 100 100 91.0708 100

Mole Fraction Light Liquid % 0 0 8.56961 0

Mole Fraction Heavy Liquid % 0 0 0.359590 0

Molecular Weight kg/kmol 24.8106 24.8106 24.8106 24.8151

Mass Density kg/m^3 52.8586 52.8586 65.9378 69.9882

Mass Flow kg/h 15921.0 30891.9 30891.9 30711.6

Vapor Volumetric Flow m^3/h 301.199 584.426 468.502 438.811

Liquid Volumetric Flow m^3/h 301.199 584.426 468.502 438.811

Std Vapor Volumetric Flow m^3/h 15202.2 29497.2 29497.2 29319.7

Std Liquid Volumetric Flow m^3/h 41.8879 81.2763 81.2763 81.0152

Specific Gravity 0.856644 0.856644 0.856797

Phase: Total

Phase: Total

Enthalpy kcal/h -1.29412E+07 -2.51103E+07 -2.60447E+07 -2.55733E+07

Mass Enthalpy kcal/kg -812.842 -812.842 -843.089 -832.692

Mass Cp kcal/(kg*°C) 0.600694 0.600694 0.628419 0.683798

Dynamic Viscosity cP 0.0128465 0.0128465 0.0122417

Thermal Conductivity W/(m*°C) 0.0376236 0.0376236 0.0337663

Normal Vapor Volumetric Flow Nm^3/h 14383.1 27907.9 27907.9 27740.0





Mole Fraction % % % %

Methane 66.7969 66.7969 71.3461 67.1607

Ethane 13.7885 13.7885 13.8009 13.8457

Propane 10.5111 10.5111 9.32647 10.5418

i-Butane 1.46511 1.46511 1.10776 1.46892

n-Butane 3.72613 3.72613 2.55683 3.72984


i-Pentane 0.817084 0.817084 0.422524 0.816157

n-Pentane 1.06989 1.06989 0.499959 1.06696

n-Hexane 0.720315 0.720315 0.177494 0.714833

n-Heptane 0.0283786 0.0283786 0.00393880 0.0278627

n-Octane 0.00757906 0.00757906 0.000490512 0.00736423

n-Nonane 0.000972123 0.000972123 2.57097E-05 0.000925569

n-Decane 0.000648817 0.000648817 9.03928E-06 0.000598915

Nitrogen 0.488894 0.488894 0.530232 0.491779

CO2 0.118704 0.118704 0.123955 0.118497

H2O 0.454205 0.454205 0.0997241 0.00234763

TEG 0 0 0 1.15395E-05

O2 0 0 0 0

Mass Flow kg/h kg/h kg/h kg/h

Methane 6876.37 13342.4 12978.6 13334.4

Ethane 2660.54 5162.32 4705.58 5152.54

Propane 2974.22 5770.98 4663.37 5753.05

i-Butane 546.441 1060.28 730.089 1056.64

n-Butane 1389.73 2696.54 1685.12 2682.99


i-Pentane 378.292 734.012 345.674 728.768

n-Pentane 495.334 961.112 409.025 952.720

n-Hexane 398.325 772.881 173.442 762.385

n-Heptane 18.2473 35.4058 4.47535 34.5530

n-Octane 5.55548 10.7795 0.635347 10.4109

n-Nonane 0.800070 1.55240 0.0373902 1.46916

n-Decane 0.592383 1.14942 0.0145838 1.05463

Nitrogen 87.8845 170.525 168.430 170.499

CO2 33.5231 65.0458 61.8583 64.5418

H2O 52.5080 101.883 20.3717 0.523428

TEG 0 0 0 0.0214469

O2 0 0 0 0




Property Units

Temperature °C 63.7935 63.7935 30 20.2820

Pressure bar 50.656 50.656 50.556 50.356

Mole Fraction Vapor % 100 100 100 100

Mole Fraction Light Liquid % 0 0 0 0

Mole Fraction Heavy Liquid % 0 0 0 0

Phase: Vapor

Phase: Vapor

Molecular Weight kg/kmol 24.8106 24.8106 22.8847 24.8151

Mass Density kg/m^3 52.8586 52.8586 56.5761 69.9882

Mass Flow kg/h 15921.0 30891.9 25949.7 30711.6

Vapor Volumetric Flow m^3/h 301.199 584.426 458.668 438.811

Liquid Volumetric Flow m^3/h 301.199 584.426 458.668 438.811

Std Vapor Volumetric Flow m^3/h 15202.2 29497.2 26863.3 29319.7

Std Liquid Volumetric Flow m^3/h 41.8879 81.2763 71.7161 81.0152

Specific Gravity 0.856644 0.856644 0.790146 0.856797

Enthalpy kcal/h -1.29412E+07 -2.51103E+07 -2.25343E+07 -2.55733E+07

Mass Enthalpy kcal/kg -812.842 -812.842 -868.384 -832.692

Mass Cp kcal/(kg*°C) 0.600694 0.600694 0.619699 0.683798

Dynamic Viscosity cP 0.0128465 0.0128465 0.0122003 0.0122417

Thermal Conductivity W/(m*°C) 0.0376236 0.0376236 0.0349252 0.0337663

Normal Vapor Volumetric Flow Nm^3/h 14383.1 27907.9 25415.9 27740.0





Mole Fraction %

Methane 21.2514

Ethane 14.2353

Propane 23.5407

i-Butane 5.32415

n-Butane 16.3087

2,2-Dimethylpropane 0.0274556

i-Pentane 5.04443

n-Pentane 7.17150

n-Hexane 6.51919

n-Heptane 0.289296

n-Octane 0.0832283

n-Nonane 0.0110706

n-Decane 0.00747507

Nitrogen 0.0700907

CO2 0.0677918

H2O 0.0481723

TEG 0

O2 0

Mass Flow kg/h

Methane 363.770

Ethane 456.726

Propane 1107.60

i-Butane 330.187

n-Butane 1011.42


i-Pentane 388.338

n-Pentane 552.087

n-Hexane 599.439

n-Heptane 30.9305

n-Octane 10.1441

n-Nonane 1.51501

n-Decane 1.13484

Nitrogen 2.09505

CO2 3.18341

H2O 0.925991

TEG 0

O2 0


Phase: Light Liquid



Property Units

Temperature °C 30

Pressure bar 50.556

Mole Fraction Vapor % 0

Mole Fraction Light Liquid % 100

Mole Fraction Heavy Liquid % 0

Molecular Weight kg/kmol 45.5629

Mass Density kg/m^3 498.524

Mass Flow kg/h 4861.61

Vapor Volumetric Flow m^3/h 9.75201

Liquid Volumetric Flow m^3/h 9.75201

Std Vapor Volumetric Flow m^3/h 2527.79

Std Liquid Volumetric Flow m^3/h 9.47924

Specific Gravity 0.498995

Enthalpy kcal/h -3.20546E+06

Mass Enthalpy kcal/kg -659.341

Mass Cp kcal/(kg*°C) 0.669263

Dynamic Viscosity cP 0.102252

Thermal Conductivity W/(m*°C) 0.100643

Normal Vapor Volumetric Flow Nm^3/h 2391.60

Surface Tension dyne/cm 4.67453?




