Mass Heat of Vap. Phase Fraction Molar Basis Surface Tension Thermal Conductivity Viscosity Cv (SemiIdeal) Mass Cv (SemiIdeal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) CpCv (Ent. Method) Reid VP at 37.8 C True VP at 37.8 C Liq. Vol. Flow Sum(Std. Cond) Viscosity Index (kJkg) (dynecm) (WmK) (cP) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC)Mass Heat of Vap. Phase Fraction Molar Basis Surface Tension Thermal Conductivity Viscosity Cv (SemiIdeal) Mass Cv (SemiIdeal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) CpCv (Ent. Method) Reid VP at 37.8 C True VP at 37.8 C Liq. Vol. Flow Sum(Std. Cond) Viscosity Index (kJkg) (dynecm) (WmK) (cP) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC)Mass Heat of Vap. Phase Fraction Molar Basis Surface Tension Thermal Conductivity Viscosity Cv (SemiIdeal) Mass Cv (SemiIdeal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) CpCv (Ent. Method) Reid VP at 37.8 C True VP at 37.8 C Liq. Vol. Flow Sum(Std. Cond) Viscosity Index (kJkg) (dynecm) (WmK) (cP) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC)Mass Heat of Vap. Phase Fraction Molar Basis Surface Tension Thermal Conductivity Viscosity Cv (SemiIdeal) Mass Cv (SemiIdeal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) CpCv (Ent. Method) Reid VP at 37.8 C True VP at 37.8 C Liq. Vol. Flow Sum(Std. Cond) Viscosity Index (kJkg) (dynecm) (WmK) (cP) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC)Mass Heat of Vap. Phase Fraction Molar Basis Surface Tension Thermal Conductivity Viscosity Cv (SemiIdeal) Mass Cv (SemiIdeal) Cv Mass Cv Cv (Ent. Method) Mass Cv (Ent. Method) CpCv (Ent. Method) Reid VP at 37.8 C True VP at 37.8 C Liq. Vol. Flow Sum(Std. Cond) Viscosity Index (kJkg) (dynecm) (WmK) (cP) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC) (kJkgmoleC) (kJkgC)
Trang 1Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall0.000094.31200.016421.741e+005199.68345-12.731.370e+007199.1*
Liquid Phase1.000094.31200.016421.741e+005199.68345-12.731.370e+007199.1PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(MJ/m3)(MJ/m3)(kJ/kg)
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)
Overall106.07.575803.1216.778.71-0.1200202.71.9124.378e+0064.581e+0064.321e+004 -4.130e+0040.00000.00000.00000.00000.0000 -8.225202.73.882e+004872.16.020e-0028.642e-00310.34 -0.00001.0431.2893.406e+0040.3620874.1199.11.0000.1320
Liquid Phase
106.07.575803.1216.778.71-0.1200202.71.9124.378e+0064.581e+0064.321e+004 -4.130e+0041.0001.0001.000 -0.0000 -8.225202.73.882e+004872.16.020e-0028.642e-00310.34 -1.0431.289 -0.3620874.1199.11.0000.1320
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Trang 2Mass Heat of Vap
Phase Fraction [Molar Basis]
(kPa)(kPa)(m3/h)
Overall321.30.000021.120.12270.2907194.41.833157.21.482162.21.5301.2502.7232.723199.1-16.58
Liquid Phase
1.000021.120.12270.2907194.41.833157.21.482162.21.5301.2502.7232.723199.1 -COMPOSITION
MOLE FRACTION
0.94300.05550.00000.00070.00000.00070.00000.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.06370.00000.0000
MASS FRACTION
0.94430.05450.00000.00050.00000.00060.00000.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.13000.00000.0000
LIQUID VOLUMEFRACTION 0.94650.05230.00000.00050.00000.00070.00000.0000
MOLE FRACTION
0.94300.05550.00000.00070.00000.00070.00000.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.06370.00000.0000
MASS FRACTION
0.94430.05450.00000.00050.00000.00060.00000.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.13000.00000.0000
LIQUID VOLUMEFRACTION 0.94650.05230.00000.00050.00000.00070.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzene
MIXED
0.00000.0000 -0.0000
LIGHT
0.00000.0000 -0.0000
HEAVY
-
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Trang 3K VALUECOMPONENTS
EthyleneTolueneH2OMethane
MIXED
0.0000 -
-LIGHT
0.0000 -
-HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Inactive): 200.0 kPa
Flow Specification (Inactive) Molar: 1642 kgmole/h Mass: 1.741e+005 kg/h Std Ideal Liq Volume: 199.6 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000240.0*
170.0*
16421.741e+005199.67.276e+004136.21.195e+008199.1*
Vapour Phase1.0000240.0170.016421.741e+005199.67.276e+004136.21.195e+008199.1PROPERTIES
