document1
DESCRIPTION
Stream propertiesTRANSCRIPT
ENERFLEX LTDBurlington, MAUSA
Case Name: E002100 TEG DEHY UNIT - 03PE.hsc
Unit Set: NewUser3
Date/Time: Fri Feb 05 17:04:24 2016
Material Stream: 1Fluid Package: Glycol
Property Package: Glycol Package
CONDITIONS
Vapour / Phase FractionTemperature: (F)Pressure: (psia)Molar Flow (MMSCFD)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (USGPM)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)Liq Vol Flow @Std Cond (USGPM)
Overall0.8018192.914.00
0.83411697
4.997-9.140e+004
39.71-8.371e+006
4.480 *
Vapour Phase0.8018192.914.00
0.66881370
4.342-8.412e+004
45.43-6.177e+006
3.890
Aqueous Phase0.1982192.914.00
0.1653327.2
0.6547-1.208e+005
16.58-2.194e+006
0.6439
PROPERTIES
Molecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)
(lbmole/ft3)(lb/ft3)
(USGPM)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
Overall18.53
2.509e-0034.649e-002
4551-49332.14310.67
0.57629.029e+0041.126e+005
6077
Vapour Phase18.65
2.012e-0033.753e-002
4550-45102.4368.878
0.47601.126e+0051.360e+005
7294
Aqueous Phase18.023.31459.73
0.6829-6705
0.919917.94
0.995678.93
1.772e+004983.0
Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.3.8628) Page 1 of 6
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* Specified by user.Licensed to: ENERFLEX LTD
ENERFLEX LTDBurlington, MAUSA
Case Name: E002100 TEG DEHY UNIT - 03PE.hsc
Unit Set: NewUser3
Date/Time: Fri Feb 05 17:04:24 2016
Material Stream: 1 (continued)Fluid Package: Glycol
Property Package: Glycol Package
PROPERTIES
CO2 LoadingCO2 App ML ConCO2 App WT ConLHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic Viscosity
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(Btu/lbmole)(cSt)
Overall---------
48740.86900.80720.999890.07
0.14640.0000608.32.28510.67
0.832542.33
0.6829---
17.68---
0.00001.2291.180
2.352e+004---
Vapour Phase---------
60370.86900.80720.9998
------
0.0000608.32.1088.878
0.667539.32
---0.993617.69
------
1.2881.297
---16.69
Aqueous Phase---
6.509e-0061.090e-007
4.3790.13100.1928
1.501e-004------
0.0000---
3.45717.94
0.165062.30
0.68296.032e-004
8.865------
1.1241.183
---0.3276
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* Specified by user.Licensed to: ENERFLEX LTD
ENERFLEX LTDBurlington, MAUSA
Case Name: E002100 TEG DEHY UNIT - 03PE.hsc
Unit Set: NewUser3
Date/Time: Fri Feb 05 17:04:24 2016
Material Stream: 1 (continued)Fluid Package: Glycol
Property Package: Glycol Package
PROPERTIES
Liq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(lb/ft3)(USGPM)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(USGPM)
Overall47.224.480
0.1982398.51270
0.801860.59
------
8.6890.46909.043
0.4881---------------
4.533---
Vapour Phase43.903.890
0.0000497.0
---0.8018
---1.615e-0021.003e-002
6.8920.36956.843
0.3669---------------
3.890---
Aqueous Phase63.36
0.64391.000
0.3017---
0.198260.59
0.39030.313515.96
0.885415.17
0.841514.60
0.81021.22967.873.457
0.6439---
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* Specified by user.Licensed to: ENERFLEX LTD
ENERFLEX LTDBurlington, MAUSA
Case Name: E002100 TEG DEHY UNIT - 03PE.hsc
Unit Set: NewUser3
Date/Time: Fri Feb 05 17:04:24 2016
Material Stream: 1 (continued)Fluid Package: Glycol
Property Package: Glycol Package
COMPOSITION
Overall Phase Vapour Fraction 0.8018
COMPONENTS
MethaneEthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-OctaneBenzeneE-Benzeneo-XyleneTolueneH2OTEGlycolNitrogenCO2H2S
MOLAR FLOW (lbmole/hr)
