New LP New LP

From New Manifold to Manifold to

Stream Number
LP Manifold Separator Separator
(EPF-V-502) Eksisting

Phase Properties 1 2 3
Vapour / Phase Fraction 0.61653554 0.6165355408 0.6165355408
Temperature [F] 90.836077 90.83607695 90.83607695
Pressure [psig] 50 50 50
Molar Flow [MMSCFD] 5.21752212 5.2175221185 0
Overall

Mass Flow [lb/hr] 43440.4248 43440.424792 1.850403E-11

Std Ideal Liq Vol Flow [barrel/day] 4358.2368 4358.2367999 0
Molar Enthalpy [Btu/lbmole] -88067.3138 -88067.31381 -88067.31381
Molar Entropy [Btu/lbmole-F] 37.8621099 37.862109911 37.862109911
Heat Flow [Btu/hr] -50455013 -50455012.97 0
Liq Vol Flow @Std Cond [barrel/day] 4109.00631 4109.0063063 0

Mass Flow [lb/hr] 10893.7495 10893.749538 0

Std. Gas Flow [MMSCFD] 3.21076033 3.2107603324 0
Act. Gas Flow [ACFM] 522.820251 522.82025135 0
Vapour Phase

Mass Density [lb/ft3] 0.34727546 0.3472754615 0.3472754615

Molecular Weight 30.841077 30.841076985 30.841076985
Mass Heat Capacity [Btu/lb-F] 0.41421667 0.4142166735 0.4142166735
Thermal Conductivity [Btu/hr-ft-F] 0.0145483 0.0145482975 0.0145482975
Cp/Cv 1.2092752 1.2092752008 1.2092752008
Viscosity [cP] 0.01106967 0.0110696716 0.0110696716
Z Factor 0.97255611 0.9725561143 0.9725561143

Mass Flow [lb/hr] 32546.6753 32546.675254 0

Liq Vol Flow @Std Cond [barrel/day] 2671.29007 2671.2900708 0
Act. Volume Flow [barrel/day] 2717.10164 2717.1016443 0
Liquid Phase

Mass Density [lb/ft3] 51.2028236 51.202823601 51.202823601

Molecular Weight 148.146631 148.14663068 148.14663068
Mass Heat Capacity [Btu/lb-F] 0.43460491 0.4346049102 0.4346049102
Thermal Conductivity [Btu/hr-ft-F] 0.06406817 0.0640681656 0.0640681656
Viscosity [cP] 1.18235874 1.1823587381 1.1823587381
Surface Tension [dyne/cm] 23.9492211 23.949221101 23.949221101

H2S 0 0 0
CO2 0.08272482 0.0827248241 0.0827248241
Nitrogen 0.00374212 0.0037421159 0.0037421159
Methane 0.2912578 0.2912578006 0.2912578006
Ethane 0.07475388 0.0747538833 0.0747538833
Propane 0.13619725 0.1361972468 0.1361972468
i-Butane 0.02681875 0.0268187525 0.0268187525
n-Butane 0.04081815 0.0408181503 0.0408181503
Composition
 i-Pentane 0.02165688 0.0216568769 0.0216568769

Composition
n-Pentane 0.02083215 0.020832153 0.020832153
n-Hexane 0.01171152 0.0117115163 0.0117115163
n-Heptane 0 0 0
n-Octane 0 0 0
n-Nonane 0 0 0
n-Decane 6.27066E-08 6.270662E-08 6.270662E-08
n-C11 0 0 0
Dodecane* 0 0 0
Heptane* 0.28675121 0.2867512082 0.2867512082
H2O 0.00273541 0.0027354094 0.0027354094
Oxygen 0 0 0
 Inlet LP Gas Outlet LP Liquid Outlet Inlet HP Gas Outlet HP Liquid Outlet Inlet Tank
Separator Separaor (EPF- LP Separaor Scrubber (EPF- Scrubber (EPF- HP Scrubber EPF-T-501
(EPF-V-502) V-502) (EPF-V-502) V-504) V-504) (EPF-V-504) A-H

4 5 6 7 8 9 10
0.6069253368 1 0 0.9732494821 1 0 0.06687
88.800472945 87.636590347 87.636590347 104.03883197 103.80145172 103.80145172 80.74931
50 45 45 450 447 447 0
5.441657871 3.3278369651 2.1138209058 8.3962249371 8.1720891846 0.2241357525 2.113821
45345.302515 11404.141956 33941.160559 24731.342709 22826.464987 1904.8777227 33941.16
4561.0833797 1709.0233709 2852.0600088 4013.0286717 3810.1820919 202.84657983 2852.06
-87826.84243 -55259.78184 -139097.9164 -49829.46699 -48940.84409 -82229.05297 -139098
37.718168747 42.320849219 30.720444591 37.894818556 38.098967948 30.8634788 30.83891
-52478785.51 -20192797.08 -32285988.44 -45940485.45 -43916712.91 -2023772.543-32285988
4304.4109609 587120.64118 2802.4491462 1484098.3348 1445300.2358 195.79091914 2802.449

11264.804782 11404.141956 0 22825.00538 22826.464987 0 702.8572

3.296491606 3.3216013972 0 8.1563099135 8.1567766504 0 0.141086
534.35075458 583.32708271 <empty> 170.09667032 171.26123411 <empty> 100.4976
0.3513551758 0.3258363912 0.3258363912 2.2364757267 2.2214099013 2.2214099013 0.116563
31.062165824 31.208661184 31.208661184 25.437662888 25.437833913 25.437833913 45.28376
0.4136087327 0.4124817419 0.4124817419 0.4991444411 0.4986077792 0.4986077792 0.398316
0.0144150086 0.0143183373 0.0143183373 0.0184476503 0.0184254109 0.0184254109 0.010673
1.2085155199 1.2062317354 1.2062317354 1.3706369056 1.3696624767 1.3696624767 1.131582
0.010997249 0.0109449088 0.0109449088 0.0127047018 0.0126916673 0.0126916673 0.008758
0.9717475936 0.9734955979 0.9734955979 0.8737181333 0.874339007 0.874339007 0.984448

34080.497732 0 33941.160559 1906.3373294 0 1904.8157729 33238.3

2817.4197249 0 2802.4491462 196.02287419 0 195.78822233 2728.449
2863.2977019 0 2846.0369315 204.68480014 0 204.37621291 2759.674
50.878299769 50.97759263 50.97759263 39.811388493 39.839675909 39.839675909 51.48423
145.10227104 146.22885001 146.22885001 77.296184659 77.406424747 77.406424747 153.4628
0.4358277264 0.4346596633 0.4346596633 0.5282030558 0.5278619124 0.5278619124 0.428045
0.064069919 0.0643370806 0.0643370806 0.0540231441 0.0540777055 0.0540777055 0.066121
1.1433285145 1.1740627612 1.1740627612 0.2709287248 0.2719221028 0.2719221028 1.374816
23.564695811 23.81230547 23.81230547 11.2725434 11.304785937 11.304785937 25.42857