Overall106.04.117e-0024.3653.988e+004686.31.285
Vapour Phase
106.04.117e-0024.3653.988e+004686.31.285
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Trang 4CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall210.51.9854.378e+0064.581e+0064.321e+004 -4.130e+0041.0001.0001.0000.00000.00003.988e+0048.225210.53.882e+004872.1 -0.967910.34 -0.00001.0411.0473.450e+0042.373874.1199.10.000024.29325.41.0000 -2.906e-0021.036e-002202.21.907201.11.896 -2.7232.723199.1 -
Vapour Phase
210.51.9854.378e+0064.581e+0064.321e+004 -4.130e+0041.0001.0001.000 -0.00003.988e+0048.225210.53.882e+004872.1 -0.967910.34 -1.0411.047 -2.373874.1199.10.000024.29 -1.0000 -2.906e-0021.036e-002202.21.907201.11.896 -2.7232.723199.1 -
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Trang 5MOLE FRACTION
0.94300.05550.00000.00070.00000.00070.00000.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.06370.00000.0000
MASS FRACTION
0.94430.05450.00000.00050.00000.00060.00000.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.13000.00000.0000
LIQUID VOLUMEFRACTION 0.94650.05230.00000.00050.00000.00070.00000.0000
MOLE FRACTION
0.94300.05550.00000.00070.00000.00070.00000.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.06370.00000.0000
MASS FRACTION
0.94430.05450.00000.00050.00000.00060.00000.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.13000.00000.0000
LIQUID VOLUMEFRACTION 0.94650.05230.00000.00050.00000.00070.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Active): 170.0 kPa*
Flow Specification (Inactive) Molar: 1642 kgmole/h Mass: 1.741e+005 kg/h Std Ideal Liq Volume: 199.6 m3/h
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Trang 6User Variables
NOTES
Description
Property Package: Peng-Robinson
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000722.0*
170.0*
3000*
5.405e+00454.15-2.159e+005213.2-6.478e+00853.26*
Vapour Phase1.0000722.0170.030005.405e+00454.15-2.159e+005213.2-6.478e+00853.26PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Z Factor
(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(MJ/m3)(MJ/m3)(kJ/kg)
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
Overall18.022.056e-0020.37031.459e+005-1.199e+00411.8441.262.2900.00004.101e+0042276 -1.0001.0001.0000.00000.00001.459e+00555.4041.267.093e+004998.0 -0.9995
Vapour Phase
18.022.056e-0020.37031.459e+005-1.199e+00411.8441.262.2900.00004.101e+0042276 -1.0001.0001.000 -0.00001.459e+00555.4041.267.093e+004998.0 -0.9995
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Trang 7Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall
-0.00001.2521.2544.028e+00477.84101553.260.000048.6422361.0000 -8.603e-0022.883e-00232.951.82932.911.827 -6.4676.46753.2610.58
-Vapour Phase
-1.2521.254 -77.84101553.260.000048.64 -1.0000 -8.603e-0022.883e-00232.951.82932.911.827 -6.4676.46753.26 -COMPOSITION
MOLE FRACTION
0.00000.00000.00000.00000.0000
MASS FLOW (kg/h)0.00000.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION 0.00000.00000.00000.00000.0000
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Trang 8MOLE FRACTION
0.00001.00000.0000
MASS FLOW (kg/h)0.000054045.30140.0000
MASS FRACTION
0.00001.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.000054.15440.0000
LIQUID VOLUMEFRACTION 0.00001.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
-FEED TO
UTILITIES( No utilities reference this stream )PROCESS UTILITY
DYNAMICSPressure Specification (Active): 170.0 kPa*
Flow Specification (Active) Molar: 3000 kgmole/h* Mass: 5.405e+004 kg/h Std Ideal Liq Volume: 54.15 m3/h
User Variables
NOTES
Description
Property Package: Peng-Robinson
200.0*
123.4*
1.305e+004
Liquid Phase1.0000136.0200.0123.41.305e+004
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Trang 9Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall15.001.149e+004-20.271.418e+00614.96*
Liquid Phase
15.001.149e+004-20.271.418e+00614.96PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
Surface Tension
Thermal Conductivity
Viscosity
(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(MJ/m3)(MJ/m3)(kJ/kg)
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)
Overall105.87.190760.317.17108.6-0.1917221.62.0954.371e+0064.575e+0064.326e+004 -4.133e+0040.00000.00000.00000.00000.0000 -8.228221.62918870.14.768e-0038.177e-00310.35 -0.00001.0391.2813.411e+0040.2754872.414.961.0000.1391322.50.000016.770.11200.2094