Mole Fraction %

Methane 0.0714359

Ethane 0.0111614

Propane 0.00590194

i-Butane 0.000209109

n-Butane 0.00107665

2,2-Dimethylpropane 5.15841E-07

i-Pentane 8.64938E-05

n-Pentane 9.90455E-05

n-Hexane 1.10764E-05

n-Heptane 1.62621E-07

n-Octane 1.21791E-08

n-Nonane 1.42735E-09

n-Decane 2.72243E-10

Nitrogen 0.000312047

CO2 0.00207582

H2O 99.9076

TEG 0

O2 0

Mass Flow kg/h

Methane 0.0513100

Ethane 0.0150263

Propane 0.0116521

i-Butane 0.000544164

n-Butane 0.00280177

2,2-Dimethylpropane 1.66632E-06

i-Pentane 0.000279402

n-Pentane 0.000319947

n-Hexane 4.27364E-05

n-Heptane 7.29573E-07

n-Octane 6.22881E-08

n-Nonane 8.19634E-09

n-Decane 1.73428E-09

Nitrogen 0.000391381

Phase: Light Liquid

Phase: Heavy Liquid

CO2 0.00409027

H2O 80.5851

TEG 0

O2 0




Property Units

Temperature °C 30

Pressure bar 50.556


Mole Fraction Light Liquid % 0

Mole Fraction Heavy Liquid % 100









Enthalpy kcal/h -304928










Mole Fraction %

Methane 20.3985

Ethane 13.6625

Propane 22.5929

i-Butane 5.10974

n-Butane 15.6520


i-Pentane 4.84129

n-Pentane 6.88270

n-Hexane 6.25665

n-Heptane 0.277645

n-Octane 0.0798766

n-Nonane 0.0106248

n-Decane 0.00717404

Nitrogen 0.0672806

CO2 0.0651454

H2O 4.06964

TEG 0

O2 0

Mass Flow kg/h

Methane 363.822

Ethane 456.741

Propane 1107.61

i-Butane 330.188

n-Butane 1011.42


Phase: Heavy Liquid

Phase: Mixed Liquid

i-Pentane 388.338

n-Pentane 552.087

n-Hexane 599.439

n-Heptane 30.9305

n-Octane 10.1441

n-Nonane 1.51501

n-Decane 1.13484

Nitrogen 2.09544

CO2 3.18750

H2O 81.5111

TEG 0

O2 0




Property Units

Temperature °C 30

Pressure bar 50.556


Mole Fraction Light Liquid % 95.9729

Mole Fraction Heavy Liquid % 4.02712









Enthalpy kcal/h -3.51038E+06







Phase: Mixed Liquid

5-Recycle 6-Rich TEG 7 8-Rich Flash in 9-Flash Gas 10-Flash LiquidSolved Solved Solved Solved Solved Solved