0 0 0 0 0 0 0
0.0806663659 0.1279545521 0.0062194846 0.0965154402 3880.6369469 0.0327487495 0.006219
0.0036002224 0.0058694735 2.768817E-05 0.0046895234 120.91009225 0.0002971697 2.769E-05
0.2835759634 0.4592613768 0.0069903684 0.642847012 9466.8758834 0.1047550691 0.00699
0.0733986181 0.1136983868 0.0099537635 0.0653883994 1781.7960982 0.0418502089 0.009954
0.139626256 0.1903091306 0.0598350387 0.126567758 4907.5017311 0.2194481103 0.059835
0.0280483925 0.0306697973 0.0239214544 0.016352526 795.22329629 0.0566724464 0.023921
0.0432118154 0.0411736334 0.0464205723 0.0222670406 1051.71483 0.0989325135 0.046421
0.0232353548 0.0137691149 0.0381382744 0.0072788629 377.6811187 0.0599797976 0.038138
0.0216864229 0.0104442412 0.0393852485 0.0042427469 208.40547089 0.0415724605 0.039385
0.012358362 0.002334692 0.0281388566 0.0015442094 64.542669739 0.0274158956 0.028139
0.0024572649 0.0001652369 0.0060656574 0.0023130843 66.564116207 0.0596584642 0.006066
0.0033358593 7.620319E-05 0.0084676111 0.0025639513 42.332602266 0.0809893332 0.008468
0.001882113 1.510438E-05 0.0048213876 0.0013165621 11.440612179 0.0456946952 0.004821
0.0013657929 4.013347E-06 0.0035096739 0.000915948 4.0411516754 0.03315781 0.00351
0.0009038943 9.194702E-07 0.0023254683 0.0005945126 1.2526061354 0.0219451087 0.002325
0.0030375606 1.423851E-06 0.0078174207 0.0019818241 2.5232198595 0.073747117 0.007817
0.2749402493 3.299508E-05 0.7077330748 0 0 0 0.707733
0.0026694924 0.0042197051 0.0002289567 0.0026205988 43.022540756 0.0011350507 0.000229
0 0 0 0 0 0 0
 Liquid
Outlet Tank
(EPF-T-501
A-H) to
Pump

11
0
80.7493094
0
1.9724698
33238.3033
2760.40523
-145001.85
30.0022405
-31405750
2728.44903

0
0
<empty>
0.11656298
45.2837595
0.39831568
0.01067254
1.13158196
0.00875781
0.98444798

33238.3033
2728.44903
2759.67425
51.4842263
153.462776
0.42804518
0.06612104
1.3748159
25.4285696

0
0.0010093
4.662E-07
0.00037836
0.00260933
0.03515231
0.01938949
0.04076943
0.03759985
0.03970071
0.02959379
0.00646164
0.00905721
0.00516361
0.00376034
0.00249193
0.00837734
0.7584444
4.0481E-05
0
 New LP
Gas Outlet LP
From New Manifold to
Stream Number Separaor (EPF-
LP Manifold Separator
V-502)
(EPF-V-502)

Phase Properties 1 2 3
Vapour / Phase Fraction 0.61653554 0.6165316155 1
Temperature [F] 90.836077 90.835000465 89.732500207
Pressure [psig] 50 50 45
Molar Flow [MMSCFD] 5.21752212 5.2176145342 3.2395323322
Overall

Mass Flow [lb/hr] 43440.4248 43441.193122 11019.848891

Std Ideal Liq Vol Flow [barrel/day] 4358.2368 4358.318648 1656.1048572
Molar Enthalpy [Btu/lbmole] -88067.3138 -88067.2188 -55299.02463
Molar Entropy [Btu/lbmole-F] 37.8621099 37.862122065 42.402566516
Heat Flow [Btu/hr] -50455013 -50455852.22 -19670937.72
Liq Vol Flow @Std Cond [barrel/day] 4109.00631 4109.0355814 571618.60334

Mass Flow [lb/hr] 10893.7495 10893.902843 11019.848891

Std. Gas Flow [MMSCFD] 3.21076033 3.2107967611 3.233462226
Act. Gas Flow [ACFM] 522.820251 522.82496671 570.4797505
Vapour Phase

Mass Density [lb/ft3] 0.34727546 0.3472772165 0.3219471008

Molecular Weight 30.841077 30.841161085 30.97903503
Mass Heat Capacity [Btu/lb-F] 0.41421667 0.4142163486 0.4131305159
Thermal Conductivity [Btu/hr-ft-F] 0.0145483 0.0145482319 0.0144556694
Cp/Cv 1.2092752 1.2092753096 1.2070420159
Viscosity [cP] 0.01106967 0.0110696364 0.0110197546
Z Factor 0.97255611 0.9725557532 0.9742756628

Mass Flow [lb/hr] 32546.6753 32547.29028 0

Liq Vol Flow @Std Cond [barrel/day] 2671.29007 2671.2884888 0
Act. Volume Flow [barrel/day] 2717.10164 2717.0988965 0
Liquid Phase

Mass Density [lb/ft3] 51.2028236 51.203842949 51.298288884

Molecular Weight 148.146631 148.14528965 149.26612108
Mass Heat Capacity [Btu/lb-F] 0.43460491 0.4346053163 0.4334981259
Thermal Conductivity [Btu/hr-ft-F] 0.06406817 0.064068175 0.0643191815
Viscosity [cP] 1.18235874 1.182360684 1.2134988899
Surface Tension [dyne/cm] 23.9492211 23.949063632 24.191602759

Mass Flow [lb/hr] - - -

Liq Vol Flow @Std Cond [barrel/day] - - -
Act. Volume Flow [barrel/day] - - -
Aqueous Phase

Mass Density [lb/ft3] - - -

Molecular Weight - - -
Mass Heat Capacity [Btu/lb-F] - - -
Thermal Conductivity [Btu/hr-ft-F] - - -
Viscosity [cP] - - -
Aqueou
Surface Tension [dyne/cm] - - -

H2S 0 0 0
CO2 0.08272482 0.0827248241 0.1279545521
Nitrogen 0.00374212 0.0037421159 0.0058694735
Methane 0.2912578 0.2912578006 0.4592613768
Ethane 0.07475388 0.0747538833 0.1136983868
Propane 0.13619725 0.1361972468 0.1903091306
i-Butane 0.02681875 0.0268187525 0.0306697973
n-Butane 0.04081815 0.0408181503 0.0411736334
i-Pentane 0.02165688 0.0216568769 0.0137691149
Composition

n-Pentane 0.02083215 0.020832153 0.0104442412

n-Hexane 0.01171152 0.0117115163 0.002334692
n-Heptane 0 0 0.0001652369
n-Octane 0 0 7.620319E-05
n-Nonane 0 0 1.510438E-05
n-Decane 6.27066E-08 6.270662E-08 4.013347E-06
n-C11 0 0 9.194702E-07
Dodecane* 0 0 1.423851E-06
Heptane* 0.28675121 0.2867512082 3.299508E-05
H2O 0.00273541 0.0027354094 0.0042197051
Oxygen 0 0 0
Liquid Outlet Inlet HP Gas Outlet HP Liquid Outlet Inlet Tank
LP Separaor Scrubber (EPF- Scrubber (EPF- HP Scrubber EPF-T-501
(EPF-V-502) V-504) V-504) (EPF-V-504) A-H

4 5 6 7 8
0 0.9998092921 1 0 0.0628
89.732500207 103.70907204 103.46737302 103.46737302 83.48424
45 450 447 447 0
1.978082202 0.4628522182 0.4627598025 9.241571E-05 1.978082
32421.344231 1293.4376101 1292.6692799 0.7683301522 32421.34
2702.2137907 215.86005519 215.77820709 0.081848097 2702.214
-141732.1395 -48930.292 -48923.54741 -82702.97007 -141732
30.684675668 38.078130312 38.09091486 30.382970656 30.79923
-30784914.5 -2486826.178 -2485986.926 -839.2515846-30784915
2657.8539822 81858.716105 81842.699881 0.0789339906 2657.854

0 1292.6924676 1292.6692799 0 613.5164

0 0.46189684 0.4618927017 0 0.12399
<empty> 9.6236987001 9.6889142797 <empty> 88.81005
0.3219471008 2.2387330633 2.2236243802 2.2236243802 0.115137
30.97903503 25.439599232 25.439370834 25.439370834 44.97799
0.4131305159 0.4992147494 0.4986763851 0.4986763851 0.39922
0.0144556694 0.0184358811 0.0184136341 0.0184136341 0.010809
1.2070420159 1.3710857995 1.3701122243 1.3701122243 1.132031
0.0110197546 0.0126988825 0.0126858172 0.0126858172 0.00885
0.9742756628 0.8734145285 0.8740392503 0.8740392503 0.98493