Liquid Phase
105.87.190760.317.17108.6-0.1917221.62.0954.371e+0064.575e+0064.326e+004 -4.133e+0041.0001.0001.000 -0.0000 -8.228221.62918870.14.768e-0038.177e-00310.35 -1.0391.281 -0.2754872.414.961.0000.1391 -1.000016.770.11200.2094
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Trang 10Overall213.22.016173.01.636173.41.6401.2783.0093.01014.96-27.14
Liquid Phase
213.22.016173.01.636173.41.6401.2783.0093.01014.96 -COMPOSITION
MOLE FRACTION
0.98040.00000.00000.00980.00000.00980.00000.0000
MASS FLOW (kg/h)12846.08600.00000.000094.51310.0000111.49040.00000.0000
MASS FRACTION
0.98420.00000.00000.00720.00000.00850.00000.0000
LIQUID VOLUMEFLOW (m3/h)14.76510.00000.00000.10710.00000.12810.00000.0000
LIQUID VOLUMEFRACTION 0.98430.00000.00000.00710.00000.00850.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
0.0000 -0.0000 -0.0000 -
LIGHT
0.0000 -0.0000 -0.0000 -
HEAVY
-
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Trang 11UNIT OPERATIONSFEED TO
UTILITIES( No utilities reference this stream )PROCESS UTILITY
DYNAMICSPressure Specification (Active): 200.0 kPa*
Flow Specification (Active) Molar: 123.4 kgmole/h* Mass: 1.305e+004 kg/h Std Ideal Liq Volume: 15.00 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000550.0*
135.0*
46432.281e+005253.8-9.070e+004230.0-4.211e+008242.8*
Vapour Phase1.0000550.0135.046432.281e+005253.8-9.070e+004230.0-4.211e+008242.8PROPERTIES
(kgmole/m3)
Overall49.131.975e-0020.97032.351e+005-18464.682125.92.5641.548e+0061.646e+0063.351e+004 -
Vapour Phase
49.131.975e-0020.97032.351e+005-18464.682125.92.5641.548e+0061.646e+0063.351e+004 -
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Trang 12CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall
3.151e+0041.0001.0001.0000.00000.00002.351e+00518.30125.91.098e+005898.8 -0.998810.34 -0.00001.0711.0718.017e+00424.56939.5242.80.000050.6316321.0000 -6.702e-0022.383e-002117.62.394117.62.393 -6.882208.3242.85.995
-Vapour Phase
3.151e+0041.0001.0001.000 -0.00002.351e+00518.30125.91.098e+005898.8 -0.998810.34 -1.0711.071 -24.56939.5242.80.000050.63 -1.0000 -6.702e-0022.383e-002117.62.394117.62.393 -6.882208.3242.8 -COMPOSITION
MOLE FRACTION
0.33310.01990.00030.0003
MASS FLOW (kg/h)164217.98379627.42662.697494.5136
MASS FRACTION
0.71990.04220.00000.0004
LIQUID VOLUMEFLOW (m3/h)188.749110.59320.03860.1071
LIQUID VOLUMEFRACTION 0.74380.04170.00020.0004
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Trang 13MOLE FRACTION
0.00000.00030.64610.0000
MASS FLOW (kg/h)0.0002113.069454045.30140.0010
MASS FRACTION
0.00000.00050.23690.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.130054.15440.0000
LIQUID VOLUMEFRACTION 0.00000.00050.21340.0000
MOLE FRACTION
0.33310.01990.00030.00030.00000.00030.64610.0000
MASS FLOW (kg/h)164217.98379627.42662.697494.51360.0002113.069454045.30140.0010
MASS FRACTION
0.71990.04220.00000.00040.00000.00050.23690.0000
LIQUID VOLUMEFLOW (m3/h)188.749110.59320.03860.10710.00000.130054.15440.0000
LIQUID VOLUMEFRACTION 0.74380.04170.00020.00040.00000.00050.21340.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Active): 135.0 kPa*
Flow Specification (Inactive) Molar: 4643 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 253.8 m3/h
Trang 14Property Package: Peng-Robinson
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000267.0*
110.0*
47542.281e+005256.2-1.173e+005196.2-5.575e+008246.3*
Vapour Phase1.0000267.0110.047542.281e+005256.2-1.173e+005196.2-5.575e+008246.3PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
Overall47.982.461e-0021.1811.932e+005-24444.08898.102.0451.514e+0061.610e+0063.354e+004 -3.155e+0041.0001.0001.0000.00000.00001.932e+00518.5698.101.124e+005890.5 -0.995310.31 -0.00001.0931.095
Vapour Phase
47.982.461e-0021.1811.932e+005-24444.08898.102.0451.514e+0061.610e+0063.354e+004 -3.155e+0041.0001.0001.000 -0.00001.932e+00518.5698.101.124e+005890.5 -0.995310.31 -1.0931.095
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Trang 15Heat of Vap
Kinematic Viscosity
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall7.839e+00412.51926.0246.30.000040.6316341.0000 -3.810e-0021.478e-00289.791.87189.621.868 -353.21.802e+004246.3-2.547
