Thông số dòng và tính toán thiết bị trong hysys

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)

1 LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: Basis-1 Property Package: Peng-Robinson CONDITIONS 10 Overall 11 12 Vapour / Phase Fraction 13 Temperature: 14 Pressure: 15 Liquid Phase 0.0000 1.0000 (C) 94.31 94.31 (kPa) 200.0 200.0 Molar Flow (kgmole/h) 1642 1642 16 Mass Flow (kg/h) 1.741e+005 1.741e+005 17 Std Ideal Liq Vol Flow 199.6 18 Molar Enthalpy 19 Molar Entropy 20 Heat Flow 21 Liq Vol Flow @Std Cond (m3/h) 199.6 (kJ/kgmole) 8345 8345 (kJ/kgmole-C) -12.73 -12.73 (kJ/h) 1.370e+007 1.370e+007 (m3/h) 199.1 * 22 199.1 PROPERTIES 23 Overall 24 25 Molecular Weight 26 Molar Density 27 Mass Density 28 Liquid Phase 106.0 106.0 (kgmole/m3) 7.575 7.575 (kg/m3) 803.1 803.1 Act Volume Flow (m3/h) 216.7 216.7 29 Mass Enthalpy (kJ/kg) 78.71 78.71 30 Mass Entropy (kJ/kg-C) -0.1200 -0.1200 31 Heat Capacity (kJ/kgmole-C) 202.7 202.7 32 Mass Heat Capacity (kJ/kg-C) 1.912 1.912 33 LHV Vol Basis (Std) (MJ/m3) 4.378e+006 4.378e+006 34 HHV Vol Basis (Std) (MJ/m3) 4.581e+006 4.581e+006 35 HHV Mass Basis (Std) (kJ/kg) 4.321e+004 4.321e+004 36 CO2 Loading - - 37 CO2 App ML Con (kgmole/m3) - - 38 CO2 App WT Con (kgmol/kg) - - 39 LHV Mass Basis (Std) (kJ/kg) 4.130e+004 4.130e+004 40 Phase Fraction [Vol Basis] 0.0000 1.000 41 Phase Fraction [Mass Basis] 0.0000 1.000 42 Phase Fraction [Act Vol Basis] 0.0000 1.000 43 Partial Pressure of CO2 44 Cost Based on Flow 45 Act Gas Flow (ACT_m3/h) - - 46 Avg Liq Density (kgmole/m3) 8.225 8.225 47 Specific Heat 48 Std Gas Flow 49 Std Ideal Liq Mass Density 50 Act Liq Flow 51 Z Factor 52 Watson K 53 User Property 54 Partial Pressure of H2S 55 Cp/(Cp - R) 56 Cp/Cv 57 Heat of Vap 58 Kinematic Viscosity 59 Liq Mass Density (Std Cond) 60 Liq Vol Flow (Std Cond) 61 Liquid Fraction 62 Molar Volume 63 Fluid Package: 0.0000 - (Cost/s) 0.0000 0.0000 (kJ/kgmole-C) 202.7 202.7 (STD_m3/h) 3.882e+004 3.882e+004 Aspen Technology Inc Licensed to: LEGENDS (kPa) (kg/m3) 872.1 872.1 (m3/s) 6.020e-002 6.020e-002 8.642e-003 8.642e-003 10.34 10.34 - - (kPa) 0.0000 - 1.043 1.043 1.289 1.289 (kJ/kgmole) 3.406e+004 - (cSt) 0.3620 0.3620 (kg/m3) 874.1 874.1 (m3/h) 199.1 199.1 (m3/kgmole) 1.000 1.000 0.1320 0.1320 Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Basis-1 Property Package: Peng-Robinson PROPERTIES 10 Overall 11 12 Mass Heat of Vap 13 Phase Fraction [Molar Basis] 14 Surface Tension 15 Thermal Conductivity 16 Viscosity 17 Cv (Semi-Ideal) (kJ/kg) 18 Mass Cv (Semi-Ideal) 19 Cv 20 Mass Cv 21 Cv (Ent Method) 22 Mass Cv (Ent Method) 23 Cp/Cv (Ent Method) 24 Reid VP at 37.8 C 25 True VP at 37.8 C Liquid Phase 321.3 - 0.0000 1.0000 (dyne/cm) 21.12 21.12 (W/m-K) 0.1227 0.1227 (cP) 0.2907 0.2907 (kJ/kgmole-C) 194.4 194.4 (kJ/kg-C) 1.833 1.833 (kJ/kgmole-C) 157.2 157.2 (kJ/kg-C) 1.482 1.482 (kJ/kgmole-C) 162.2 162.2 (kJ/kg-C) 1.530 1.530 1.250 1.250 (kPa) 2.723 2.723 (kPa) 2.723 2.723 26 Liq Vol Flow - Sum(Std Cond) (m3/h) 199.1 199.1 27 Viscosity Index -16.58 - 28 COMPOSITION 29 30 Overall Phase 31 32 Fluid Package: COMPONENTS 33 34 