TEG Recycle TEG Contactor TEG Reflux Coil Valve TEG Rich Flash TEG Rich Flash

TEG Contactor TEG Reflux Coil Valve TEG Rich Flash -- --

% % % % % %

7.64313E-09 1.58491 1.58491 1.58491 40.2038 1.14703

1.91561E-07 1.02906 1.02906 1.02906 21.5177 3.60556

1.45720E-06 1.28629 1.28629 1.28629 21.1458 12.2117

4.68703E-07 0.197845 0.197845 0.197845 2.81371 4.06733

4.27910E-06 0.737874 0.737874 0.737874 8.23928 17.8898

4.14730E-09 0.000779193 0.000779193 0.000779193 0.00955542 0.0265095

4.95539E-06 0.229971 0.229971 0.229971 1.73406 9.00141

1.15576E-05 0.368064 0.368064 0.368064 2.31783 15.8272

3.72197E-05 0.385416 0.385416 0.385416 1.29775 30.3542

7.88040E-06 0.0269365 0.0269365 0.0269365 0.0411432 2.80873

8.40831E-06 0.0102157 0.0102157 0.0102157 0.00813093 1.78343

4.81292E-06 0.00205724 0.00205724 0.00205724 0.000728640 0.517674

1.30659E-05 0.00211795 0.00211795 0.00211795 0.000344592 0.695845

0 0.00292592 0.00292592 0.00292592 0.0780322 0.000676738

6.29276E-08 0.0362403 0.0362403 0.0362403 0.503604 0.0361282

7.52534 23.5445 23.5445 23.5445 0.0884903 0.00549724

92.4746 70.5548 70.5548 70.5548 1.87314E-05 0.0213312

0 0 0 0 0 0


2.95652E-08 8.03542 8.03542 8.03542 7.53627 0.00417303

1.38888E-06 9.77897 9.77897 9.77897 7.56019 0.0245865

1.54936E-05 17.9253 17.9253 17.9253 10.8953 0.122117

6.56869E-06 3.63412 3.63412 3.63412 1.91091 0.0536114

5.99700E-05 13.5537 13.5537 13.5537 5.59563 0.235804

7.21495E-08 0.0177667 0.0177667 0.0177667 0.00805557 0.000433746

8.62076E-05 5.24365 5.24365 5.24365 1.46188 0.147280

0.000201065 8.39237 8.39237 8.39237 1.95402 0.258963

0.000773383 10.4965 10.4965 10.4965 1.30675 0.593209

0.000190398 0.853001 0.853001 0.853001 0.0481718 0.0638252

0.000231591 0.368788 0.368788 0.368788 0.0108526 0.0461992

0.000148841 0.0833856 0.0833856 0.0833856 0.00109196 0.0150569

0.000448258 0.0952353 0.0952353 0.0952353 0.000572891 0.0224526

0 0.0259036 0.0259036 0.0259036 0.0255422 4.29924E-06

6.67770E-07 0.504046 0.504046 0.504046 0.258972 0.000360577

32.6894 134.049 134.049 134.049 0.0186275 2.24590E-05

3348.52 3348.50 3348.50 3348.50 3.28686E-05 0.000726462

0 0 0 0 0 0




35 19.0033 22.8340 23.5015 23.5015 23.5015

50.95 50.556 50.506 5.17* 5.17 5.17

0 0 0 3.69731 100 0

100 100 1.91493 0.0717585 0 100

0 0 98.0851 96.2309 0 0

140.228 112.696 112.696 112.696 33.0285 70.0601

1114.09 1094.52 1091.14 418.683 7.24667 618.479

3381.21 3561.56 3561.56 3561.56 38.5928 1.58883

3.03495 3.25400 3.26408 8.50658 5.32559 0.00256893

3.03495 3.25400 3.26408 8.50658 5.32559 0.00256893

571.232 748.696 748.696 748.696 27.6816 0.537252

3 3.26102 3.26102 3.26102 0.0887675 0.00257598

1.11514 1.09555 1.09217 1.14038 0.619063

-4.38511E+06 -4.85648E+06 -4.85005E+06 -4.85005E+06 -26598.0 -925.232

-1296.90 -1363.58 -1361.78 -1361.78 -689.194 -582.337

0.542328 0.549602 0.553564 0.552126 0.439551 0.554954

24.3669 27.8730 27.3918 0.00938537 0.217386

0.195948 0.195546 0.196233 0.0235971 0.112370

540.454 708.356 708.356 708.356 26.1901 0.508305

44.1695 42.8847? 42.9147? 14.5086?




% %

40.2038 40.2038

21.5177 21.5177

21.1458 21.1458

2.81371 2.81371

8.23928 8.23928

0.00955542 0.00955542

1.73406 1.73406

2.31783 2.31783

1.29775 1.29775

0.0411432 0.0411432

0.00813093 0.00813093

0.000728640 0.000728640

0.000344592 0.000344592

0.0780322 0.0780322

0.503604 0.503604

0.0884903 0.0884903

1.87314E-05 1.87314E-05

0 0

kg/h kg/h

7.53627 7.53627

7.56019 7.56019

10.8953 10.8953

1.91091 1.91091

5.59563 5.59563

0.00805557 0.00805557

1.46188 1.46188

1.95402 1.95402

1.30675 1.30675

0.0481718 0.0481718

0.0108526 0.0108526

0.00109196 0.00109196

0.000572891 0.000572891

0.0255422 0.0255422

0.258972 0.258972

0.0186275 0.0186275

3.28686E-05 3.28686E-05

0 0




23.5015 23.5015

5.17 5.17

100 100

0 0

0 0

33.0285 33.0285

7.24667 7.24667

38.5928 38.5928

5.32559 5.32559

5.32559 5.32559

27.6816 27.6816

0.0887675 0.0887675

1.14038 1.14038

-26598.0 -26598.0

-689.194 -689.194

0.439551 0.439551

0.00938537 0.00938537

0.0235971 0.0235971

26.1901 26.1901




% % % % %

7.64313E-09 1.58491 16.3601 1.14703 1.14703

1.91561E-07 1.02906 12.2776 3.60556 3.60556

1.45720E-06 1.28629 20.9423 12.2117 12.2117

4.68703E-07 0.197845 4.56966 4.06733 4.06733

4.27910E-06 0.737874 16.3452 17.8898 17.8898

4.14730E-09 0.000779193 0.0221220 0.0265095 0.0265095

4.95539E-06 0.229971 5.91479 9.00141 9.00141

1.15576E-05 0.368064 9.48713 15.8272 15.8272

3.72197E-05 0.385416 12.4466 30.3542 30.3542

7.88040E-06 0.0269365 0.920110 2.80873 2.80873

8.40831E-06 0.0102157 0.404559 1.78343 1.78343

4.81292E-06 0.00205724 0.0895406 0.517674 0.517674

1.30659E-05 0.00211795 0.0956817 0.695845 0.695845

0 0.00292592 0.0433089 0.000676738 0.000676738

6.29276E-08 0.0362403 0.0712071 0.0361282 0.0361282

7.52534 23.5445 0.00512528 0.00549724 0.00549724

92.4746 70.5548 0.00503976 0.0213312 0.0213312

0 0 0 0 0


2.95652E-08 8.03542 1.58833 0.00417303 0.00417303

1.38888E-06 9.77897 2.23417 0.0245865 0.0245865

1.54936E-05 17.9253 5.58862 0.122117 0.122117

6.56869E-06 3.63412 1.60735 0.0536114 0.0536114

5.99700E-05 13.5537 5.74933 0.235804 0.235804

7.21495E-08 0.0177667 0.00965913 0.000433746 0.000433746

8.62076E-05 5.24365 2.58258 0.147280 0.147280

0.000201065 8.39237 4.14237 0.258963 0.258963

0.000773383 10.4965 6.49110 0.593209 0.593209

0.000190398 0.853001 0.557957 0.0638252 0.0638252

0.000231591 0.368788 0.279667 0.0461992 0.0461992

0.000148841 0.0833856 0.0694991 0.0150569 0.0150569

0.000448258 0.0952353 0.0823878 0.0224526 0.0224526

0 0.0259036 0.00734224 4.29924E-06 4.29924E-06

6.67770E-07 0.504046 0.0189651 0.000360577 0.000360577

32.6894 134.049 0.000558783 2.24590E-05 2.24590E-05

3348.52 3348.50 0.00458022 0.000726462 0.000726462

0 0 0 0 0




35 19.0033 22.8340 23.5015 23.5015

50.95 50.556 50.506 5.17 5.17

0 0 0 0 0

100 100 100 100 100

0 0 0 0 0

140.228 112.696 51.2483 70.0601 70.0601

1114.09 1094.52 547.622 618.479 618.479

3381.21 3561.56 31.0145 1.58883 1.58883

3.03495 3.25400 0.0566348 0.00256893 0.00256893

3.03495 3.25400 0.0566348 0.00256893 0.00256893

571.232 748.696 14.3370 0.537252 0.537252

3 3.26102 0.0572818 0.00257598 0.00257598

1.11514 1.09555 0.548139 0.619063 0.619063

-4.38511E+06 -4.85648E+06 -19786.7 -925.232 -925.232

-1296.90 -1363.58 -637.982 -582.337 -582.337

0.542328 0.549602 0.609307 0.554954 0.554954

24.3669 27.8730 0.137483 0.217386 0.217386

0.195948 0.195546 0.105561 0.112370 0.112370

540.454 708.356 13.5645 0.508305 0.508305

44.1695 42.8847? 6.61604? 14.5086? 14.5086?