Vapour Phase
12.51926.0246.30.000040.63 -1.0000 -3.810e-0021.478e-00289.791.87189.621.868 -353.21.802e+004246.3 -COMPOSITION
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
Trang 16K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Active): 110.0 kPa*
Flow Specification (Inactive) Molar: 4754 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 256.2 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000180.0*
95.00*
47542.281e+005256.2-1.254e+005181.1-5.960e+008246.3*
Vapour Phase1.0000180.095.0047542.281e+005256.2-1.254e+005181.1-5.960e+008246.3PROPERTIES
Molecular Weight
Molar Density (kgmole/m3)
Overall47.982.539e-002
Vapour Phase
47.982.539e-002
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Trang 17CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall1.2181.872e+005-26133.77487.901.8321.514e+0061.610e+0063.354e+004 -3.155e+0041.0001.0001.0000.00000.00001.872e+00518.5687.901.124e+005890.5 -0.993110.31 -0.00001.1041.1087.820e+0049.943926.0246.30.000039.3816301.0000 -2.904e-0021.211e-00279.581.65979.361.654 -353.21.802e+004246.3
Vapour Phase
1.2181.872e+005-26133.77487.901.8321.514e+0061.610e+0063.354e+004 -3.155e+0041.0001.0001.000 -0.00001.872e+00518.5687.901.124e+005890.5 -0.993110.31 -1.1041.108 -9.943926.0246.30.000039.38 -1.0000 -2.904e-0021.211e-00279.581.65979.361.654 -353.21.802e+004246.3
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Trang 18Viscosity Index
Overall-46.01
Vapour Phase
COMPOSITION
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
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Trang 19DYNAMICSPressure Specification (Active): 95.00 kPa*
Flow Specification (Inactive) Molar: 4754 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 256.2 m3/h
User Variables
NOTES
Description
Property Package: Peng-Robinson
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall0.041365.00*
80.00*
47542.281e+005256.2-1.742e+00548.03-8.283e+008246.3*
Vapour Phase0.041365.0080.00196.237637.124-6.929e+004147.9-1.359e+0074615
Liquid Phase0.341365.0080.0016231.715e+005196.099827.9611.620e+007195.6
Aqueous Phase
0.617465.0080.0029355.287e+00452.98-2.831e+00563.50-8.309e+00852.10PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(MJ/m3)(MJ/m3)(kJ/kg)
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)
Overall47.980.666131.967137-36311.001114.52.3861.514e+0061.610e+0063.354e+004 -3.155e+0042.781e-0021.650e-0020.96360.00000.0000687718.56114.5
Vapour Phase
19.192.852e-0020.54736877-36117.70843.912.2886.497e+0057.094e+0053.698e+004 -3.386e+0042.781e-0021.650e-0020.9636 -0.0000687727.5343.91
Liquid Phase
105.77.880832.6205.994.477.534e-002188.81.7874.356e+0064.555e+0064.311e+004 -4.122e+0040.76540.75172.885e-002 -0.0000 -8.277188.8
Aqueous Phase
18.0254.20976.554.15-1.572e+0043.52578.104.3350.34564.101e+0042276 -1.919e-0020.20680.23187.587e-003 -0.0000 -55.4078.10
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Trang 20Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall1.124e+005890.57.225e-002 -10.31 -0.00001.0781.0037.799e+004 -926.0246.30.95871.50116250.0413 -106.22.213114.12.378 -353.21.802e+0044863-8.601
Vapour Phase
4638528.3 -0.997612.87 -1.2341.236 -23.900.815446150.000035.06 -0.0413 -7.774e-0021.308e-00235.591.85535.511.851 -4615 -
Liquid Phase3.837e+004874.65.720e-0023.611e-00310.31 -1.0461.300 -0.4561876.7195.61.0000.1269 -0.341324.410.13090.3798180.51.708145.21.375152.31.4421.2393.77962.31195.6 -
Aqueous Phase6.940e+004998.01.504e-0025.250e-00447.59 -1.1191.166 -0.4402101552.101.0001.845e-002 -0.617465.060.65810.429869.793.87466.983.71864.033.5541.22043.2143.2152.10 -COMPOSITION
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
MOLE FRACTION
0.1054
MASS FLOW (kg/h)2194.7213
MASS FRACTION
0.5832
LIQUID VOLUMEFLOW (m3/h)2.5226
LIQUID VOLUMEFRACTION 0.3541
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Trang 21MOLE FRACTION
0.01070.56840.00060.00010.00030.31280.0017
MASS FLOW (kg/h)219.0192224.78538.62180.71854.93801105.40205.2824
MASS FRACTION
0.05820.05970.00230.00020.00130.29370.0014
LIQUID VOLUMEFLOW (m3/h)0.24103.21770.00980.00190.00571.10760.0176
LIQUID VOLUMEFRACTION 0.03380.45170.00140.00030.00080.15550.0025