E-Benzene 35 Styrene 36 MOLAR FLOW (kgmole/h) MOLE FRACTION MASS FLOW (kg/h) Vapour Fraction 0.0000 MASS FRACTION LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 1548.1420 0.9430 164360.0484 0.9443 188.9124 0.9465 91.0982 0.0555 9488.0639 0.0545 10.4399 0.0523 Hydrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 37 Benzene 1.2100 0.0007 94.5131 0.0005 0.1071 0.0005 38 Ethylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 39 Toluene 1.2271 0.0007 113.0637 0.0006 0.1300 0.0007 40 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 41 Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 42 Total 1641.6774 1.0000 174055.6891 1.0000 199.5894 1.0000 43 Liquid Phase 44 45 COMPONENTS 46 47 E-Benzene 48 Styrene 49 MOLAR FLOW (kgmole/h) MOLE FRACTION MASS FLOW (kg/h) Phase Fraction 1.000 MASS FRACTION LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 1548.1420 0.9430 164360.0484 0.9443 188.9124 0.9465 91.0982 0.0555 9488.0639 0.0545 10.4399 0.0523 Hydrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 50 Benzene 1.2100 0.0007 94.5131 0.0005 0.1071 0.0005 51 Ethylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 52 Toluene 1.2271 0.0007 113.0637 0.0006 0.1300 0.0007 53 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 54 Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 55 Total 1641.6774 1.0000 174055.6891 1.0000 199.5894 1.0000 56 K VALUE 57 58 COMPONENTS MIXED LIGHT HEAVY 59 E-Benzene 0.0000 0.0000 - 60 Styrene 0.0000 0.0000 - 61 Hydrogen - - - 62 Benzene 0.0000 0.0000 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) - Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Fluid Package: Basis-1 Property Package: Peng-Robinson K VALUE 10 COMPONENTS 11 MIXED LIGHT HEAVY 12 Ethylene - - - 13 Toluene 0.0000 0.0000 - 14 H2O - - - 15 Methane - - - 16 UNIT OPERATIONS 17 FEED TO 18 19 PRODUCT FROM Heater: E-100 Mixer: LOGICAL CONNECTION MIX-100 20 UTILITIES 21 ( No utilities reference this stream ) 22 23 PROCESS UTILITY 24 25 26 DYNAMICS 27 28 Pressure Specification (Inactive): 29 Flow Specification (Inactive) 200.0 kPa Molar: 1642 kgmole/h 30 Mass: 1.741e+005 kg/h Std Ideal Liq Volume: 199.6 m3/h User Variables 31 32 NOTES 33 34 35 Description 36 37 38 Material Stream: 39 40 41 Fluid Package: Basis-1 Property Package: Peng-Robinson CONDITIONS 42 Overall 43 Vapour Phase 44 Vapour / Phase Fraction 1.0000 45 Temperature: 1.0000 46 Pressure: 47 Molar Flow (kgmole/h) 1642 1642 48 Mass Flow (kg/h) 1.741e+005 1.741e+005 49 Std Ideal Liq Vol Flow 50 Molar Enthalpy 51 Molar Entropy 52 Heat Flow 53 Liq Vol Flow @Std Cond (C) 240.0 * 240.0 (kPa) 170.0 * 170.0 (m3/h) 199.6 199.6 (kJ/kgmole) 7.276e+004 7.276e+004 (kJ/kgmole-C) 136.2 136.2 (kJ/h) 1.195e+008 1.195e+008 (m3/h) 199.1 * 54 199.1 PROPERTIES 55 Overall 56 Vapour Phase 57 Molecular Weight 58 Molar Density (kgmole/m3) 59 Mass Density (kg/m3) 4.365 4.365 60 Act Volume Flow (m3/h) 3.988e+004 3.988e+004 61 Mass Enthalpy (kJ/kg) 686.3 686.3 62 Mass Entropy (kJ/kg-C) 1.285 1.285 63 Aspen Technology Inc Licensed to: LEGENDS 106.0 106.0 4.117e-002 4.117e-002 Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Fluid Package: Basis-1 Property Package: Peng-Robinson PROPERTIES 10 Overall 11 12 Heat Capacity 13 Vapour Phase (kJ/kgmole-C) 210.5 Mass Heat Capacity (kJ/kg-C) 1.985 210.5 1.985 14 LHV Vol Basis (Std) (MJ/m3) 4.378e+006 4.378e+006 15 HHV Vol Basis (Std) (MJ/m3) 4.581e+006 4.581e+006 16 HHV Mass Basis (Std) (kJ/kg) 4.321e+004 4.321e+004 17 CO2 Loading - - 18 CO2 App ML Con (kgmole/m3) - - 19 CO2 App WT Con (kgmol/kg) - - 20 LHV Mass Basis (Std) (kJ/kg) 4.130e+004 4.130e+004 21 Phase Fraction [Vol Basis] 1.000 1.000 22 Phase Fraction [Mass Basis] 1.000 1.000 23 Phase Fraction [Act Vol Basis] 1.000 1.000 24 Partial Pressure of CO2 25 Cost Based on Flow 26 27 28 Specific Heat 29 Std Gas Flow 30 Std Ideal Liq Mass Density 31 Act Liq Flow 32 Z Factor 33 Watson K 34 User Property 35 Partial Pressure of H2S 36 Cp/(Cp - R) 37 Cp/Cv 38 Heat of Vap 39 Kinematic Viscosity 40 Liq Mass Density (Std Cond) 41 Liq Vol Flow (Std Cond) 42 Liquid Fraction 43 Molar Volume 44 Mass Heat of Vap 45 Phase Fraction [Molar Basis] 46 Surface Tension 47 Thermal Conductivity 48 Viscosity 49 Cv (Semi-Ideal) 50 Mass Cv (Semi-Ideal) 51 Cv 52 Mass Cv 53 Cv (Ent Method) 54 Mass Cv (Ent Method) 55 Cp/Cv (Ent Method) 56 Reid VP at 37.8 C 57 True VP at 37.8 C 58 59 Viscosity Index (kPa) 0.0000 - (Cost/s) 0.0000 0.0000 Act Gas Flow (ACT_m3/h) 3.988e+004 3.988e+004 Avg Liq Density (kgmole/m3) 8.225 8.225 (kJ/kgmole-C) 210.5 210.5 (STD_m3/h) 3.882e+004 3.882e+004 (kg/m3) 872.1 872.1 (m3/s) - - 0.9679 0.9679 10.34 10.34 - - (kPa) 0.0000 - 1.041 1.041 1.047 1.047 (kJ/kgmole) 3.450e+004 - (cSt) 2.373 2.373 (kg/m3) 874.1 874.1 (m3/h) 199.1 199.1 0.0000 0.0000 (m3/kgmole) 24.29 24.29 (kJ/kg) 325.4 - 1.0000 1.0000 (dyne/cm) - - (W/m-K) 2.906e-002 2.906e-002 (cP) 1.036e-002 1.036e-002 (kJ/kgmole-C) 202.2 202.2 (kJ/kg-C) 1.907 1.907 (kJ/kgmole-C) 201.1 201.1 (kJ/kg-C) 1.896 1.896 (kJ/kgmole-C) - - (kJ/kg-C) - - - - (kPa) 2.723 2.723 (kPa) 2.723 2.723 Liq Vol Flow - Sum(Std Cond) (m3/h) 199.1 199.1 - - 60 61 62 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Basis-1 Property Package: Peng-Robinson COMPOSITION 10 11 Overall Phase 12 13 Fluid Package: COMPONENTS MOLAR FLOW (kgmole/h) 14 15 E-Benzene 16 Styrene 17 MOLE FRACTION MASS FLOW (kg/h) Vapour Fraction 1.0000 MASS FRACTION LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 1548.1420 0.9430 164360.0484 0.9443 188.9124 0.9465 91.0982 0.0555 9488.0639 0.0545 10.4399 0.0523 Hydrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 18 Benzene 1.2100 0.0007 94.5131 0.0005 0.1071 0.0005 19 Ethylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 20 Toluene 1.2271 0.0007 113.0637 0.0006 0.1300 0.0007 21 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 22 Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 23 Total 1641.6774 1.0000 174055.6891 1.0000 199.5894 1.0000 24 Vapour Phase 25 26 COMPONENTS MOLAR FLOW (kgmole/h) 27 28 E-Benzene 29 Styrene 30 MOLE FRACTION MASS FLOW (kg/h) Phase Fraction 1.000 MASS FRACTION LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 1548.1420 0.9430 164360.0484 0.9443 