% %

1.29645 0.101453

0.809455 0.239943

0.902545 0.515118

0.112493 0.0944544

0.433170 0.436871

0.000362514 0.000422813

0.118985 0.165641

0.190031 0.281624

0.149944 0.328016

0.00949896 0.0243163

0.00251692 0.00897358

0.000349286 0.00172379

0.000291295 0.00166878

0.00213752 4.19229E-05

0.0355576 0.0182837

24.0041 24.4633

71.9321 73.3182

0 0

kg/h kg/h

6.44708 0.494975

7.54479 2.19419

12.3367 6.90794

2.02676 1.66960

7.80433 7.72221

0.00810754 0.00927734

2.66108 3.63449

4.25000 6.17939

4.00543 8.59657

0.295044 0.741004

0.0891208 0.311736

0.0138864 0.0672367

0.0128475 0.0722097

0.0185614 0.000357161

0.485081 0.244713

134.048 134.030

3348.50 3348.50

0 0




22.8340 23.5015

50.506 5.17

0 0

0 0

100 100

113.895 115.789

1100.73 1107.90

3530.54 3521.38

3.20745 3.17841

3.20745 3.17841

734.359 720.477

3.20374 3.16968

1.10177 1.10895

-4.83026E+06 -4.82253E+06

-1368.14 -1369.50

0.553074 0.553358

27.8730 32.2159

0.197834 0.199320

694.791 681.657

43.5557? 44.5132?




% %

1.58491 0.102232

1.02906 0.242451

1.28629 0.523833

0.197845 0.0974148

0.737874 0.449876

0.000779193 0.000442251

0.229971 0.172225

0.368064 0.293208

0.385416 0.350390

0.0269365 0.0263911

0.0102157 0.0102958

0.00205724 0.00210824

0.00211795 0.00218604

0.00292592 4.23959E-05

0.0362403 0.0182970

23.5445 24.4450

70.5548 73.2636

0 0

kg/h kg/h

8.03542 0.499148

9.77897 2.21878

17.9253 7.03006

3.63412 1.72321

13.5537 7.95802

0.0177667 0.00971109

5.24365 3.78177

8.39237 6.43836

10.4965 9.18977

0.853001 0.804829

0.368788 0.357935

0.0833856 0.0822936

0.0952353 0.0946624

0.0259036 0.000361460

0.504046 0.245073

134.049 134.030

3348.50 3348.50

0 0




22.8340 23.5015

50.506 5.17

0 0

1.91493 0.0745135

98.0851 99.9255

112.696 115.754

1091.14 1107.51

3561.56 3522.96

3.26408 3.18098

3.26408 3.18098

748.696 721.014

3.26102 3.17226

1.09217 1.10856

-4.85005E+06 -4.82345E+06

-1361.78 -1369.15

0.553564 0.553359

27.3918 32.1901

0.196233 0.199249

708.356 682.166

42.9147? 44.4890?

11-inlet cross exchanger 12- Regenerator inlet 13-overhead vapor 14-Reflux 15-Water VaporSolved Solved Solved Solved Solved