MOLE FRACTION
0.87190.12400.00020.00070.00000.00090.00220.0000
MASS FLOW (kg/h)150216.432220953.47260.697388.02110.0465139.048065.23210.1015
MASS FRACTION
0.87610.12220.00000.00050.00000.00080.00040.0000
LIQUID VOLUMEFLOW (m3/h)172.656023.05540.01000.09980.00010.15980.06540.0003
LIQUID VOLUMEFRACTION 0.88070.11760.00010.00050.00000.00080.00030.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00001.00000.0000
MASS FLOW (kg/h)0.00000.00000.00850.00000.00000.000052874.66730.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00001.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.00000.00010.00000.00000.000052.98140.0000
LIQUID VOLUMEFRACTION 0.00000.00000.00000.00000.00000.00001.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
0.33950.242974012.276359.40.82520.48521209
LIGHT
0.12098.647e-00226670.8103127.90.2938140.2430.4
HEAVY
-3.980e+005 -0.31282.688e+007
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Trang 22UNIT OPERATIONSFEED TO
DYNAMICSPressure Specification (Active): 80.00 kPa*
Flow Specification (Inactive) Molar: 4754 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 256.2 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall0.000065.00*
200.0*
30005.405e+00454.15-2.831e+00563.50-8.493e+00853.26*
Aqueous Phase
1.000065.00200.030005.405e+00454.15-2.831e+00563.50-8.493e+00853.26PROPERTIES
(kgmole/m3)
Overall18.0254.20976.555.35-1.571e+0043.52578.104.3350.00004.101e+0042276 -
Aqueous Phase
18.0254.20976.555.35-1.571e+0043.52578.104.3350.00004.101e+0042276 -
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Trang 23CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall
-0.00000.00000.00000.00000.0000 -55.4078.107.093e+004998.01.537e-0021.312e-003 -0.00001.1191.1664.003e+0040.4402101553.261.0001.845e-00222220.000065.060.65810.429869.783.87466.983.718 -6.4676.46753.26-11.35
-Aqueous Phase
-1.0001.0001.000 -0.0000 -55.4078.107.093e+004998.01.537e-0021.312e-003 -1.1191.166 -0.4402101553.261.0001.845e-002 -1.000065.060.65810.429869.783.87466.983.718 -6.4676.46753.26 -COMPOSITION
MOLE FRACTION
0.00000.00000.00000.0000
MASS FLOW (kg/h)0.00000.00000.00000.0000
MASS FRACTION
0.00000.00000.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.00000.00000.0000
LIQUID VOLUMEFRACTION 0.00000.00000.00000.0000
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Trang 24MOLE FRACTION
0.00000.00001.00000.0000
MASS FLOW (kg/h)0.00000.000054045.30140.0000
MASS FRACTION
0.00000.00001.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.000054.15440.0000
LIQUID VOLUMEFRACTION 0.00000.00001.00000.0000
MOLE FRACTION
0.00000.00000.00000.00000.00000.00001.00000.0000
MASS FLOW (kg/h)0.00000.00000.00000.00000.00000.000054045.30140.0000
MASS FRACTION
0.00000.00000.00000.00000.00000.00001.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.00000.00000.00000.00000.000054.15440.0000
LIQUID VOLUMEFRACTION 0.00000.00000.00000.00000.00000.00001.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-0.0000 -
-LIGHT
-
-HEAVY
-0.0000 -UNIT OPERATIONS
LOGICAL CONNECTION
UTILITIES( No utilities reference this stream )PROCESS UTILITY
DYNAMICSPressure Specification (Active): 200.0 kPa*
Flow Specification (Inactive) Molar: 3000 kgmole/h Mass: 5.405e+004 kg/h Std Ideal Liq Volume: 54.15 m3/h
Trang 25Property Package: Peng-Robinson
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall0.000090.75200.0*
15211.613e+005184.98090-12.301.230e+007184.4*
Liquid Phase1.000090.75200.015211.613e+005184.98090-12.301.230e+007184.4PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
Overall106.07.606806.6199.976.29-0.1160201.11.8964.379e+0064.582e+0064.320e+004 -4.129e+0040.00000.00000.00000.00000.0000 -8.225201.13.595e+004872.25.553e-0028.690e-00310.34 -0.00001.0431.291
Liquid Phase
106.07.606806.6199.976.29-0.1160201.11.8964.379e+0064.582e+0064.320e+004 -4.129e+0041.0001.0001.000 -0.0000 -8.225201.13.595e+004872.25.553e-0028.690e-00310.34 -1.0431.291
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Trang 26Heat of Vap
Kinematic Viscosity
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall3.406e+0040.3715874.3184.41.0000.1315321.20.000021.500.12360.2996192.81.818155.81.469153.81.4501.3082.7002.700184.4-15.82
Liquid Phase