188.9124 0.9465 91.0982 0.0555 9488.0639 0.0545 10.4399 0.0523 Hydrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 31 Benzene 1.2100 0.0007 94.5131 0.0005 0.1071 0.0005 32 Ethylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 33 Toluene 1.2271 0.0007 113.0637 0.0006 0.1300 0.0007 34 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 35 Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 36 Total 1641.6774 1.0000 174055.6891 1.0000 199.5894 1.0000 37 K VALUE 38 COMPONENTS 39 MIXED LIGHT HEAVY 40 E-Benzene - - - 41 Styrene - - - 42 Hydrogen - - - 43 Benzene - - - 44 Ethylene - - - 45 Toluene - - - 46 H2O - - - 47 Methane - - - 48 UNIT OPERATIONS 49 FEED TO 50 51 Mixer: PRODUCT FROM MIX-101 52 Heater: LOGICAL CONNECTION E-100 UTILITIES 53 ( No utilities reference this stream ) 54 55 PROCESS UTILITY 56 57 58 DYNAMICS 59 60 Pressure Specification (Active): 61 Flow Specification (Inactive) 170.0 kPa * Molar: 1642 kgmole/h Mass: 1.741e+005 kg/h Std Ideal Liq Volume: 199.6 m3/h 62 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Fluid Package: Basis-1 Property Package: Peng-Robinson Fluid Package: Basis-1 Property Package: Peng-Robinson User Variables 10 11 NOTES 12 13 14 Description 15 16 17 Material Stream: 18 19 20 CONDITIONS 21 Overall 22 23 Vapour / Phase Fraction 24 Temperature: 25 Pressure: 26 Vapour Phase 1.0000 1.0000 (C) 722.0 * 722.0 (kPa) 170.0 * 170.0 Molar Flow (kgmole/h) 3000 * 27 Mass Flow (kg/h) 28 Std Ideal Liq Vol Flow 29 Molar Enthalpy 30 Molar Entropy 31 Heat Flow 32 Liq Vol Flow @Std Cond 5.405e+004 3000 5.405e+004 (m3/h) 54.15 54.15 (kJ/kgmole) -2.159e+005 -2.159e+005 (kJ/kgmole-C) 213.2 213.2 (kJ/h) -6.478e+008 -6.478e+008 (m3/h) 53.26 * 33 53.26 PROPERTIES 34 Overall 35 Vapour Phase 36 Molecular Weight 37 Molar Density (kgmole/m3) 38 Mass Density (kg/m3) 0.3703 0.3703 39 Act Volume Flow (m3/h) 1.459e+005 1.459e+005 40 Mass Enthalpy (kJ/kg) -1.199e+004 -1.199e+004 41 Mass Entropy (kJ/kg-C) 11.84 11.84 42 Heat Capacity (kJ/kgmole-C) 41.26 41.26 43 Mass Heat Capacity (kJ/kg-C) 2.290 2.290 44 LHV Vol Basis (Std) (MJ/m3) 0.0000 0.0000 45 HHV Vol Basis (Std) (MJ/m3) 4.101e+004 4.101e+004 46 HHV Mass Basis (Std) (kJ/kg) 2276 2276 47 CO2 Loading - - 48 CO2 App ML Con (kgmole/m3) - - 49 CO2 App WT Con (kgmol/kg) - - 50 LHV Mass Basis (Std) (kJ/kg) - - 51 Phase Fraction [Vol Basis] 1.000 1.000 52 Phase Fraction [Mass Basis] 1.000 1.000 53 Phase Fraction [Act Vol Basis] 1.000 1.000 54 Partial Pressure of CO2 55 Cost Based on Flow 56 57 58 Specific Heat 59 Std Gas Flow 60 Std Ideal Liq Mass Density 61 Act Liq Flow 62 63 18.02 18.02 2.056e-002 2.056e-002 (kPa) 0.0000 - (Cost/s) 0.0000 0.0000 Act Gas Flow (ACT_m3/h) 1.459e+005 1.459e+005 Avg Liq Density (kgmole/m3) 55.40 55.40 (kJ/kgmole-C) 41.26 41.26 (STD_m3/h) 7.093e+004 7.093e+004 (kg/m3) 998.0 998.0 (m3/s) - - Z Factor 0.9995 0.9995 Aspen Technology Inc Aspen HYSYS Version 7.3 (25.0.0.7336) Licensed to: LEGENDS Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Basis-1 Property Package: Peng-Robinson PROPERTIES 10 Overall 11 Vapour Phase 12 Watson K - - 13 User Property - - 14 Partial Pressure of H2S 15 Cp/(Cp - R) 16 Cp/Cv 17 Heat of Vap 18 Kinematic Viscosity 19 Liq Mass Density (Std Cond) 20 Liq Vol Flow (Std Cond) 21 Liquid Fraction 22 Molar Volume 23 Mass Heat of Vap 24 Phase Fraction [Molar Basis] 25 Surface Tension 26 Thermal Conductivity 27 Viscosity 28 Cv (Semi-Ideal) 29 Mass Cv (Semi-Ideal) 30 Cv 31 Mass Cv 32 Cv (Ent Method) 33 Mass Cv (Ent Method) 34 Cp/Cv (Ent Method) 35 Reid VP at 37.8 C 36 True VP at 37.8 C 37 38 Viscosity Index (kPa) 0.0000 - 1.252 1.252 1.254 1.254 (kJ/kgmole) 4.028e+004 - (cSt) 77.84 77.84 (kg/m3) 1015 1015 (m3/h) 53.26 53.26 0.0000 0.0000 (m3/kgmole) 48.64 48.64 (kJ/kg) 2236 - 1.0000 1.0000 (dyne/cm) - - (W/m-K) 8.603e-002 8.603e-002 (cP) 2.883e-002 2.883e-002 (kJ/kgmole-C) 32.95 32.95 (kJ/kg-C) 1.829 1.829 (kJ/kgmole-C) 32.91 32.91 (kJ/kg-C) 1.827 1.827 (kJ/kgmole-C) - - (kJ/kg-C) - - - - (kPa) 6.467 6.467 (kPa) 6.467 6.467 Liq Vol Flow - Sum(Std Cond) (m3/h) 53.26 53.26 10.58 - 39 COMPOSITION 40 41 Overall Phase 42 43 Fluid Package: COMPONENTS 44 MOLAR FLOW (kgmole/h) MOLE FRACTION MASS FLOW (kg/h) Vapour Fraction MASS FRACTION LIQUID VOLUME FLOW (m3/h) 1.0000 LIQUID VOLUME FRACTION 45 E-Benzene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 46 Styrene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 47 Hydrogen 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 48 Benzene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 49 Ethylene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 50 Toluene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 51 H2O 3000.0000 * 1.0000 * 54045.3014 * 1.0000 * 54.1544 * 1.0000 * 52 Methane 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 53 Total 3000.0000 1.0000 54 1.0000 Vapour Phase 55 56 54045.3014 COMPONENTS 57 MOLAR FLOW (kgmole/h) MOLE FRACTION MASS FLOW (kg/h) 54.1544 1.0000 Phase Fraction 1.000 MASS FRACTION LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 58 E-Benzene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 59 Styrene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 60 Hydrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 61 Benzene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 62 Ethylene 0.0000 0.0000 0.0000 0.0000 0.0000 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) 0.0000 Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Basis-1 Property Package: Peng-Robinson COMPOSITION 10 11 Vapour Phase (continued) 12 13 Fluid Package: COMPONENTS MOLAR FLOW (kgmole/h) 14 15 Toluene 16 H2O 17 Methane 18 Total MOLE FRACTION MASS FLOW (kg/h) Phase Fraction MASS FRACTION 1.000 LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 3000.0000 1.0000 54045.3014 1.0000 54.1544 1.