TEG Rich Flash TEG Cross Exchanger TEG Regenerator TEG Condenser TEG Condenser

TEG Cross Exchanger TEG Regenerator TEG Condenser TEG Regenerator --

% % % % %

0.101453 0.101453 0.445238 8.40540E-06 0.489761

0.239943 0.239943 1.05301 1.93508E-05 1.15831

0.515118 0.515118 2.26064 2.57102E-05 2.48671

0.0944544 0.0944544 0.414522 2.21202E-06 0.455974

0.436871 0.436871 1.91725 2.53000E-05 2.10897

0.000422813 0.000422813 0.00185555 7.79658E-09 0.00204110

0.165641 0.165641 0.726924 4.97272E-06 0.799616

0.281624 0.281624 1.23592 1.00624E-05 1.35951

0.328016 0.328016 1.43947 5.63381E-06 1.58342

0.0243163 0.0243163 0.106702 9.15412E-08 0.117372

0.00897358 0.00897358 0.0393673 7.94286E-08 0.0433040

0.00172379 0.00172379 0.00755621 3.37784E-08 0.00831183

0.00166878 0.00166878 0.00729845 2.03038E-08 0.00802830

4.19229E-05 4.19229E-05 0.000183983 1.95401E-09 0.000202381

0.0182837 0.0182837 0.0802411 1.61726E-05 0.0882636

24.4633 24.4633 90.2567 99.9223 89.2901

73.3182 73.3182 0.00716410 0.0775456 0.000125945

0 0 0 0 0


0.494975 0.494975 0.494976 8.49489E-07 0.494975

2.19419 2.19419 2.19419 3.66561E-06 2.19419

6.90794 6.90794 6.90794 7.14215E-06 6.90793

1.66960 1.66960 1.66959 8.09953E-07 1.66959

7.72221 7.72221 7.72220 9.26383E-06 7.72219

0.00927734 0.00927734 0.00927732 3.54374E-09 0.00927731

3.63449 3.63449 3.63445 2.26023E-06 3.63445

6.17939 6.17939 6.17931 4.57363E-06 6.17931

8.59657 8.59657 8.59622 3.05853E-06 8.59622

0.741004 0.741004 0.740917 5.77858E-08 0.740917

0.311736 0.311736 0.311624 5.71584E-08 0.311624

0.0672367 0.0672367 0.0671583 2.72924E-08 0.0671583

0.0722097 0.0722097 0.0719616 1.81993E-08 0.0719616

0.000357161 0.000357161 0.000357161 3.44843E-10 0.000357161

0.244713 0.244713 0.244717 4.48389E-06 0.244713

134.030 134.030 112.679 11.3405 101.338

3348.50 3348.50 0.0745546 0.0733630 0.00119152

0 0 0 0 0




23.5015 148.44* 101.337 97.8657 97.8657

5.17 4.97 1.048 1.048 1.048

0 1.34048 100 0 100

100 98.6595 0 100 0

0 0 0 0 0

115.789 115.789 21.8762 18.1178 22.2521

1107.90 555.787 0.742098 961.024 0.762015

3521.38 3521.38 151.598 11.4139 140.184

3.17841 6.33584 204.283 0.0118768 183.965

3.17841 6.33584 204.283 0.0118768 183.965

720.477 720.477 164.170 14.9246 149.246

3.16968 3.16968 0.181117 0.0114167 0.169700

1.10895 0.755327 0.961932 0.768304

-4.82253E+06 -4.55416E+06 -376986 -42257.0 -341152

-1369.50 -1293.29 -2486.75 -3702.24 -2433.60

0.553358 0.653936 0.464721 0.980108 0.463999

32.2159 0.0126013 0.289403 0.0124683

0.199320 0.0259729 0.670938? 0.0255732

681.657 681.657 155.325 14.1204 141.204

44.5132? 58.5613




% % %

6.29661 0.445238 0.489761

12.2640 1.05301 1.15831

22.4537 2.26064 2.48671

3.78633 0.414522 0.455974

15.4021 1.91725 2.10897

0.0151070 0.00185555 0.00204110

4.68488 0.726924 0.799616

7.38328 1.23592 1.35951

6.69417 1.43947 1.58342

0.375950 0.106702 0.117372

0.0991412 0.0393673 0.0433040

0.0131185 0.00755621 0.00831183

0.00890272 0.00729845 0.00802830

0.00290073 0.000183983 0.000202381

0.752230 0.0802411 0.0882636

19.6145 90.2567 89.2901

0.153138 0.00716410 0.000125945

0 0 0

kg/h kg/h kg/h

0.411798 0.494976 0.494975

1.50335 2.19419 2.19419

4.03635 6.90794 6.90793

0.897154 1.66959 1.66959

3.64945 7.72220 7.72219

0.00444337 0.00927732 0.00927731

1.37795 3.63445 3.63445

2.17162 6.17931 6.17931

2.35172 8.59622 8.59622

0.153572 0.740917 0.740917

0.0461674 0.311624 0.311624

0.00685909 0.0671583 0.0671583

0.00516390 0.0719616 0.0719616

0.000331268 0.000357161 0.000357161

0.134960 0.244717 0.244713

1.44053 112.679 101.338

0.0937519 0.0745546 0.00119152

0 0 0




148.44 101.337 97.8657

4.97 1.048 1.048

100 100 100

0 0 0

0 0 0

44.8532 21.8762 22.2521

6.53827 0.742098 0.762015

18.2852 151.598 140.184

2.79664 204.283 183.965

2.79664 204.283 183.965

9.65783 164.170 149.246

0.0326144 0.181117 0.169700

1.54866 0.755327 0.768304

-13065.2 -376986 -341152

-714.526 -2486.75 -2433.60

0.532888 0.464721 0.463999

0.0120681 0.0126013 0.0124683

0.0325248 0.0259729 0.0255732

9.13746 155.325 141.204




% % %

0.101453 0.0172802 8.40540E-06

0.239943 0.0765728 1.93508E-05

0.515118 0.217040 2.57102E-05

0.0944544 0.0442933 2.21202E-06

0.436871 0.233540 2.53000E-05

0.000422813 0.000223301 7.79658E-09

0.165641 0.104239 4.97272E-06

0.281624 0.185135 1.00624E-05

0.328016 0.241520 5.63381E-06

0.0243163 0.0195387 9.15412E-08

0.00897358 0.00774848 7.94286E-08

0.00172379 0.00156897 3.37784E-08

0.00166878 0.00157050 2.03038E-08

4.19229E-05 3.08058E-06 1.95401E-09

0.0182837 0.00831161 1.61726E-05

24.4633 24.5291 99.9223

73.3182 74.3123 0.0775456

0 0 0

kg/h kg/h kg/h

0.494975 0.0831776 8.49489E-07

2.19419 0.690844 3.66561E-06

6.90794 2.87159 7.14215E-06

1.66960 0.772441 8.09953E-07

7.72221 4.07276 9.26383E-06

0.00927734 0.00483398 3.54374E-09

3.63449 2.25654 2.26023E-06

6.17939 4.00777 4.57363E-06

8.59657 6.24484 3.05853E-06

0.741004 0.587432 5.77858E-08

0.311736 0.265569 5.71584E-08

0.0672367 0.0603776 2.72924E-08

0.0722097 0.0670458 1.81993E-08

0.000357161 2.58931E-05 3.44843E-10

0.244713 0.109753 4.48389E-06

134.030 132.590 11.3405

3348.50 3348.41 0.0733630

0 0 0




23.5015 148.44 97.8657

5.17 4.97 1.048

0 0 0

100 100 100

0 0 0

115.789 116.752 18.1178

1107.90 989.797 961.024

3521.38 3503.09 11.4139

3.17841 3.53920 0.0118768

3.17841 3.53920 0.0118768

720.477 710.819 14.9246

3.16968 3.13707 0.0114167

1.10895 0.990732 0.961932

-4.82253E+06 -4.54109E+06 -42257.0

-1369.50 -1296.31 -3702.24

0.553358 0.654568 0.980108

32.2159 1.39256 0.289403

0.199320 0.197598? 0.670938?

681.657 672.520 14.1204

44.5132? 35.0335? 58.5613




16-Regenerator bottom 17-Reboiler vapor 18-Lean TEG 19-to Makeup Tank 20-TEGSolved Solved Solved Solved Solved

TEG Regenerator TEG Reboiler TEG Reboiler TEG Cross Exchanger --

TEG Reboiler TEG Regenerator TEG Cross Exchanger TEG Make up block TEG Make up block