0.3715874.3184.41.0000.1315 -1.000021.500.12360.2996192.81.818155.81.469153.81.4501.3082.7002.700184.4 -COMPOSITION
MOLE FRACTION
0.94000.06000.00000.00000.00000.00000.00000.0000
MASS FLOW (kg/h)151752.20189502.69000.00000.00000.00001.50360.00000.0000
MASS FRACTION
0.94110.05890.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (m3/h)174.421210.45600.00000.00000.00000.00170.00000.0000
LIQUID VOLUMEFRACTION 0.94340.05660.00000.00000.00000.00000.00000.0000
MOLE FRACTION
0.94000.06000.00000.00000.00000.00000.00000.0000
MASS FLOW (kg/h)151752.20189502.69000.00000.00000.00001.50360.00000.0000
MASS FRACTION
0.94110.05890.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (m3/h)174.421210.45600.00000.00000.00000.00170.00000.0000
LIQUID VOLUMEFRACTION 0.94340.05660.00000.00000.00000.00000.00000.0000
Trang 27K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
0.00000.0000 -0.0000 -
LIGHT
0.00000.0000 -0.0000 -
HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Active): 200.0 kPa*
Flow Specification (Inactive) Molar: 1521 kgmole/h Mass: 1.613e+005 kg/h Std Ideal Liq Volume: 184.9 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall0.000090.75*
200.0*
1518*
1.610e+005184.68090-12.301.228e+007184.2*
Liquid Phase1.000090.75200.015181.610e+005184.68090-12.301.228e+007184.2PROPERTIES
Molecular Weight
Molar Density (kgmole/m3)
Overall106.07.606
Liquid Phase
106.07.606
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Trang 28CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall806.6199.676.29-0.1160201.11.8964.379e+0064.582e+0064.320e+004 -4.129e+0040.00000.00000.00000.00000.0000 -8.225201.13.590e+004872.25.545e-0028.690e-00310.34 -0.00001.0431.2913.406e+0040.3715874.3184.21.0000.1315321.20.000021.500.12360.2996192.81.818155.81.469161.11.5191.2482.7002.700184.2
Liquid Phase
806.6199.676.29-0.1160201.11.8964.379e+0064.582e+0064.320e+004 -4.129e+0041.0001.0001.000 -0.0000 -8.225201.13.590e+004872.25.545e-0028.690e-00310.34 -1.0431.291 -0.3715874.3184.21.0000.1315 -1.000021.500.12360.2996192.81.818155.81.469161.11.5191.2482.7002.700184.2
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Trang 29Viscosity Index
Overall-15.82
Liquid Phase
COMPOSITION
MOLE FRACTION
0.94000.06000.00000.00000.00000.00000.00000.0000
MASS FLOW (kg/h)151513.96249488.06390.00000.00000.00001.57330.00000.0000
MASS FRACTION
0.94110.05890.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFLOW (m3/h)174.147410.43990.00000.00000.00000.00180.00000.0000
LIQUID VOLUMEFRACTION 0.94340.05660.00000.00000.00000.00000.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
0.00000.0000 -0.0000 -
LIGHT
0.00000.0000 -0.0000 -
HEAVY
-UNIT OPERATIONS
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Trang 30DYNAMICSPressure Specification (Inactive): 200.0 kPa*
Flow Specification (Inactive) Molar: 1518 kgmole/h* Mass: 1.610e+005 kg/h Std Ideal Liq Volume: 184.6 m3/h
User Variables
NOTES
Description
Property Package: Peng-Robinson
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000355.0170.046422.281e+005253.7-1.138e+005196.0-5.284e+008242.8*
Vapour Phase1.0000355.0170.046422.281e+005253.7-1.138e+005196.0-5.284e+008242.8PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(MJ/m3)(MJ/m3)(kJ/kg)
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)
Overall49.143.270e-0021.6071.419e+005-23163.989109.62.2311.549e+0061.647e+0063.351e+004 -3.151e+0041.0001.0001.0000.00000.00001.419e+00518.29109.6
Vapour Phase
49.143.270e-0021.6071.419e+005-23163.989109.62.2311.549e+0061.647e+0063.351e+004 -3.151e+0041.0001.0001.000 -0.00001.419e+00518.29109.6
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Trang 31Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall1.097e+005898.9 -0.995410.34 -0.00001.0821.0844.020e+00410.76939.6242.80.000030.58818.01.0000 -4.561e-0021.729e-002101.32.062101.12.058 -2.7239.195242.82.791
Vapour Phase1.097e+005898.9 -0.995410.34 -1.0821.084 -10.76939.6242.80.000030.58 -1.0000 -4.561e-0021.729e-002101.32.062101.12.058 -2.7239.195242.8 -COMPOSITION
MOLE FRACTION
0.33350.01960.00000.00030.00000.00030.64630.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.063754045.30140.0000
MASS FRACTION
0.72060.04160.00000.00040.00000.00050.23690.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.130054.15440.0000