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 3000.0000 1.0000 54045.3014 1.0000 54.1544 1.0000 19 K VALUE 20 COMPONENTS 21 MIXED LIGHT HEAVY 22 E-Benzene - - - 23 Styrene - - - 24 Hydrogen - - - 25 Benzene - - - 26 Ethylene - - - 27 Toluene - - - 28 H2O - - - 29 Methane - - - 30 UNIT OPERATIONS 31 FEED TO 32 33 PRODUCT FROM Mixer: LOGICAL CONNECTION MIX-101 34 UTILITIES 35 ( No utilities reference this stream ) 36 37 PROCESS UTILITY 38 39 40 DYNAMICS 41 42 Pressure Specification (Active): 43 Flow Specification (Active) 170.0 kPa * Molar: 3000 kgmole/h * 44 Mass: 5.405e+004 kg/h Std Ideal Liq Volume: 54.15 m3/h User Variables 45 46 NOTES 47 48 49 Description 50 51 52 Material Stream: 53 54 55 Basis-1 Property Package: Peng-Robinson CONDITIONS 56 Overall 57 58 Vapour / Phase Fraction 59 Temperature: 60 Pressure: 61 62 63 Fluid Package: Liquid Phase 0.0000 1.0000 (C) 136.0 * 136.0 (kPa) 200.0 * 200.0 Molar Flow (kgmole/h) 123.4 * Mass Flow (kg/h) Aspen Technology Inc Licensed to: LEGENDS 1.305e+004 123.4 1.305e+004 Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Fluid Package: Basis-1 Property Package: Peng-Robinson CONDITIONS 10 Overall 11 12 Std Ideal Liq Vol Flow 13 Molar Enthalpy 14 Molar Entropy 15 Heat Flow 16 Liq Vol Flow @Std Cond Liquid Phase (m3/h) 15.00 15.00 (kJ/kgmole) 1.149e+004 1.149e+004 (kJ/kgmole-C) -20.27 -20.27 (kJ/h) 1.418e+006 1.418e+006 (m3/h) 14.96 * 17 14.96 PROPERTIES 18 Overall 19 20 Molecular Weight 21 Molar Density 22 Mass Density 23 Liquid Phase 105.8 105.8 (kgmole/m3) 7.190 7.190 (kg/m3) 760.3 760.3 Act Volume Flow (m3/h) 17.17 17.17 24 Mass Enthalpy (kJ/kg) 108.6 108.6 25 Mass Entropy (kJ/kg-C) -0.1917 -0.1917 26 Heat Capacity (kJ/kgmole-C) 221.6 221.6 27 Mass Heat Capacity (kJ/kg-C) 2.095 2.095 28 LHV Vol Basis (Std) (MJ/m3) 4.371e+006 4.371e+006 29 HHV Vol Basis (Std) (MJ/m3) 4.575e+006 4.575e+006 30 HHV Mass Basis (Std) (kJ/kg) 4.326e+004 4.326e+004 31 CO2 Loading - - 32 CO2 App ML Con (kgmole/m3) - - 33 CO2 App WT Con (kgmol/kg) - - 34 LHV Mass Basis (Std) (kJ/kg) 4.133e+004 4.133e+004 35 Phase Fraction [Vol Basis] 0.0000 1.000 36 Phase Fraction [Mass Basis] 0.0000 1.000 37 Phase Fraction [Act Vol Basis] 0.0000 1.000 38 Partial Pressure of CO2 39 Cost Based on Flow 40 Act Gas Flow (ACT_m3/h) - - 41 Avg Liq Density (kgmole/m3) 8.228 8.228 42 Specific Heat (kJ/kgmole-C) 221.6 221.6 43 Std Gas Flow (STD_m3/h) 2918 2918 44 Std Ideal Liq Mass Density (kg/m3) 870.1 870.1 45 Act Liq Flow (m3/s) 4.768e-003 4.768e-003 46 Z Factor 8.177e-003 8.177e-003 47 Watson K 10.35 10.35 48 User Property - - 49 Partial Pressure of H2S 50 Cp/(Cp - R) 51 Cp/Cv 52 Heat of Vap 53 Kinematic Viscosity 54 Liq Mass Density (Std Cond) 55 Liq Vol Flow (Std Cond) 56 Liquid Fraction 57 Molar Volume 58 Mass Heat of Vap 59 Phase Fraction [Molar Basis] 60 Surface Tension 61 Thermal Conductivity 62 Viscosity 63 Aspen Technology Inc Licensed to: LEGENDS (kPa) 0.0000 - (Cost/s) 0.0000 0.0000 (kPa) 0.0000 - 1.039 1.039 1.281 1.281 (kJ/kgmole) 3.411e+004 - (cSt) 0.2754 0.2754 (kg/m3) 872.4 872.4 (m3/h) 14.96 14.96 (m3/kgmole) (kJ/kg) 1.000 1.000 0.1391 0.1391 322.5 - 0.0000 1.0000 (dyne/cm) 16.77 16.77 (W/m-K) 0.1120 0.1120 0.2094 0.2094 (cP) Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Material Stream: (continued) Basis-1 Property Package: Peng-Robinson PROPERTIES 10 Overall 11 12 Cv (Semi-Ideal) 13 Mass Cv (Semi-Ideal) 14 Cv 15 Mass Cv 16 Cv (Ent Method) 17 Mass Cv (Ent Method) 18 Cp/Cv (Ent Method) 19 Reid VP at 37.8 C 20 True VP at 