32421.344231 0.745142489 0 0.7645435587 31807.83

2657.8539822 0.076775517 0 0.0787701523 2593.896
2701.601595 0.0801584843 0 0.0822169987 2626.931
51.298288884 39.735894812 39.749693166 39.749693166 51.75813
149.26612108 76.878150481 76.932251833 76.932251833 156.2542
0.4334981259 0.5289795112 0.5288853033 0.5288853033 0.427475
0.0643191815 0.0539877086 0.0540439652 0.0540439652 0.066006
1.2134988899 0.2682722332 0.268733951 0.268733951 1.407531
24.191602759 11.234914728 11.263299429 11.263299429 25.7296

- - 0 0.0037865935 -
- - 0 0.0002553923 -
- - 0 0.0002599197 -
- - 62.273401448 62.273401448 -
- - 18.039703654 18.039703654 -
- - 1.0284688969 1.0284688969 -
- - 0.3646644296 0.3646644296 -
- - 0.6551132243 0.6551132243 -
 - - 69.47840563 69.47840563 -

0 0 0 0 0
0.0062194846 0.0965154402 3880.6369469 0.0327487495 0.006219
2.768817E-05 0.0046895234 120.91009225 0.0002971697 2.769E-05
0.0069903684 0.642847012 9466.8758834 0.1047550691 0.00699
0.0099537635 0.0653883994 1781.7960982 0.0418502089 0.009954
0.0598350387 0.126567758 4907.5017311 0.2194481103 0.059835
0.0239214544 0.016352526 795.22329629 0.0566724464 0.023921
0.0464205723 0.0222670406 1051.71483 0.0989325135 0.046421
0.0381382744 0.0072788629 377.6811187 0.0599797976 0.038138
0.0393852485 0.0042427469 208.40547089 0.0415724605 0.039385
0.0281388566 0.0015442094 64.542669739 0.0274158956 0.028139
0.0060656574 0.0023130843 66.564116207 0.0596584642 0.006066
0.0084676111 0.0025639513 42.332602266 0.0809893332 0.008468
0.0048213876 0.0013165621 11.440612179 0.0456946952 0.004821
0.0035096739 0.000915948 4.0411516754 0.03315781 0.00351
0.0023254683 0.0005945126 1.2526061354 0.0219451087 0.002325
0.0078174207 0.0019818241 2.5232198595 0.073747117 0.007817
0.7077330748 0 0 0 0.707733
0.0002289567 0.0026205988 43.022540756 0.0011350507 0.000229
0 0 0 0 0
Stream Name 1 Vapour Ph Liquid Phase
Vapour / Phase Fraction 0.616536 0.616536 0.383464
Temperature [F] 90.83608 90.83608 90.83608
Pressure [psig] 50 50 50
Molar Flow [MMSCFD] 5.217522 3.216788 2.000734
Mass Flow [lb/hr] 43440.42 10893.75 32546.68
Std Ideal Liq Vol Flow [barrel/day] 4358.237 1640.327 2717.91
Molar Enthalpy [Btu/lbmole] -88067.31 -55285.28 -140774
Molar Entropy [Btu/lbmole-F] 37.86211 42.27561 30.76607
Heat Flow [Btu/hr] -5E+07 -2E+07-30927040
Liq Vol Flow @Std Cond [barrel/day] 4109.006 567648.1 2671.29
Fluid Package Basis-1
Utility Type
Stream Name 1 Vapour Ph Liquid Phase
Act. Gas Flow [ACFM] 522.8203 522.8203 <empty>
Act. Liq. Flow [barrel/day] 2717.102 <empty> 2717.102
Act. Volume Flow [barrel/day] 136807.1 134090 2717.102
Avg. Liq. Density [lbmole/ft3] 0.561917 0.920472 0.34552
Bubble Point Pressure [psig] 1904.942 <empty> <empty>
CO2 Apparent Mole Conc. [lbmole/ft3]<empty> <empty> 2.30E-03
CO2 Apparent Wt. Conc. [lbmol/lb] <empty> <empty> 4.48E-05
CO2 Loading <empty> <empty> <empty>
Cost Based on Flow [Cost/s] 0 0 0
Cp/(Cp - R) 1.06494 1.184061 1.031825
Cp/Cv 1.044199 1.209275 1.210795
Cp/Cv (Ent. Method) <empty> <empty> 1.121173
Cv [Btu/lbmole-F] 31.1872 10.56409 53.17599
Cv (Ent. Method) [Btu/lbmole-F] <empty> <empty> 57.42667
Cv (Semi-Ideal) [Btu/lbmole-F] 30.57979 10.78905 62.39941
HHV Mass Basis (Std) [Btu/lb] <empty> <empty> <empty>
HHV Molar Basis (Std) [Btu/SCF] <empty> <empty> <empty>
Heat Capacity [Btu/lbmole-F] 32.56563 12.77489 64.38525
Heat of Vap. [Btu/SCF] 85.98725 <empty> <empty>
Ideal Gas Cp [Btu/lbmole-F] 27.00588 12.52042 50.29564
Ideal Gas Cp/Cv 1.07937 1.188507 1.041106
Kinematic Viscosity [cSt] <empty> 1.98994 1.441567
LHV Mass Basis (Std) [Btu/lb] <empty> <empty> <empty>
LHV Molar Basis (Std) [Btu/SCF] <empty> <empty> <empty>
Liq. Mass Density (Std. Cond) [lb/ft3] 45.19084 8.20E-02 52.08093
Liq. Vol. Flow (Std. Cond) [barrel/day] 4109.006 567648.1 2671.29
Liq. Vol. Flow - Sum(Std. Cond) [barrel/ 570319.4 567648.1 2671.29
Liquid Fraction 0.383464 0 1
Mass Cv [Btu/lb-F] 0.411313 0.342533 0.358942
Mass Cv (Ent. Method) [Btu/lb-F] <empty> <empty> 0.387634
Mass Cv (Semi-Ideal) [Btu/lb-F] 0.403302 0.349827 0.4212
Mass Density [lb/ft3] 1.357308 0.347275 51.20282
Mass Enthalpy [Btu/lb] -1161.476 -1792.586 -950.2369
Mass Entropy [Btu/lb-F] 0.499345 1.370757 0.207673
Mass Exergy [Btu/lb] 13.44124 <empty> <empty>
Mass Heat Capacity [Btu/lb-F] 0.429492 0.414217 0.434605
Mass Heat of Vap. [Btu/lb] 430.3216 <empty> <empty>
Mass Ideal Gas Cp [Btu/lb-F] 0.356167 0.405966 0.339499
Molar Density [lbmole/ft3] 1.79E-02 1.13E-02 0.345623
Molar Volume [ft3/lbmole] 55.86322 88.80872 2.893331
Molecular Weight 75.82359 30.84108 148.1466
Partial Pressure of CO2 [psig] -6.28257 <empty> <empty>
Partial Pressure of H2S [psig] -14.69594 <empty> <empty>
Phase Fraction [Act. Vol. Basis] 0.980139 0.980139 1.99E-02
Phase Fraction [Mass Basis] 0.250774 0.250774 0.749226
Phase Fraction [Molar Basis] 0.616536 0.616536 0.383464
Phase Fraction [Vol. Basis] 0.376374 0.376374 0.623626
Reid VP at 37.8 C [psig] 407.5627 <empty> 10.0701
Specific Heat [Btu/lbmole-F] 32.56563 12.77489 64.38525
Std. Gas Flow [MMSCFD] 5.207746 3.21076 1.996985