% % % % %

9.01284E-07 4.34267E-06 3.30690E-09 3.30690E-09 0*

1.12149E-05 5.38803E-05 8.20099E-08 8.20099E-08 0*

5.85119E-05 0.000280352 6.26210E-07 6.26210E-07 0*

1.59065E-05 7.61000E-05 1.99917E-07 1.99917E-07 0*

0.000123920 0.000591624 1.87952E-06 1.87952E-06 0*

1.15256E-07 5.50081E-07 1.79485E-09 1.79485E-09 0*

0.000102559 0.000487231 2.18534E-06 2.18534E-06 0*

0.000221841 0.00105233 5.13722E-06 5.13722E-06 0*

0.000542778 0.00255843 1.68249E-05 1.68249E-05 0*

8.40478E-05 0.000392372 3.59533E-06 3.59533E-06 0*

7.14243E-05 0.000329522 4.07758E-06 4.07758E-06 0*

3.25824E-05 0.000147733 2.53558E-06 2.53558E-06 0*

6.88406E-05 0.000304943 7.23340E-06 7.23340E-06 0*

5.52729E-11 2.66753E-10 9.03959E-14 9.03959E-14 0*

2.63142E-06 1.26066E-05 2.85621E-08 2.85621E-08 0*

25.1189 92.5418 7.52596 7.52596 6.50316*

74.8797 7.45187 92.4740 92.4740 93.4968*

0 0 0 0 0*


4.39606E-06 4.38327E-06 1.27918E-08 1.27918E-08 0*

0.000102529 0.000101934 5.94599E-07 5.94599E-07 0*

0.000784460 0.000777802 6.65816E-06 6.65816E-06 0*

0.000281091 0.000278289 2.80176E-06 2.80176E-06 0*

0.00218985 0.00216351 2.63408E-05 2.63408E-05 0*

2.52827E-06 2.49704E-06 3.12245E-08 3.12245E-08 0*

0.00224976 0.00221174 3.80177E-05 3.80177E-05 0*

0.00486635 0.00477697 8.93708E-05 8.93708E-05 0*

0.0142212 0.0138716 0.000349602 0.000349602 0*

0.00256055 0.00247369 8.68668E-05 8.68668E-05 0*

0.00248057 0.00236826 0.000112309 0.000112309 0*

0.00127054 0.00119213 7.84134E-05 7.84134E-05 0*

0.00297800 0.00272984 0.000248159 0.000248159 0*

4.70771E-10 4.70160E-10 6.10595E-13 6.10595E-13 0*

3.52101E-05 3.49070E-05 3.03093E-07 3.03093E-07 0*

137.586 104.894 32.6920 32.6920 0.000183495*

3418.91 70.4088 3348.50 3348.50 0.0219911*

0 0 0 0 0*




153.540 204.110 204.110 77.6100 40*

1.148 1.098 1.098 1.048 1.75*

0 100 0 0 0

100 0 100 100 100

0 0 0 0 0

116.975 27.8676 140.227 140.227 141.579

990.337 0.776359 930.655 1069.23 1108.36

3556.53 175.335 3381.19 3381.19 0.0221746

3.59123 225.843 3.63313 3.16227 2.00067E-05

3.59123 225.843 3.63313 3.16227 2.00067E-05

720.285 149.054 571.231 571.231 0.00371049

3.16742 0.167440 2.99998 2.99998 1.96710E-05

0.991273 0.962193 0.931534 1.07024 1.10941

-4.62227E+06 -402841 -4.03989E+06 -4.30826E+06 -28.6462

-1299.66 -2297.55 -1194.81 -1274.18 -1291.85

0.658105 0.503731 0.669175 0.581257 0.546809

1.35467 0.0158521 0.798178 5.86113 19.3895

0.199507? 0.0321958 0.184490? 0.197049 0.195891

681.476 141.023 540.453 540.453 0.00351057

35.1889? 29.4000 40.7219? 43.7499




%

4.34267E-06

5.38803E-05

0.000280352

7.61000E-05

0.000591624

5.50081E-07

0.000487231

0.00105233

0.00255843

0.000392372

0.000329522

0.000147733

0.000304943

2.66753E-10

1.26066E-05

92.5418

7.45187

0

kg/h

4.38327E-06

0.000101934

0.000777802

0.000278289

0.00216351

2.49704E-06

0.00221174

0.00477697

0.0138716

0.00247369

0.00236826

0.00119213

0.00272984

4.70160E-10

3.49070E-05

104.894

70.4088

0




204.110

1.098

100

0

0

27.8676

0.776359

175.335

225.843

225.843

149.054

0.167440

0.962193

-402841

-2297.55

0.503731

0.0158521

0.0321958

141.023




% % % %

9.01284E-07 3.30690E-09 3.30690E-09 0

1.12149E-05 8.20099E-08 8.20099E-08 0

5.85119E-05 6.26210E-07 6.26210E-07 0

1.59065E-05 1.99917E-07 1.99917E-07 0

0.000123920 1.87952E-06 1.87952E-06 0

1.15256E-07 1.79485E-09 1.79485E-09 0

0.000102559 2.18534E-06 2.18534E-06 0

0.000221841 5.13722E-06 5.13722E-06 0

0.000542778 1.68249E-05 1.68249E-05 0

8.40478E-05 3.59533E-06 3.59533E-06 0

7.14243E-05 4.07758E-06 4.07758E-06 0

3.25824E-05 2.53558E-06 2.53558E-06 0

6.88406E-05 7.23340E-06 7.23340E-06 0

5.52729E-11 9.03959E-14 9.03959E-14 0

2.63142E-06 2.85621E-08 2.85621E-08 0

25.1189 7.52596 7.52596 6.50316

74.8797 92.4740 92.4740 93.4968

0 0 0 0

kg/h kg/h kg/h kg/h

4.39606E-06 1.27918E-08 1.27918E-08 0

0.000102529 5.94599E-07 5.94599E-07 0

0.000784460 6.65816E-06 6.65816E-06 0

0.000281091 2.80176E-06 2.80176E-06 0

0.00218985 2.63408E-05 2.63408E-05 0

2.52827E-06 3.12245E-08 3.12245E-08 0

0.00224976 3.80177E-05 3.80177E-05 0

0.00486635 8.93708E-05 8.93708E-05 0

0.0142212 0.000349602 0.000349602 0

0.00256055 8.68668E-05 8.68668E-05 0

0.00248057 0.000112309 0.000112309 0

0.00127054 7.84134E-05 7.84134E-05 0

0.00297800 0.000248159 0.000248159 0

4.70771E-10 6.10595E-13 6.10595E-13 0

3.52101E-05 3.03093E-07 3.03093E-07 0

137.586 32.6920 32.6920 0.000183495

3418.91 3348.50 3348.50 0.0219911

0 0 0 0




153.540 204.110 77.6100 40

1.148 1.098 1.048 1.75

0 0 0 0

100 100 100 100

0 0 0 0

116.975 140.227 140.227 141.579

990.337 930.655 1069.23 1108.36

3556.53 3381.19 3381.19 0.0221746

3.59123 3.63313 3.16227 2.00067E-05

3.59123 3.63313 3.16227 2.00067E-05

720.285 571.231 571.231 0.00371049

3.16742 2.99998 2.99998 1.96710E-05

0.991273 0.931534 1.07024 1.10941

-4.62227E+06 -4.03989E+06 -4.30826E+06 -28.6462

-1299.66 -1194.81 -1274.18 -1291.85

0.658105 0.669175 0.581257 0.546809

1.35467 0.798178 5.86113 19.3895

0.199507? 0.184490? 0.197049 0.195891

681.476 540.453 540.453 0.00351057

35.1889? 29.4000 40.7219? 43.7499




21-Blowdown 22-Makeup outlet 23-Pump out 24 25-Dry Gas 26-Propane inSolved Solved Solved Solved Solved Solved