17.48081.50340.85040.19540.19560.05510.02900.00010.00000.00000.00000.00000.00000.0000
70.44230.00100.06630.76800.0000
MOLE FRACTION
0.19090.01640.00930.00210.00210.00060.00030.00000.00000.00000.00000.00000.00000.00000.76910.00000.00070.00840.0000
MASS FLOW (lb/hr)
280.442345.207137.501911.356311.36623.97312.09190.01020.00280.00100.00000.00000.00000.0000
1269.02480.15091.8583
33.80040.0000
MASS FRACTION
0.16530.02660.02210.00670.00670.00230.00120.00000.00000.00000.00000.00000.00000.00000.74790.00010.00110.01990.0000
LIQUID VOLUMEFLOW (barrel/day)
64.13858.70295.06801.38371.33440.43640.22750.00110.00030.00010.00000.00000.00000.0000
87.06910.00920.15782.80420.0000
LIQUID VOLUMEFRACTION
0.37430.05080.02960.00810.00780.00250.00130.00000.00000.00000.00000.00000.00000.00000.50820.00010.00090.01640.0000
Total 91.5874 1.0000 1696.7872 1.0000 171.3330 1.0000
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* Specified by user.Licensed to: ENERFLEX LTD
ENERFLEX LTDBurlington, MAUSA
Case Name: E002100 TEG DEHY UNIT - 03PE.hsc
Unit Set: NewUser3
Date/Time: Fri Feb 05 17:04:24 2016
Material Stream: 1 (continued)Fluid Package: Glycol
Property Package: Glycol Package
COMPOSITION
Vapour Phase Phase Fraction 0.8018
COMPONENTS
MethaneEthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-OctaneBenzeneE-Benzeneo-XyleneTolueneH2OTEGlycolNitrogenCO2H2S
MOLAR FLOW (lbmole/hr)
17.48071.50340.85040.19540.19560.05510.02900.00010.00000.00000.00000.00000.00000.0000
52.28850.00000.06630.76800.0000
MOLE FRACTION
0.23810.02050.01160.00270.00270.00070.00040.00000.00000.00000.00000.00000.00000.00000.71210.00000.00090.01050.0000
MASS FLOW (lb/hr)
280.441245.206937.501811.356211.36623.97312.09190.01020.00280.00100.00000.00000.00000.0000
941.98250.00001.8583
33.79890.0000
MASS FRACTION
0.20480.03300.02740.00830.00830.00290.00150.00000.00000.00000.00000.00000.00000.00000.68780.00000.00140.02470.0000
LIQUID VOLUMEFLOW (barrel/day)
64.13828.70285.06801.38371.33440.43640.22750.00110.00030.00010.00000.00000.00000.0000
64.63040.00000.15782.80410.0000
LIQUID VOLUMEFRACTION
0.43080.05850.03400.00930.00900.00290.00150.00000.00000.00000.00000.00000.00000.00000.43410.00000.00110.01880.0000
Total 73.4325 1.0000 1369.5911 1.0000 148.8847 1.0000
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* Specified by user.Licensed to: ENERFLEX LTD
ENERFLEX LTDBurlington, MAUSA
Case Name: E002100 TEG DEHY UNIT - 03PE.hsc
Unit Set: NewUser3
Date/Time: Fri Feb 05 17:04:24 2016
Material Stream: 1 (continued)Fluid Package: Glycol
Property Package: Glycol Package
COMPOSITION
Aqueous Phase Phase Fraction 0.1982
COMPONENTS
MethaneEthanePropanei-Butanen-Butanei-Pentanen-Pentanen-Hexanen-Heptanen-OctaneBenzeneE-Benzeneo-XyleneTolueneH2OTEGlycolNitrogenCO2H2S
MOLAR FLOW (lbmole/hr)
0.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
18.15380.00100.00000.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.99990.00010.00000.00000.0000
MASS FLOW (lb/hr)
0.00110.00020.00010.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
327.04230.15080.00000.00160.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.99950.00050.00000.00000.0000
LIQUID VOLUMEFLOW (barrel/day)
0.00030.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
22.43870.00920.00000.00010.0000
LIQUID VOLUMEFRACTION
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.99960.00040.00000.00000.0000
Total 18.1549 1.0000 327.1961 1.0000 22.4483 1.0000
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* Specified by user.Licensed to: ENERFLEX LTD