Std. Ideal Liq. Mass Density [lb/ft3] 42.60655 28.38835 51.1876
Surface Tension [dyne/cm] 23.94922 <empty> 23.94922
Thermal Conductivity [Btu/hr-ft-F] <empty> 1.45E-02 6.41E-02
True VP at 37.8 C [psig] 1977.606 1656.125 54.22413
User Property <empty> <empty> <empty>
Viscosity [cP] <empty> 1.11E-02 1.182359
Viscosity Index -8.796734 <empty> <empty>
Watson K 11.93793 14.86876 11.34217
Z Factor <empty> 0.972556 3.17E-02
H2S 0 0 0
CO2 8.27E-02 0.130045 6.64E-03
Nitrogen 3.74E-03 6.05E-03 3.03E-05
Methane 0.291258 0.467744 7.50E-03
Ethane 7.48E-02 0.114758 1.04E-02
Propane 0.136197 0.183998 5.93E-02
i-Butane 2.68E-02 2.91E-02 2.31E-02
n-Butane 4.08E-02 3.87E-02 4.42E-02
i-Pentane 2.17E-02 1.29E-02 3.58E-02
n-Pentane 2.08E-02 1.01E-02 3.81E-02
n-Hexane 1.17E-02 2.26E-03 2.69E-02
n-Heptane 0 0 0
n-Octane 0 0 0
n-Nonane 0 0 0
n-Decane 6.27E-08 1.99E-10 1.63E-07
n-C11 0 0 0
Dodecane* 0 0 0
Heptane LP* 0.286751 3.75E-05 0.747731
H2O 2.74E-03 4.28E-03 2.45E-04
Oxygen 0.00E+00 0.00E+00 0.00E+00
Stream Na 4 Vapour Ph Liquid Phase
Vapour / P 0.616532 6.17E-01 3.83E-01
Temperatur 90.835 9.08E+01 90.835
Pressure [p 50 5.00E+01 5.00E+01
Molar Flo 5.217615 3.22E+00 2.00079
Mass Flow 43441.19 1.09E+04 32547.29
Std Ideal L 4358.319 1.64E+03 2717.971
Molar Enth-88067.22 -5.53E+04 -140773
Molar Entr 37.86212 4.23E+01 30.76627
Heat Flow -5E+07 -1.95E+07-30927653
Liq Vol Fl 4109.036 5.68E+05 2671.288
Fluid Pack Basis-1
Utility Type
Stream Na 4 Vapour Ph Liquid Phase
Act. Gas F 522.825 5.23E+02 <empty>
Act. Liq. F 2717.099 <empty> 2.72E+03
Act. Volum 136808.3 1.34E+05 2.72E+03
Avg. Liq. D 0.561916 9.20E-01 3.46E-01
Bubble Poin1904.877 <empty> <empty>
CO2 Appare <empty> <empty> 2.30E-03
CO2 Appare <empty> <empty> 4.48E-05
CO2 Loadin<empty> <empty> <empty>
Cost Based 0 0.00E+00 0.00E+00
Cp/(Cp - R) 1.06494 1.18406 1.031825
Cp/Cv 1.044198 1.21E+00 1.210795
Cp/Cv (Ent<empty> <empty> 1.121164
Cv [Btu/lb 31.18722 1.06E+01 53.17558
Cv (Ent. M <empty> <empty> 5.74E+01
Cv (Semi-Id 30.57981 1.08E+01 62.39889
HHV Mass <empty>
Ba <empty> <empty>
HHV Molar<empty> <empty> <empty>
Heat Capac 32.56565 12.77491 64.38473
Heat of Vap85.98718 <empty> <empty>
Ideal Gas C 27.00588 1.25E+01 50.29522
Ideal Gas 1.07937 1.188506 1.041107
Kinematic V<empty> 1.99E+00 1.44E+00
LHV Mass Ba <empty> <empty> <empty>
LHV Molar <empty>
B <empty> <empty>
Liq. Mass D 45.19132 8.20E-02 5.21E+01
Liq. Vol. F 4109.036 5.68E+05 2671.288
Liq. Vol. F 570325.8 5.68E+05 2671.288
Liquid Frac 0.383468 0.00E+00 1
Mass Cv [Bt0.411313 3.43E-01 0.358942
Mass Cv (E<empty> <empty> 3.88E-01
Mass Cv (Se0.403302 3.50E-01 4.21E-01
Mass Densit 1.35732 3.47E-01 5.12E+01
Mass Entha-1161.475 -1.79E+03 -9.50E+02
Mass Entro 0.499345 1.37E+00 2.08E-01
Mass Exerg 13.44118 <empty> <empty>
Mass Heat C0.429492 4.14E-01 4.35E-01
Mass Heat o430.3213 <empty> <empty>
Mass Ideal 0.356167 4.06E-01 0.339499
Molar Densi1.79E-02 1.13E-02 0.345633
Molar Volu 55.86273 88.80852 2.893247
Molecular 75.82359 30.84116 148.1453
Partial Pre -6.282615 <empty> <empty>
Partial Pre -14.69594 <empty> <empty>
Phase Fract0.980139 9.80E-01 1.99E-02
Phase Fract0.250774 2.51E-01 0.749226
Phase Fract0.616532 6.17E-01 0.383468
Phase Fract0.376372 3.76E-01 0.623628
Reid VP at 407.5613 <empty> 10.07089
Specific He 32.56565 1.28E+01 64.38473
Std. Gas F 5.207838 3.21E+00 1.997041
Std. Ideal 42.60651 2.84E+01 51.18742
Surface Te 23.94906 <empty> 23.94906
Thermal Con <empty> 1.45E-02 6.41E-02
True VP at 1977.549 1656.108 54.22468
User Prope<empty> <empty> <empty>
Viscosity [ <empty> 1.11E-02 1.182361
Viscosity I -8.796737 <empty> <empty>
Watson K 11.93795 1.49E+01 11.34219
Z Factor <empty> 9.73E-01 3.17E-02
H2S 0 0.00E+00 0
CO2 8.27E-02 1.30E-01 6.64E-03
Nitrogen 3.74E-03 6.05E-03 3.03E-05
Methane 0.291258 0.467744 7.50E-03
Ethane 7.48E-02 0.114758 1.04E-02
Propane 0.136197 0.183998 5.93E-02
i-Butane 2.68E-02 2.91E-02 2.31E-02
n-Butane 4.08E-02 3.87E-02 4.42E-02
i-Pentane 2.17E-02 1.29E-02 3.58E-02
n-Pentane 2.08E-02 1.01E-02 3.81E-02
n-Hexane 1.17E-02 2.26E-03 2.69E-02
n-Heptane 0 0 0.00E+00
n-Octane 0 0 0
n-Nonane 0 0 0
n-Decane 6.27E-08 1.99E-10 1.63E-07
n-C11 0 0 0
Dodecane* 0 0 0
Heptane L 0.286751 3.75E-05 7.48E-01
H2O 2.74E-03 4.28E-03 2.45E-04
Oxygen 0 0 0.00E+00
Stream Na 5 Vapour Ph Liquid Phase
Vapour / P 1 1 0
Temperatur 89.7325 89.7325 89.7325
Pressure [p 45 45 45
Molar Flo 3.239532 3.239532 0
Mass Flow 11019.85 11019.85 0
Std Ideal L 1656.105 1656.105 0
Molar Enth -55299 -55299 -141732
Molar Entr 42.40257 42.40257 30.68468
Heat Flow -2E+07 -2E+07 0
Liq Vol Fl 571618.6 571618.6 0
Fluid Pack Basis-1
Utility Type
Stream Na 5 Vapour Ph Liquid Phase
Act. Gas F 570.4798 570.4798 <empty>
Act. Liq. F <empty> <empty> <empty>
Act. Volum 146313.5 146313.5 0
Avg. Liq. D 0.918149 0.918149 0.343592
Bubble Poin1496.844 <empty> <empty>
CO2 Appare <empty> <empty> <empty>
CO2 Appare <empty> <empty> <empty>
CO2 Loadin<empty> <empty> <empty>
Cost Based 0 0 0
Cp/(Cp - R) 1.183661 1.183661 1.031662
Cp/Cv 1.207042 1.207042 1.20915
Cp/Cv (Ent<empty> <empty> 1.126769