LIQUID VOLUMEFRACTION 0.74450.04110.00000.00040.00000.00050.21340.0000
MOLE FRACTION
0.3335
MASS FLOW (kg/h)164360.0484
MASS FRACTION
0.7206
LIQUID VOLUMEFLOW (m3/h)188.9124
LIQUID VOLUMEFRACTION 0.7445
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Trang 32MOLE FRACTION
0.01960.00000.00030.00000.00030.64630.0000
MASS FLOW (kg/h)9488.06390.000094.51310.0000113.063754045.30140.0000
MASS FRACTION
0.04160.00000.00040.00000.00050.23690.0000
LIQUID VOLUMEFLOW (m3/h)10.43990.00000.10710.00000.130054.15440.0000
LIQUID VOLUMEFRACTION 0.04110.00000.00040.00000.00050.21340.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Inactive): 170.0 kPa
Flow Specification (Inactive) Molar: 4642 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 253.7 m3/h
User Variables
NOTES
Description
Property Package: Peng-Robinson
CONDITIONS
Vapour / Phase Fraction
Overall1.0000
Vapour Phase1.0000
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Trang 33Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall354.9160.046422.281e+005253.7-1.138e+005196.5-5.284e+008242.8*
Vapour Phase
354.9160.046422.281e+005253.7-1.138e+005196.5-5.284e+008242.8PROPERTIES
CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
(kgmole/m3)(kg/m3)(m3/h)(kJ/kg)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(MJ/m3)(MJ/m3)(kJ/kg)
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
Overall49.143.077e-0021.5121.508e+005-23163.999109.62.2301.549e+0061.647e+0063.351e+004 -3.151e+0041.0001.0001.0000.00000.00001.508e+00518.29109.61.097e+005898.9 -0.995710.34 -0.00001.0821.0844.027e+00411.43939.6242.80.000032.50819.4
Vapour Phase
49.143.077e-0021.5121.508e+005-23163.999109.62.2301.549e+0061.647e+0063.351e+004 -3.151e+0041.0001.0001.000 -0.00001.508e+00518.29109.61.097e+005898.9 -0.995710.34 -1.0821.084 -11.43939.6242.80.000032.50 -
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Trang 34Overall1.0000 -4.559e-0021.729e-002101.32.061101.12.058 -2.7239.195242.83.073
Vapour Phase1.0000 -4.559e-0021.729e-002101.32.061101.12.058 -2.7239.195242.8 -COMPOSITION
MOLE FRACTION
0.33350.01960.00000.00030.00000.00030.64630.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.063754045.30140.0000
MASS FRACTION
0.72060.04160.00000.00040.00000.00050.23690.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.130054.15440.0000
LIQUID VOLUMEFRACTION 0.74450.04110.00000.00040.00000.00050.21340.0000
MOLE FRACTION
0.33350.01960.00000.00030.00000.00030.64630.0000
MASS FLOW (kg/h)164360.04849488.06390.000094.51310.0000113.063754045.30140.0000
MASS FRACTION
0.72060.04160.00000.00040.00000.00050.23690.0000
LIQUID VOLUMEFLOW (m3/h)188.912410.43990.00000.10710.00000.130054.15440.0000
LIQUID VOLUMEFRACTION 0.74450.04110.00000.00040.00000.00050.21340.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthylene
MIXED
-
-LIGHT
-
-HEAVY
-
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Trang 35K VALUECOMPONENTS
TolueneH2OMethane
MIXED
-
-LIGHT
-
-HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Inactive): 160.0 kPa
Flow Specification (Inactive) Molar: 4642 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 253.7 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall1.0000526.4125.047542.281e+005256.2-8.858e+004238.2-4.211e+008246.3*
Vapour Phase1.0000526.4125.047542.281e+005256.2-8.858e+004238.2-4.211e+008246.3
Aqueous Phase
0.0000526.4125.00.00000.00000.0000-8.858e+004238.20.00000.0000PROPERTIES
Overall47.981.883e-0020.90332.525e+005-18464.964121.5
Vapour Phase
47.981.883e-0020.90332.525e+005-18464.964121.5
Aqueous Phase
47.981.883e-0020.90330.0000-18464.964121.5
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Trang 36CO2 App ML Con
CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kgmole/m3)(kgmol/kg)(kJ/kg)
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall2.5331.514e+0061.610e+0063.354e+004 -3.155e+0041.0001.0001.0000.00000.00002.525e+00518.56121.51.124e+005890.50.0000 -10.31 -0.00001.0731.0747.855e+00425.93926.0246.30.000053.1216371.0000 -6.698e-0022.342e-002113.22.359113.12.358 -353.21.802e+004246.36.121
Vapour Phase