TEG Make up block TEG Make up block TEG Pump Gas/Glycol HEX Gas/Glycol HEX --

-- TEG Pump Gas/Glycol HEX TEG Recycle -- Propane side

% % % % % %

3.30687E-09 3.30687E-09 3.30687E-09 3.30687E-09 67.1607 0*

8.20094E-08 8.20094E-08 8.20094E-08 8.20094E-08 13.8457 0*

6.26206E-07 6.26206E-07 6.26206E-07 6.26206E-07 10.5418 100*

1.99916E-07 1.99916E-07 1.99916E-07 1.99916E-07 1.46892 0*

1.87951E-06 1.87951E-06 1.87951E-06 1.87951E-06 3.72984 0*

1.79484E-09 1.79484E-09 1.79484E-09 1.79484E-09 0.00564072 0*

2.18532E-06 2.18532E-06 2.18532E-06 2.18532E-06 0.816157 0*

5.13719E-06 5.13719E-06 5.13719E-06 5.13719E-06 1.06696 0*

1.68248E-05 1.68248E-05 1.68248E-05 1.68248E-05 0.714833 0*

3.59531E-06 3.59531E-06 3.59531E-06 3.59531E-06 0.0278627 0*

4.07755E-06 4.07755E-06 4.07755E-06 4.07755E-06 0.00736423 0*

2.53556E-06 2.53556E-06 2.53556E-06 2.53556E-06 0.000925569 0*

7.23335E-06 7.23335E-06 7.23335E-06 7.23335E-06 0.000598915 0*

9.03953E-14 9.03953E-14 9.03953E-14 9.03953E-14 0.491779 0*

2.85620E-08 2.85620E-08 2.85620E-08 2.85620E-08 0.118497 0*

7.52595 7.52595 7.52595 7.52595 0.00234763 0*

92.4740 92.4740 92.4740 92.4740 1.15395E-05 0*

0 0 0 0 0 0*


0 1.27918E-08 1.27918E-08 1.27918E-08 13334.4 0*

0 5.94599E-07 5.94599E-07 5.94599E-07 5152.54 0*

0 6.65816E-06 6.65816E-06 6.65816E-06 5753.05 94088.4*

0 2.80176E-06 2.80176E-06 2.80176E-06 1056.64 0*

0 2.63408E-05 2.63408E-05 2.63408E-05 2682.99 0*

0 3.12245E-08 3.12245E-08 3.12245E-08 5.03675 0*

0 3.80177E-05 3.80177E-05 3.80177E-05 728.768 0*

0 8.93708E-05 8.93708E-05 8.93708E-05 952.720 0*

0 0.000349602 0.000349602 0.000349602 762.385 0*

0 8.68668E-05 8.68668E-05 8.68668E-05 34.5530 0*

0 0.000112309 0.000112309 0.000112309 10.4109 0*

0 7.84134E-05 7.84134E-05 7.84134E-05 1.46916 0*

0 0.000248159 0.000248159 0.000248159 1.05463 0*

0 6.10595E-13 6.10595E-13 6.10595E-13 170.499 0*

0 3.03093E-07 3.03093E-07 3.03093E-07 64.5418 0*

0 32.6922 32.6922 32.6922 0.523428 0*

0 3348.52 3348.52 3348.52 0.0214469 0*

0 0 0 0 0 0*




77.6100 78.4729 35* 34.0465 1.72685

1.048 1.048 51* 50.95 50.256 5*

0 0 0 93.2970 92*

100 100 100 6.70304 8

0 0 0 0 0

140.227 140.227 140.227 140.227 24.8151 44.0956

1069.23 1069.39 1114.09 63.1990 11.7035

0 3381.21 3381.21 3381.21 30711.6 94088.4

3.16229 3.16181 3.03495 485.951 8039.37

3.16229 3.16181 3.03495 485.951 8039.37

0 571.235 571.235 571.235 29319.7 50549.2

0 3* 3 3 81.0152 185.694

1.07024 1.07040 1.11514

0 -4.30829E+06 -4.30248E+06 -4.38512E+06 -2.54907E+07 -5.52233E+07

-1274.18 -1274.18 -1272.47 -1296.91 -830.001 -586.930

0.581257 0.580949 0.542329 0.623228 0.416404

5.86113 5.87844 24.3670

0.197049 0.197044 0.195948

0 540.457 540.457 540.457 27740.0 47825.6

40.7219? 40.6646? 44.1695




% %

70.5145 0

13.8612 0

9.65758 100

1.19242 0

2.80862 0

0.00401543 0

0.490378 0

0.589772 0

0.228484 0

0.00526584 0

0.000678795 0

3.63281E-05 0

1.25150E-05 0

0.522216 0

0.122391 0

0.00243428 0

7.16675E-07 0

0 0

kg/h kg/h

13061.8 0

4812.54 0

4917.20 86561.4

800.248 0

1884.91 0

3.34515 0

408.521 0

491.323 0

227.349 0

6.09254 0

0.895298 0

0.0537986 0

0.0205605 0

168.916 0

62.1941 0

0.506367 0

0.00124271 0

0 0




34.0465 1.72685

50.256 5

100 100

0 0

0 0

23.2501 44.0956

56.1376 10.7863

26845.9 86561.4

478.217 8025.09

478.217 8025.09

27354.4 46505.2

73.5595 170.838

0.802762 1.52250

-2.29731E+07 -5.01770E+07

-855.739 -579.669

0.616297 0.398448

0.0122586 0.00783666

0.0351272 0.0154937

25880.5 43999.5




% % % % %

3.30690E-09 3.30687E-09 3.30687E-09 20.4807 0

8.20099E-08 8.20094E-08 8.20094E-08 13.6302 0

6.26210E-07 6.26206E-07 6.26206E-07 22.8494 100

1.99917E-07 1.99916E-07 1.99916E-07 5.31750 0

1.87952E-06 1.87951E-06 1.87951E-06 16.5519 0

1.79485E-09 1.79484E-09 1.79484E-09 0.0282625 0

2.18534E-06 2.18532E-06 2.18532E-06 5.35055 0

5.13722E-06 5.13719E-06 5.13719E-06 7.70881 0

1.68249E-05 1.68248E-05 1.68248E-05 7.48414 0

3.59533E-06 3.59531E-06 3.59531E-06 0.342379 0

4.07758E-06 4.07755E-06 4.07755E-06 0.100416 0

2.53558E-06 2.53556E-06 2.53556E-06 0.0133026 0

7.23340E-06 7.23335E-06 7.23335E-06 0.00876079 0

9.03959E-14 9.03953E-14 9.03953E-14 0.0681319 0

2.85621E-08 2.85620E-08 2.85620E-08 0.0643038 0

7.52596 7.52595 7.52595 0.00114158 0

92.4740 92.4740 92.4740 0.000162178 0

0 0 0 0 0


1.27918E-08 1.27918E-08 1.27918E-08 272.568 0

5.94603E-07 5.94599E-07 5.94599E-07 340.000 0

6.65820E-06 6.65816E-06 6.65816E-06 835.851 7527.08

2.80177E-06 2.80176E-06 2.80176E-06 256.394 0

2.63410E-05 2.63408E-05 2.63408E-05 798.082 0

3.12247E-08 3.12245E-08 3.12245E-08 1.69160 0

3.80180E-05 3.80177E-05 3.80177E-05 320.247 0

8.93714E-05 8.93708E-05 8.93708E-05 461.397 0

0.000349605 0.000349602 0.000349602 535.036 0

8.68674E-05 8.68668E-05 8.68668E-05 28.4605 0