Cv [Btu/lb 10.6031 10.6031 53.51411
Cv (Ent. M <empty> <empty> 57.79246
Cv (Semi-Id 10.81254 10.81254 62.72074
HHV Mass <empty>
Ba <empty> <empty>
HHV Molar<empty> <empty> <empty>
Heat Capac 12.79838 12.79838 64.70658
Heat of Vap24.65998 <empty> <empty>
Ideal Gas C 12.56145 12.56145 50.54081
Ideal Gas 1.187776 1.187776 1.040899
Kinematic V2.136815 2.136815 1.47678
LHV Mass Ba <empty> <empty> <empty>
LHV Molar <empty>
B <empty> <empty>
Liq. Mass D 8.24E-02 8.24E-02 52.14265
Liq. Vol. F 571618.6 571618.6 0
Liq. Vol. F 571618.6 571618.6 0
Liquid Frac 0 0 1
Mass Cv [Bt0.342267 0.342267 0.358515
Mass Cv (E<empty> <empty> 0.387177
Mass Cv (Se0.349028 0.349028 0.420194
Mass Densit0.321947 0.321947 51.29829
Mass Entha-1785.047 -1785.047 -949.5265
Mass Entro 1.36875 1.36875 0.20557
Mass Exerg 47.56949 <empty> <empty>
Mass Heat C0.413131 0.413131 0.433498
Mass Heat o302.0566 <empty> <empty>
Mass Ideal 0.405482 0.405482 0.338595
Molar Densi1.04E-02 1.04E-02 0.34367
Molar Volu 96.22403 96.22403 2.909769
Molecular 30.97904 30.97904 149.2661
Partial Pre -6.966792 <empty> <empty>
Partial Pre -14.69594 <empty> <empty>
Phase Fract 1 1 0
Phase Fract 1 1 0
Phase Fract 1 1 0
Phase Fract 1 1 <empty>
Reid VP at <empty> <empty> 8.558085
Specific He 12.79838 12.79838 64.70658
Std. Gas F 3.233462 3.233462 0
Std. Ideal 28.44336 28.44336 51.28667
Surface Te <empty> <empty> 24.1916
Thermal Con1.45E-02 1.45E-02 6.43E-02
True VP at 1632.069 1632.069 49.42951
User Prope<empty> <empty> <empty>
Viscosity [ 1.10E-02 1.10E-02 1.213499
Viscosity I -17.51744 <empty> <empty>
Watson K 14.85617 14.85617 11.33593
Z Factor <empty> 0.974276 2.95E-02
H2S 0 0 0
CO2 0.127955 0.127955 6.22E-03
Nitrogen 5.87E-03 5.87E-03 2.77E-05
Methane 0.459261 0.459261 6.99E-03
Ethane 0.113698 0.113698 9.95E-03
Propane 0.190309 0.190309 5.98E-02
i-Butane 3.07E-02 3.07E-02 2.39E-02
n-Butane 4.12E-02 4.12E-02 4.64E-02
i-Pentane 1.38E-02 1.38E-02 3.81E-02
n-Pentane 1.04E-02 1.04E-02 3.94E-02
n-Hexane 2.33E-03 2.33E-03 2.81E-02
n-Heptane 1.65E-04 1.65E-04 6.07E-03
n-Octane 7.62E-05 7.62E-05 8.47E-03
n-Nonane 1.51E-05 1.51E-05 4.82E-03
n-Decane 4.01E-06 4.01E-06 3.51E-03
n-C11 9.19E-07 9.19E-07 2.33E-03
Dodecane* 1.42E-06 1.42E-06 7.82E-03
Heptane L 3.30E-05 3.30E-05 0.707733
H2O 4.22E-03 4.22E-03 2.29E-04
Oxygen 0 0 0
Stream Na 6 Vapour Ph Liquid Phase
Vapour / P 0 0 1
Temperatur 89.7325 89.7325 89.7325
Pressure [p 45 45 45
Molar Flo 1.978082 0 1.978082
Mass Flow 32421.34 0 32421.34
Std Ideal L 2702.214 0 2702.214
Molar Enth -141732 -55299 -141732
Molar Entr 30.68468 42.40257 30.68468
Heat Flow -30784915 0-30784915
Liq Vol Fl 2657.854 0 2657.854
Fluid Pack Basis-1
Utility Type
Stream Na 6 Vapour Ph Liquid Phase
Act. Gas F <empty> <empty> <empty>
Act. Liq. F 2701.602 <empty> 2701.602
Act. Volum 2701.602 0 2701.602
Avg. Liq. D 0.343592 0.918149 0.343592
Bubble Poin44.99787 <empty> <empty>
CO2 Appare2.12E-03 <empty> 2.12E-03
CO2 Appare4.13E-05 <empty> 4.13E-05
CO2 Loadin<empty> <empty> <empty>
Cost Based 0 0 0
Cp/(Cp - R) 1.031662 1.183661 1.031662
Cp/Cv 1.20915 1.207042 1.20915
Cp/Cv (Ent<empty> <empty> 1.119637
Cv [Btu/lb 53.51411 10.6031 53.51411
Cv (Ent. M 57.79252 <empty> 57.79246
Cv (Semi-Id 62.72074 10.81254 62.72074
HHV Mass <empty>
Ba <empty> <empty>
HHV Molar<empty> <empty> <empty>
Heat Capac 64.70658 12.79838 64.70658
Heat of Vap139.2823 <empty> <empty>
Ideal Gas C 50.54081 12.56145 50.54081
Ideal Gas 1.040899 1.187776 1.040899
Kinematic V 1.47678 2.136815 1.47678
LHV Mass Ba <empty> <empty> <empty>
LHV Molar <empty>
B <empty> <empty>
Liq. Mass D 52.14265 8.24E-02 52.14265
Liq. Vol. F 2657.854 0 2657.854
Liq. Vol. F 2657.854 0 2657.854
Liquid Frac 1 0 1
Mass Cv [Bt0.358515 0.342267 0.358515
Mass Cv (E 0.387178 <empty> 0.387177
Mass Cv (Se0.420194 0.349028 0.420194
Mass Densit51.29829 0.321947 51.29829
Mass Entha-949.5265 -1785.047 -949.5265
Mass Entro 0.20557 1.36875 0.20557
Mass Exerg 0.43047 <empty> <empty>
Mass Heat C0.433498 0.413131 0.433498
Mass Heat o354.0774 <empty> <empty>
Mass Ideal 0.338595 0.405482 0.338595
Molar Densi 0.34367 1.04E-02 0.34367
Molar Volu 2.909769 96.22403 2.909769
Molecular 149.2661 30.97904 149.2661
Partial Pre -14.69594 <empty> <empty>
Partial Pre -14.69594 <empty> <empty>
Phase Fract 0 0 1
Phase Fract 0 0 1
Phase Fract 0 0 1
Phase Fract<empty> <empty> 1
Reid VP at 8.558085 <empty> 8.558085
Specific He 64.70658 12.79838 64.70658
Std. Gas F 1.974376 0 1.974376
Std. Ideal 51.28667 28.44336 51.28667
Surface Te 24.1916 <empty> 24.1916
Thermal Con6.43E-02 1.45E-02 6.43E-02
True VP at 49.42951 1632.069 49.42951
User Prope<empty> <empty> <empty>
Viscosity [ 1.213499 1.10E-02 1.213499
Viscosity I 8.138769 <empty> <empty>
Watson K 11.33593 14.85617 11.33593
Z Factor <empty> 0.974276 2.95E-02
H2S 0 0 0
CO2 6.22E-03 0.127955 6.22E-03
Nitrogen 2.77E-05 5.87E-03 2.77E-05
Methane 6.99E-03 0.459261 6.99E-03
Ethane 9.95E-03 0.113698 9.95E-03
Propane 5.98E-02 0.190309 5.98E-02
i-Butane 2.39E-02 3.07E-02 2.39E-02
n-Butane 4.64E-02 4.12E-02 4.64E-02