2.5331.514e+0061.610e+0063.354e+004 -3.155e+0041.0001.0001.000 -0.00002.525e+00518.56121.51.124e+005890.5 -0.998810.31 -1.0731.074 -25.93926.0246.30.000053.12 -1.0000 -6.698e-0022.342e-002113.22.359113.12.358 -353.21.802e+004246.3 -
Aqueous Phase
2.5331.514e+0061.610e+0063.355e+004 -3.155e+004 -0.00000.0000 -0.0000 -18.56121.50.0000890.50.00000.998810.31 -1.0731.074 -1.246926.00.00001.00053.12 -0.00000.00000.11821.126e-003113.22.359113.12.358 -353.21.802e+0040.0000 -
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Trang 37MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)152411.153521172.4917225.491096.64300.7650143.986054045.30145.3840
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)175.178623.29643.22780.10950.00200.165554.15440.0180
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
MOLE FRACTION
0.30200.04280.02350.00030.00000.00030.63110.0001
MASS FLOW (kg/h)0.00000.00000.00000.00000.00000.00000.00000.0000
MASS FRACTION
0.66820.09280.00100.00040.00000.00060.23690.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.00000.00000.00000.00000.00000.00000.0000
LIQUID VOLUMEFRACTION 0.68390.09090.01260.00040.00000.00060.21140.0001
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
1.0001.0001.0001.0001.0001.0001.0001.000
LIGHT
-
-HEAVY
1.0001.0001.0001.0001.0001.0001.0001.000
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Trang 38UNIT OPERATIONSFEED TO
DYNAMICSPressure Specification (Inactive): 125.0 kPa
Flow Specification (Inactive) Molar: 4754 kgmole/h Mass: 2.281e+005 kg/h Std Ideal Liq Volume: 256.2 m3/h
Std Ideal Liq Vol Flow (m3/h)
Molar Enthalpy (kJ/kgmole)
Molar Entropy (kJ/kgmole-C)
Liq Vol Flow @Std Cond (m3/h)
Overall0.000070.1645.003.093272.00.31113.208e+004-91.779.922e+0040.3093*
Liquid Phase1.000070.1645.003.093272.00.31113.208e+004-91.779.922e+0040.3093PROPERTIES
(kgmole/m3)
Overall87.939.376824.40.3299364.8-1.044154.01.7513.594e+0063.746e+0064.260e+004 -
Liquid Phase
87.939.376824.40.3299364.8-1.044154.01.7513.594e+0063.746e+0064.260e+004 -
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Trang 39CO2 App WT Con
LHV Mass Basis (Std)
Phase Fraction [Vol Basis]
Phase Fraction [Mass Basis]
Phase Fraction [Act Vol Basis]
Partial Pressure of CO2
Cost Based on Flow
Act Gas Flow
Avg Liq Density
Specific Heat
Std Gas Flow
Std Ideal Liq Mass Density
Act Liq Flow
Liq Mass Density (Std Cond)
Liq Vol Flow (Std Cond)
Liquid Fraction
Molar Volume
Mass Heat of Vap
Phase Fraction [Molar Basis]
(kPa)(Cost/s)(ACT_m3/h)(kgmole/m3)(kJ/kgmole-C)(STD_m3/h)(kg/m3)(m3/s)
(kPa)
(kJ/kgmole)(cSt)(kg/m3)(m3/h)
(m3/kgmole)(kJ/kg)
(dyne/cm)(W/m-K)(cP)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)(kJ/kgmole-C)(kJ/kg-C)
(kPa)(kPa)(m3/h)
Overall
4.087e+0040.00000.00000.00000.00000.0000 -9.943154.073.13874.39.164e-0051.681e-00310.01 -0.00001.0571.4823.488e+0040.4203879.30.30931.0000.1067396.60.000022.500.12280.3465145.71.656103.91.181 -13.2913.300.3093-12.48
-Liquid Phase
4.087e+0041.0001.0001.000 -0.0000 -9.943154.073.13874.39.164e-0051.681e-00310.01 -1.0571.482 -0.4203879.30.30931.0000.1067 -1.000022.500.12280.3465145.71.656103.91.181 -13.2913.300.3093 -COMPOSITION
MOLE FRACTION
0.10000.00000.00000.4000
MASS FLOW (kg/h)32.85270.00080.000096.6430
MASS FRACTION
0.12080.00000.00000.3553
LIQUID VOLUMEFLOW (m3/h)0.03780.00000.00000.1095
LIQUID VOLUMEFRACTION 0.12140.00000.00000.3522
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Trang 40MOLE FRACTION
0.00000.49990.00000.0000
MASS FLOW (kg/h)0.0000142.48240.00000.0000
MASS FRACTION
0.00000.52390.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.00000.16380.00000.0000
LIQUID VOLUMEFRACTION 0.00000.52640.00000.0000
MOLE FRACTION
0.10000.00000.00000.40000.00000.49990.00000.0000
MASS FLOW (kg/h)32.85270.00080.000096.64300.0000142.48240.00000.0000
MASS FRACTION
0.12080.00000.00000.35530.00000.52390.00000.0000
LIQUID VOLUMEFLOW (m3/h)0.03780.00000.00000.10950.00000.16380.00000.0000
LIQUID VOLUMEFRACTION 0.12140.00000.00000.35220.00000.52640.00000.0000
K VALUECOMPONENTS
E-BenzeneStyreneHydrogenBenzeneEthyleneTolueneH2OMethane
MIXED
0.00000.0000 -0.0000 -0.0000 -
LIGHT
0.00000.0000 -0.0000 -0.0000 -
HEAVY
-UNIT OPERATIONS
DYNAMICSPressure Specification (Inactive): 45.00 kPa
Flow Specification (Inactive) Molar: 3.093 kgmole/h Mass: 272.0 kg/h Std Ideal Liq Volume: 0.3111 m3/h