0.000112310 0.000112309 0.000112309 9.51561 0

7.84140E-05 7.84134E-05 7.84134E-05 1.41536 0

0.000248161 0.000248159 0.000248159 1.03407 0

6.10599E-13 6.10595E-13 6.10595E-13 1.58334 0

3.03095E-07 3.03093E-07 3.03093E-07 2.34769 0

32.6922 32.6922 32.6922 0.0170610 0

3348.52 3348.52 3348.52 0.0202042 0

0 0 0 0 0




77.6100 78.4729 35 34.0465 1.72685

1.048 51 50.95 50.256 5

0 0 0 0 0

100 100 100 100 100

0 0 0 0 0

140.227 140.227 140.227 46.5978 44.0956

1069.23 1069.39 1114.09 499.822 526.965

3381.21 3381.21 3381.21 3865.66 7527.08

3.16229 3.16181 3.03495 7.73407 14.2838

3.16229 3.16181 3.03495 7.73407 14.2838

571.235 571.235 571.235 1965.31 4043.93

3.00000 3 3 7.45570 14.8555

1.07024 1.07040 1.11514 0.500295 0.527463

-4.30828E+06 -4.30248E+06 -4.38512E+06 -2.51753E+06 -5.04638E+06

-1274.18 -1272.47 -1296.91 -651.255 -670.431

0.581257 0.580949 0.542329 0.671365 0.622901

5.86113 5.87844 24.3670 0.102444 0.124710

0.197049 0.197044 0.195948 0.0998408 0.105835

540.457 540.457 540.457 1859.42 3826.04

40.7219? 40.6646? 44.1695 4.68498? 9.69760




27-Propane outSolved

Propane side

--

%

0

0

100

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

kg/h

0

0

94088.4

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Propane side

--

8*

4.8*

100

0

0

44.0956

9.99512

94088.4

9413.44

9413.44

50549.2

185.694

1.52250

-5.42890E+07

-576.999

0.402086

0.00798789

0.0161040

47825.6


Propane side

--

%

0

0

100

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

kg/h

0

0

94088.4

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Propane side

--

8

4.8

100

0

0

44.0956

9.99512

94088.4

9413.44

9413.44

50549.2

185.694

1.52250

-5.42890E+07

-576.999

0.402086

0.00798789

0.0161040

47825.6


Propane side

--


Propane side

--


Propane side

--


Propane side

--

Therminol 55 exchanger TEG

Therminol in TEG

Therminol out TEG

Q-TEG Reboiler

Q-Reboiler TEG

Therminol 55 exchanger MDEA

Q-MDEA Reboiler

Q-Reboiler MDEA

Therminol in MDEATherminol out MDEA

NamesEnergy Rate

Unitskcal/h

Q-MDEA Reboiler7.1316e+007

Q-TEG Reboiler1.7954e+005

NamesTemperaturePressureMass FlowTherminol 55(Mole Fraction)

Units°Cbarkg/h%

Therminol in MDEA200*

2*2.4313e+006

100*

Therminol out MDEA150*1.6

2.4313e+006 100

Therminol in TEG270*

2*4272.6

100*

Therminol out TEG204.2*

1.9 4272.6

100

Process Streams Therminol in MDEA Therminol in TEGComposition Status: Solved Solved

From Block: -- --

To Block: Therminol 55 exchanger MDEA Therminol 55 exchanger TEG

Mole Fraction % %

Therminol 55 100* 100*

Mass Flow kg/h kg/h

Therminol 55 2.43129E+06* 4272.62*

Process Streams Therminol in MDEA Therminol in TEGProperties Status: Solved Solved

From Block: -- --


Property Units

Temperature °C 200* 270*

Pressure bar 2* 2*




Molecular Weight kg/kmol 320 320


Mass Flow kg/h 2.43129E+06 4272.62



Std Vapor Volumetric Flow m^3/h 179995 316.313



Enthalpy kcal/h 1.20019E+08 401384

Mass Enthalpy kcal/kg 49.3644 93.9434

Mass Cp kcal/(kg*°C) 0.607572 0.666325



Normal Vapor Volumetric Flow Nm^3/h 170297 299.270


Process Streams Therminol in MDEA Therminol in TEGComposition Status: Solved Solved

From Block: -- --


Mole Fraction % %

Therminol 55 100 100

Mass Flow kg/h kg/h

Therminol 55 2.43129E+06 4272.62

Process Streams Therminol in MDEA Therminol in TEGProperties Status: Solved Solved

From Block: -- --


Property Units

Temperature °C 200 270

Pressure bar 2 2




Molecular Weight kg/kmol 320 320


Mass Flow kg/h 2.43129E+06 4272.62

Phase: Total

Phase: Total

Phase: Light Liquid

Phase: Light Liquid



Std Vapor Volumetric Flow m^3/h 179995 316.313



Enthalpy kcal/h 1.20019E+08 401384

Mass Enthalpy kcal/kg 49.3644 93.9434

Mass Cp kcal/(kg*°C) 0.607572 0.666325



Normal Vapor Volumetric Flow Nm^3/h 170297 299.270


Therminol out MDEA Therminol out TEGSolved Solved

Therminol 55 exchanger MDEA Therminol 55 exchanger TEG

-- --

% %

100 100

kg/h kg/h

2.43129E+06 4272.62



-- --

150* 204.2*

1.6 1.9

0 0

100 100

0 0

320 320

783.712 745.405

2.43129E+06 4272.62

3102.28 5.73195

3102.28 5.73195

179995 316.313

2779.88 4.88521

0.784453 0.746109

4.87031E+07 221841

20.0318 51.9216

0.565545 0.611098

1.28582 0.736682

0.113241 0.106906

170297 299.270

21.9628 18.0133



-- --

% %

100 100

kg/h kg/h

2.43129E+06 4272.62



-- --

150 204.2

1.6 1.9

0 0

100 100

0 0

320 320

783.712 745.405

2.43129E+06 4272.62

3102.28 5.73195

3102.28 5.73195

179995 316.313

2779.88 4.88521

0.784453 0.746109

4.87031E+07 221841

20.0318 51.9216

0.565545 0.611098

1.28582 0.736682

0.113241 0.106906

170297 299.270

21.9628 18.0133

31.01 mdea teg therminol stream properties

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