i-Pentane 3.81E-02 1.38E-02 3.81E-02
n-Pentane 3.94E-02 1.04E-02 3.94E-02
n-Hexane 2.81E-02 2.33E-03 2.81E-02
n-Heptane 6.07E-03 1.65E-04 6.07E-03
n-Octane 8.47E-03 7.62E-05 8.47E-03
n-Nonane 4.82E-03 1.51E-05 4.82E-03
n-Decane 3.51E-03 4.01E-06 3.51E-03
n-C11 2.33E-03 9.19E-07 2.33E-03
Dodecane* 7.82E-03 1.42E-06 7.82E-03
Heptane L 0.707733 3.30E-05 0.707733
H2O 2.29E-04 4.22E-03 2.29E-04
Oxygen 0 0 0
Stream Name 7 Vapour Ph Liquid Phase
Vapour / Phase Fracti 0.999809292 0.999809 1.91E-04
Temperature [F] 103.709072 103.7091 103.7091
Pressure [psig] 450 450 450
Molar Flow [MMSCFD]0.462852218 0.462764 8.83E-05
Mass Flow [lb/hr] 1293.43761 1292.692 0.745142
Std Ideal Liq Vol Flow 215.8600552 215.7805 7.95E-02
Molar Enthalpy [Btu/l -48930.292 -48924 -81831
Molar Entropy [Btu/lb 38.07813031 38.07953 30.76123
Heat Flow [Btu/hr] -2486826.18 -2486033 -793.1478
Liq Vol Flow @Std Con81858.71611 81843.42 7.68E-02
Fluid Package Basis-1
Utility Type
Stream Name 7 Vapour Ph Liquid Phase
Act. Gas Flow [ACFM] 9.6236987 9.623699 <empty>
Act. Liq. Flow [barrel/ 8.02E-02 <empty> 8.02E-02
Act. Volume Flow [bar 2468.312682 2468.233 8.02E-02
Avg. Liq. Density [lbmo1.006441801 1.006621 0.520967
Bubble Point Pressure 2551.7194 <empty> <empty>
CO2 Apparent Mole Con <empty> <empty> 1.70E-02
CO2 Apparent Wt. Conc <empty> <empty> 4.28E-04
CO2 Loading <empty> <empty> <empty>
Cost Based on Flow [C 0 0 0
Cp/(Cp - R) 1.185258214 1.18535 1.051339
Cp/Cv 1.370787874 1.371086 1.051339
Cp/Cv (Ent. Method) 0.219840851 <empty> 0.703672
Cv [Btu/lbmole-F] 9.268506787 9.262603 38.68113
Cv (Ent. Method) [Btu<empty> <empty> <empty>
Cv (Semi-Ideal) [Btu/l 10.71931547 10.71398 38.68113
HHV Mass Basis (Std) [<empty> <empty> <empty>
HHV Molar Basis (Std)<empty> <empty> <empty>
Heat Capacity [Btu/lb 12.70515671 12.69982 40.66697
Heat of Vap. [Btu/SCF]16.21875629 <empty> <empty>
Ideal Gas Cp [Btu/lbmo11.08971361 11.08599 30.58781
Ideal Gas Cp/Cv 1.21813149 1.218221 1.06943
Kinematic Viscosity [cS<empty> 0.354114 0.421475
LHV Mass Basis (Std) [<empty> <empty> <empty>
LHV Molar Basis (Std) <empty> <empty> <empty>
Liq. Mass Density (Std. 6.75E-02 6.75E-02 41.48678
Liq. Vol. Flow (Std. Co 81858.71611 81843.42 7.68E-02
Liq. Vol. Flow - Sum(S 81843.50139 81843.42 7.68E-02
Liquid Fraction 1.91E-04 0 1
Mass Cv [Btu/lb-F] 0.3641934 0.364102 0.503148
Mass Cv (Ent. Method)<empty> <empty> <empty>
Mass Cv (Semi-Ideal) [ 0.421200959 0.421154 0.503148
Mass Density [lb/ft3] 2.239950784 2.238733 39.73589
Mass Enthalpy [Btu/lb -1922.64944 -1923.144 -1064.425
Mass Entropy [Btu/lb- 1.496228473 1.49686 0.40013
Mass Exergy [Btu/lb] 138.9218807 <empty> <empty>
Mass Heat Capacity [B 0.499231897 0.499215 0.52898
Mass Heat of Vap. [Btu241.8261598 <empty> <empty>
Mass Ideal Gas Cp [Btu0.435755252 0.435777 0.397874
Molar Density [lbmole 8.80E-02 8.80E-02 0.516869
Molar Volume [ft3/lb 11.3615977 11.3634 1.934729
Molecular Weight 25.44940897 25.4396 76.87815
Partial Pressure of CO230.89491347 <empty> <empty>
Partial Pressure of H2S -14.695945 <empty> <empty>
Phase Fraction [Act. Vo0.999967525 0.999968 3.25E-05
Phase Fraction [Mass B0.999423905 0.999424 5.76E-04
Phase Fraction [Molar 0.999809292 0.999809 1.91E-04
Phase Fraction [Vol. Ba0.999631577 0.999632 3.68E-04
Reid VP at 37.8 C [psig<empty> <empty> 145.7359
Specific Heat [Btu/lbm12.70515671 12.69982 40.66697
Std. Gas Flow [MMSCF0.461984944 0.461897 8.81E-05
Std. Ideal Liq. Mass De25.61334899 25.60803 40.05096
Surface Tension [dyne 11.23491473 <empty> 11.23491
Thermal Conductivity [<empty> 1.84E-02 5.40E-02
True VP at 37.8 C [psig2505.865492 2507.644 441.6362
User Property <empty> <empty> <empty>
Viscosity [cP] <empty> 1.27E-02 0.268272
Viscosity Index <empty> <empty> <empty>
Watson K 15.73665996 15.73858 12.85043
Z Factor <empty> 0.873415 0.148707
H2S 0 0 0
CO2 9.65E-02 9.83E-02 3.29E-02
Nitrogen 4.69E-03 4.81E-03 2.99E-04
Methane 0.642847012 0.657619 0.10539
Ethane 6.54E-02 6.60E-02 4.20E-02
Propane 0.126567758 0.124006 0.219784
i-Butane 1.64E-02 1.52E-02 5.67E-02
n-Butane 2.23E-02 2.02E-02 9.89E-02
i-Pentane 7.28E-03 5.83E-03 5.99E-02
n-Pentane 4.24E-03 3.22E-03 4.15E-02
n-Hexane 1.54E-03 8.35E-04 2.73E-02
n-Heptane 2.31E-03 7.42E-04 5.95E-02
n-Octane 2.56E-03 4.15E-04 8.08E-02
n-Nonane 1.32E-03 1.00E-04 4.56E-02
n-Decane 9.16E-04 3.19E-05 3.31E-02
n-C11 5.95E-04 9.02E-06 2.19E-02
Dodecane* 1.98E-03 1.37E-05 7.36E-02
Heptane LP* 0 0 0
H2O 2.62E-03 2.67E-03 1.00E-03
Oxygen 0 0 0
Stream Na 8 Vapour Ph Liquid Pha Aqueous Phase
Vapour / P 1 1 0 0
Temperatur103.4674 103.4674 103.4674 103.4674
Pressure [p 447 447 447 447
Molar Flo 0.46276 0.46276 0 0
Mass Flow 1292.669 1292.669 0 0
Std Ideal L 215.7782 215.7782 0 0
Molar Enth-48923.55 -48923.55 -81860.62 -122584
Molar Entr 38.09091 38.09091 30.73463 13.73385
Heat Flow -2485987 -2485987 0 0
Liq Vol Fl 81842.7 81842.7 0 0
Fluid Pack Basis-1
Utility Type
Stream Na 8 Vapour Ph Liquid Pha Aqueous Phase
Act. Gas F 9.688914 9.688914 <empty> <empty>
Act. Liq. F 0 <empty> <empty> 0
Act. Volum 2484.959 2484.959 0 0
Avg. Liq. D 1.006623 1.006623 0.520667 3.451949
Bubble Poin2550.571 <empty> <empty> <empty>
CO2 Appare <empty> <empty> <empty> <empty>
CO2 Appare <empty> <empty> <empty> <empty>
CO2 Loadin<empty> <empty> <empty> <empty>
Cost Based 0 0 0 0
Cp/(Cp - R) 1.18559 1.18559 1.05131 1.119864
Cp/Cv 1.370112 1.370112 1.05131 1.154962
Cp/Cv (Ent<empty> <empty> <empty> 1.195992
Cv [Btu/lb 9.259105 9.259105 38.7025 16.06397
Cv (Ent. M <empty> <empty> <empty> 15.51288
Cv (Semi-Id 10.70017 10.70017 38.7025 16.56743
HHV Mass <empty>
Ba <empty> <empty> 976.4302
HHV Molar<empty> <empty> <empty> 46.42022
Heat Capac 12.68601 12.68601 40.68834 18.55327
Heat of Vap16.00642 <empty> <empty> <empty>
Ideal Gas C 11.08351 11.08351 30.60591 8.040998
Ideal Gas 1.21828 1.21828 1.069386 1.327959
Kinematic V0.356153 0.356153 0.422054 0.65674
LHV Mass Ba <empty> <empty> <empty> 4.77E-03
LHV Molar <empty>
B <empty> <empty> 2.27E-04
Liq. Mass D 6.75E-02 6.75E-02 41.48907 63.37736
Liq. Vol. F 81842.7 81842.7 0 0
Liq. Vol. F 81842.7 81842.7 0 0
Liquid Frac 0 0 1 1
Mass Cv [Bt0.363968 0.363968 0.503072 0.890478
Mass Cv (E<empty> <empty> <empty> 0.85993
Mass Cv (Se0.420615 0.420615 0.503072 0.918387
Mass Densit2.223624 2.223624 39.74969 62.2734
Mass Entha-1923.143 -1923.143 -1064.061 -6795.246
Mass Entro 1.497321 1.497321 0.399502 0.761313
Mass Exerg 138.7478 <empty> <empty> <empty>
Mass Heat C0.498676 0.498676 0.528885 1.028469
Mass Heat o238.7544 <empty> <empty> <empty>
Mass Ideal 0.435683 0.435683 0.397829 0.445739
Molar Densi8.74E-02 8.74E-02 0.516684 3.452019
Molar Volu 11.4405 11.4405 1.935418 0.289686
Molecular 25.43937 25.43937 76.93225 18.0397
Partial Pre 30.60093 <empty> <empty> <empty>
Partial Pre -14.69594 <empty> <empty> <empty>
Phase Fract 1 1 0 0
Phase Fract 1 1 0 0
Phase Fract 1 1 0 0
Phase Fract 1 1 <empty> <empty>
Reid VP at <empty> <empty> 144.9546 <empty>
Specific He 12.68601 12.68601 40.68834 18.55327
Std. Gas F 0.461893 0.461893 0 0
Std. Ideal 25.60784 25.60784 40.05606 62.27214
Surface Te <empty> <empty> 11.2633 69.47841
Thermal Con1.84E-02 1.84E-02 5.40E-02 0.364664
True VP at 2507.692 2507.692 439.2173 39.34366
User Prope<empty> <empty> <empty> <empty>
Viscosity [ 1.27E-02 1.27E-02 0.268734 0.655113
Viscosity I <empty> <empty> <empty> <empty>
Watson K 15.73863 15.73863 12.85093 8.522341
Z Factor <empty> 0.874039 0.147863 2.21E-02
H2S 0 0 0 0
CO2 3880.637 3880.637 0 0
Nitrogen 120.9101 120.9101 0 0
Methane 9466.876 9466.876 0 0
Ethane 1781.796 1781.796 0 0
Propane 4907.502 4907.502 0 0
i-Butane 795.2233 795.2233 0 0
n-Butane 1051.715 1051.715 0 0
i-Pentane 377.6811 377.6811 0 0
n-Pentane 208.4055 208.4055 0 0
n-Hexane 64.54267 64.54267 0 0
n-Heptane 66.56412 66.56412 0 0
n-Octane 42.3326 42.3326 0 0
n-Nonane 11.44061 11.44061 0 0
n-Decane 4.041152 4.041152 0 0
n-C11 1.252606 1.252606 0 0
Dodecane* 2.52322 2.52322 0 0
Heptane L 0 0 0 0
H2O 43.02254 43.02254 0 0
Oxygen 0 0 0 0
Stream Na 9 Vapour Ph Liquid Pha Aqueous Phase
Vapour / P 0 0 0.979315 2.07E-02
Temperatur103.4674 103.4674 103.4674 103.4674
Pressure [p 447 447 447 447
Molar Flo 9.24E-05 0 9.05E-05 1.91E-06
Mass Flow 0.76833 0 0.764544 3.79E-03
Std Ideal L 8.18E-02 0 8.16E-02 2.60E-04
Molar Enth -82703 -48923.55 -81860.62 -122584
Molar Entr 30.38297 38.09091 30.73463 13.73385
Heat Flow -839.2516 0 -813.5208 -25.73082
Liq Vol Fl 7.89E-02 0 7.88E-02 2.55E-04
Fluid Pack Basis-1
Utility Type
Stream Na 9 Vapour Ph Liquid Pha Aqueous Phase
Act. Gas F <empty> <empty> <empty> <empty>
Act. Liq. F 8.25E-02 <empty> 8.22E-02 2.60E-04
Act. Volum 8.25E-02 0 8.22E-02 2.60E-04
Avg. Liq. D 0.529976 1.006623 0.520667 3.451949
Bubble Poin446.9969 <empty> <empty> <empty>
CO2 Appare1.69E-02 <empty> 1.69E-02 3.27E-03
CO2 Appare4.24E-04 <empty> 4.26E-04 5.24E-05
CO2 Loadin<empty> <empty> <empty> <empty>
Cost Based 0 0 0 0
Cp/(Cp - R) 1.051925 1.18559 1.05131 1.119864
Cp/Cv 1.051925 1.370112 1.05131 1.154962
Cp/Cv (Ent<empty> <empty> <empty> 1.195992
Cv [Btu/lb 38.24464 9.259105 38.7025 16.06397
Cv (Ent. M <empty> <empty> <empty> 15.51288
Cv (Semi-Id 38.24464 10.70017 38.7025 16.56743
HHV Mass <empty>
Ba <empty> <empty> 976.4302
HHV Molar<empty> <empty> <empty> 46.42022
Heat Capac 40.23048 12.68601 40.68834 18.55327
Heat of Vap67.12302 <empty> <empty> <empty>
Ideal Gas C 30.13917 11.08351 30.60591 8.040998
Ideal Gas 1.070537 1.21828 1.069386 1.327959
Kinematic V0.426109 0.356153 0.422054 0.65674
LHV Mass Ba<empty> <empty> <empty> 4.77E-03
LHV Molar <empty>
B <empty> <empty> 2.27E-04
Liq. Mass D 41.60801 6.75E-02 41.48907 63.37736
Liq. Vol. F 7.89E-02 0 7.88E-02 2.55E-04
Liq. Vol. F 7.90E-02 0 7.88E-02 2.55E-04
Liquid Frac 1 0 1 1
Mass Cv [Bt0.505119 0.363968 0.503072 0.890478
Mass Cv (E<empty> <empty> <empty> 0.85993
Mass Cv (Se0.505119 0.420615 0.503072 0.918387
Mass Densit39.82067 2.223624 39.74969 62.2734
Mass Entha-1092.306 -1923.143 -1064.061 -6795.246
Mass Entro 0.401286 1.497321 0.399502 0.761313
Mass Exerg 15.25287 <empty> <empty> <empty>
Mass Heat C0.531347 0.498676 0.528885 1.028469
Mass Heat o336.4018 <empty> <empty> <empty>
Mass Ideal 0.398066 0.435683 0.397829 0.445739
Molar Densi0.525935 8.74E-02 0.516684 3.452019
Molar Volu 1.901377 11.4405 1.935418 0.289686
Molecular 75.71408 25.43937 76.93225 18.0397
Partial Pre -14.69594 <empty> <empty> <empty>
Partial Pre -14.69594 <empty> <empty> <empty>
Phase Fract 0 0 0.996849 3.15E-03
Phase Fract 0 0 0.995072 4.93E-03
Phase Fract 0 0 0.979315 2.07E-02
Phase Fract<empty> <empty> 0.996824 3.18E-03
Reid VP at 144.9648 <empty> 144.9546 <empty>
Specific He 40.23048 12.68601 40.68834 18.55327
Std. Gas F 9.22E-05 0 9.03E-05 1.91E-06
Std. Ideal 40.12661 25.60784 40.05606 62.27214
Surface Te <empty> <empty> 11.2633 69.47841
Thermal Con5.43E-02 1.84E-02 5.40E-02 0.364664
True VP at 439.2163 2507.692 439.2173 39.34366
User Prope<empty> <empty> <empty> <empty>
Viscosity [ 0.2718 1.27E-02 0.268734 0.655113
Viscosity I -12.1085 <empty> <empty> <empty>
Watson K 12.85087 15.73863 12.85093 8.522341
Z Factor <empty> 0.874039 0.147863 2.21E-02
H2S 0 0 0 0
CO2 3.27E-02 9.83E-02 3.28E-02 9.44E-04
Nitrogen 2.97E-04 4.81E-03 2.97E-04 1.61E-06
Methane 1.05E-01 0.657605 0.10477 2.51E-07
Ethane 4.19E-02 6.60E-02 4.19E-02 5.93E-10
Propane 0.219448 0.12402 0.219479 9.85E-12
i-Butane 5.67E-02 1.52E-02 5.67E-02 3.84E-15
n-Butane 9.89E-02 2.02E-02 9.89E-02 8.09E-15
i-Pentane 6.00E-02 5.83E-03 6.00E-02 5.47E-18
n-Pentane 4.16E-02 3.22E-03 4.16E-02 3.39E-18
n-Hexane 2.74E-02 8.35E-04 2.74E-02 1.54E-21
n-Heptane 5.97E-02 7.40E-04 5.97E-02 1.52E-24
n-Octane 8.10E-02 4.13E-04 8.10E-02 8.14E-28
n-Nonane 4.57E-02 9.94E-05 4.57E-02 1.59E-31
n-Decane 3.32E-02 3.17E-05 3.32E-02 1.39E-35
n-C11 2.19E-02 8.93E-06 2.19E-02 2.44E-39
Dodecane* 7.37E-02 1.35E-05 7.38E-02 1.48E-43
Heptane L 0 0 0 0
H2O 1.14E-03 2.66E-03 9.96E-04 0.999054
Oxygen 0 0 0 0
Stream Na 10 Vapour Ph Liquid Phase
Vapour / P 6.28E-02 6.28E-02 0.9372
Temperatur83.48424 83.48424 83.48424
Pressure [p 0 0 0
Molar Flo 1.978082 1.24E-01 1.85386
Mass Flow 32421.34 613.5164 31807.83
Std Ideal L 2702.214 80.14667 2622.067
Molar Enth -141732 -56962.89 -147412
Molar Entr 30.79923 42.70663 30.00135
Heat Flow -30784915 -776995 -3E+07
Liq Vol Fl 2657.854 79.29344 2593.896
Fluid Pack Basis-1
Utility Type
Stream Na 10 Vapour Ph Liquid Phase
Act. Gas F 88.81005 88.81005 <empty>
Act. Liq. F 2626.931 <empty> 2626.931
Act. Volum 25404.44 22777.51 2626.931
Avg. Liq. D 0.343592 0.727501 0.331857
Bubble Poin42.40707 <empty> <empty>
CO2 Appare <empty> <empty> 3.41E-04
CO2 Appare <empty> <empty> 6.59E-06
CO2 Loadin<empty> <empty> <empty>
Cost Based 0 0 0
Cp/(Cp - R) 1.032164 1.124346 1.030641
Cp/Cv 1.0022 1.132031 1.1986
Cp/Cv (Ent<empty> <empty> <empty>
Cv [Btu/lb 63.58784 15.86186 55.72735
Cv (Ent. M <empty> <empty> 59.78098
Cv (Semi-Id 61.74191 15.97028 64.80896
HHV Mass <empty>
Ba <empty> <empty>
HHV Molar<empty> <empty> <empty>
Heat Capac 63.72776 17.95612 66.7948
Heat of Vap140.4156 <empty> <empty>
Ideal Gas C 49.98888 17.8339 52.14351
Ideal Gas 1.041369 1.125305 1.039592
Kinematic V<empty> 4.798494 1.697691
LHV Mass Ba <empty> <empty> <empty>
LHV Molar <empty>
B <empty> <empty>
Liq. Mass D 52.14265 33.07365 52.4173
Liq. Vol. F 2657.854 79.29344 2593.896
Liq. Vol. F 2673.189 79.29344 2593.896
Liquid Frac 0.9372 0 1
Mass Cv [Bt0.426003 0.352658 0.356645
Mass Cv (E<empty> <empty> 0.382588
Mass Cv (Se0.413636 0.355069 0.414766
Mass Densit5.455249 0.115137 51.75813
Mass Entha-949.5265 -1266.462 -943.4134
Mass Entro 0.206338 0.949501 0.192003
Mass Exerg 1.86E-02 <empty> <empty>
Mass Heat C0.426941 0.39922 0.427475
Mass Heat o356.9583 <empty> <empty>
Mass Ideal 0.334898 0.396503 0.333709
Molar Densi3.65E-02 2.56E-03 0.331243
Molar Volu 27.36194 390.6493 3.018932
Molecular 149.2661 44.97799 156.2542
Partial Pre -13.48054 <empty> <empty>
Partial Pre -14.69594 <empty> <empty>
Phase Fract0.896596 0.896596 1.03E-01
Phase Fract 1.89E-02 1.89E-02 0.981077
Phase Fract 6.28E-02 6.28E-02 0.9372
Phase Fract 2.97E-02 2.97E-02 0.97034
Reid VP at 8.558085 309.2982 -3.20045
Specific He 63.72776 17.95612 66.7948
Std. Gas F 1.974376 1.24E-01 1.850386
Std. Ideal 51.28667 32.72155 51.85413
Surface Te 25.7296 <empty> 25.7296
Thermal Con <empty> 1.08E-02 6.60E-02
True VP at 49.42951 550.9236 3.039103
User Prope<empty> <empty> <empty>
Viscosity [ <empty> 8.85E-03 1.407531
Viscosity I 8.775246 <empty> <empty>
Watson K 11.33593 14.15025 11.30732
Z Factor <empty> 0.98493 7.61E-03
H2S 0 0 0
CO2 6.22E-03 7.89E-02 1.01E-03
Nitrogen 2.77E-05 4.08E-04 4.66E-07
Methane 6.99E-03 9.93E-02 3.78E-04
Ethane 9.95E-03 0.112441 2.61E-03
Propane 5.98E-02 0.404268 3.52E-02
i-Butane 2.39E-02 8.72E-02 1.94E-02
n-Butane 4.64E-02 0.125279 4.08E-02
i-Pentane 3.81E-02 4.57E-02 3.76E-02
n-Pentane 3.94E-02 3.50E-02 3.97E-02
n-Hexane 2.81E-02 7.84E-03 2.96E-02
n-Heptane 6.07E-03 5.40E-04 6.46E-03
n-Octane 8.47E-03 2.40E-04 9.06E-03
n-Nonane 4.82E-03 4.59E-05 5.16E-03
n-Decane 3.51E-03 1.18E-05 3.76E-03
n-C11 2.33E-03 2.59E-06 2.49E-03
Dodecane* 7.82E-03 4.02E-06 8.38E-03
Heptane L 0.707733 8.70E-05 0.758444
H2O 2.29E-04 2.86E-03 4.05E-05
Oxygen 0 0 0