37.8 C Liquid Phase (kJ/kgmole-C) 213.2 213.2 (kJ/kg-C) 2.016 2.016 (kJ/kgmole-C) 173.0 173.0 (kJ/kg-C) 1.636 1.636 (kJ/kgmole-C) 173.4 173.4 (kJ/kg-C) 1.640 1.640 1.278 1.278 (kPa) 3.009 3.009 (kPa) 3.010 3.010 21 Liq Vol Flow - Sum(Std Cond) (m3/h) 14.96 14.96 22 Viscosity Index -27.14 - 23 COMPOSITION 24 25 Overall Phase 26 27 Fluid Package: COMPONENTS 28 MOLAR FLOW (kgmole/h) MOLE FRACTION MASS FLOW (kg/h) Vapour Fraction MASS FRACTION LIQUID VOLUME FLOW (m3/h) 0.0000 LIQUID VOLUME FRACTION 29 E-Benzene 121.0000 * 0.9804 * 12846.0860 * 0.9842 * 14.7651 * 0.9843 * 30 Styrene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 31 Hydrogen 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 32 Benzene 1.2100 * 0.0098 * 94.5131 * 0.0072 * 0.1071 * 0.0071 * 33 Ethylene 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 34 Toluene 1.2100 * 0.0098 * 111.4904 * 0.0085 * 0.1281 * 0.0085 * 35 H2O 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 36 Methane 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 0.0000 * 37 Total 123.4200 1.0000 38 1.0000 15.0003 Liquid Phase 39 40 13052.0895 COMPONENTS 41 MOLAR FLOW (kgmole/h) MOLE FRACTION MASS FLOW (kg/h) 1.0000 Phase Fraction 1.000 MASS FRACTION LIQUID VOLUME FLOW (m3/h) LIQUID VOLUME FRACTION 42 E-Benzene 121.0000 0.9804 12846.0860 0.9842 14.7651 0.9843 43 Styrene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 44 Hydrogen 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 45 Benzene 1.2100 0.0098 94.5131 0.0072 0.1071 0.0071 46 Ethylene 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 47 Toluene 1.2100 0.0098 111.4904 0.0085 0.1281 0.0085 48 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 49 Methane 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 50 Total 123.4200 1.0000 13052.0895 1.0000 15.0003 1.0000 51 K VALUE 52 53 COMPONENTS MIXED LIGHT HEAVY 54 E-Benzene 0.0000 0.0000 - 55 Styrene - - - 56 Hydrogen - - - 57 Benzene 0.0000 0.0000 - 58 Ethylene - - - 59 Toluene 0.0000 0.0000 - 60 H2O - - - 61 Methane - - - 62 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page 10 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-100 (continued) PROPERTIES 10 11 Name 12 LHV Vol Basis (Std) (MJ/m3) 15 0.0000 22 0.0000 13 HHV Vol Basis (Std) (MJ/m3) 4.101e+004 4.101e+004 14 HHV Mass Basis (Std) (kJ/kg) 2276 2276 15 CO2 Loading - - 16 CO2 Apparent Mole Conc (kgmole/m3) - - 17 CO2 Apparent Wt Conc (kgmol/kg) - - 18 LHV Mass Basis (Std) (kJ/kg) - - 19 Phase Fraction [Vol Basis] 0.0000 0.0000 20 Phase Fraction [Mass Basis] 0.0000 0.0000 21 Phase Fraction [Act Vol Basis] 0.0000 0.0000 22 Partial Pressure of CO2 (kPa) 0.0000 0.0000 23 Cost Based on Flow (Cost/s) 0.0000 0.0000 24 Act Gas Flow (ACT_m3/h) - - 25 Avg Liq Density (kgmole/m3) 55.40 55.40 26 Specific Heat 27 Std Gas Flow 28 Std Ideal Liq Mass Density 29 Act Liq Flow 30 Z Factor 31 Watson K 32 User Property - - 33 Partial Pressure of H2S 0.0000 0.0000 34 Cp/(Cp - R) 1.119 1.119 35 Cp/Cv 1.166 1.166 36 Heat of Vap (kJ/kgmole) 4.157e+004 4.003e+004 37 Kinematic Viscosity 0.4402 38 Liq Mass Density (Std Cond) 39 Liq Vol Flow (Std Cond) 40 Liquid Fraction 41 Molar Volume 42 Mass Heat of Vap 43 Phase Fraction [Molar Basis] 44 Surface Tension 45 Thermal Conductivity 46 Viscosity 47 Cv (Semi-Ideal) 48 Mass Cv (Semi-Ideal) 49 Cv 50 Mass Cv 51 Cv (Ent Method) 52 Mass Cv (Ent Method) 53 Cp/Cv (Ent Method) 54 Reid VP at 37.8 C 55 True VP at 37.8 C 56 57 Viscosity Index (kJ/kgmole-C) 78.10 78.10 (STD_m3/h) 7.093e+004 7.093e+004 (kg/m3) 998.0 998.0 (m3/s) 1.537e-002 1.537e-002 4.266e-004 1.312e-003 - - (kPa) (cSt) 0.4403 (kg/m3) 1015 1015 (m3/h) 53.26 53.26 1.000 1.000 (m3/kgmole) 1.845e-002 1.845e-002 (kJ/kg) 2308 2222 0.0000 0.0000 (dyne/cm) 65.07 65.06 (W/m-K) 0.6581 0.6581 (cP) 0.4299 0.4298 (kJ/kgmole-C) 69.79 69.78 (kJ/kg-C) 3.874 3.874 (kJ/kgmole-C) 66.98 66.98 (kJ/kg-C) 3.718 3.718 (kJ/kgmole-C) - - (kJ/kg-C) - - - - (kPa) 6.467 6.467 (kPa) 6.467 6.467 Liq Vol Flow - Sum(Std Cond) (m3/h) 53.26 53.26 -11.34 -11.35 58 PERFORMANCE 59 60 Results 61 62 Total Head 63 Aspen Technology Inc Licensed to: LEGENDS - Velocity Head Aspen HYSYS Version 7.3 (25.0.0.7336) -2.332e-004 m * Page 222 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-100 (continued) 10 Total Fluid Head - Pressure Head 14.10 m * 11 -2.332e-004 m * Delta P excluding Static Head Results - DYNAMICS 12 13 Dynamic Specifications 14 15 Head 16 Fluid Head 17 Adiabatic Efficiency (rpm) 18 Polytropic Efficiency (%) 19 Velocity Head Pressure Increase (m) - Not Active (kJ/kg) - Not Active - Not Active 75.00 Active (kPa) 135.0 Active 20 Power Capacity (kJ/h) 9962 (m3/h) 54.15 Not Active Use Characteristic Curves Not Active Pump is Acting as a Turbine Not Active Holdup Details 21 22 Phase Accumulation (kgmole/h) Moles (kgmole) 24 Vapour 0.0000 0.0000 * 0.0000 25 Liquid 0.0000 0.0000 * 0.0000 26 Aqueous 0.0000 0.0000 * 27 Total 0.0000 0.0000 23 28 Volume (m3) 0.0000 0.0000 NOTES 29 30 31 Pump: P-101 32 33 34 CONNECTIONS 35 36 Inlet Stream 37 Stream Name 38 39 From Unit Operation 19 Distillation 40 Outlet Stream 41 Stream Name 42 43 To Unit Operation 24 Recycle 44 Stream Name 46 From Unit Operation pump4 48 PARAMETERS 49 50 Adiabatic Efficiency (%): 75.00 Delta P: 175.0 kPa 51 53 Delta P: 54 Coefficient A: Parameter Preferences 56 58 175.0 kPa 0.0000 * Duty: Coefficient B: Units for Delta P: 12.96 kW 0.0000 * m Flow Basis Coefficient C: ActVolFlow 0.0000 * Units for Flow: m3/h RATING 59 Head Offset: 61 0.0000 m Efficiency Offset: 0.0000 Characteristic Curves 62 63 12.96 kW User Variables 57 60 Duty: CURVES 52 55 RCY-1 Energy Stream 45 47 T-101 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page 223 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-101 (continued) Speed: Flow 10 Head 11 NPSH 12 13 Efficiency (%) NPSH Required - NPSH Available 40.80 m Enable NPSH Curves: No NPSH Curves 14 15 16 Nozzle Paramaters 17 18 Base Elevation Relative to Ground Level 0.0000 m * 19 19 24 20 Diameter (m) 5.000e-002 5.000e-002 21 Elevation (Base) (m) 0.0000 0.0000 22 Elevation (Ground) (m) 0.0000 0.0000 23 Inertia 24 25 Rotational inertia (kg-m2) 0.5000 Radius of gyration (m) 26 Mass (kg) 50.00 Friction loss factor (kg-m2/s) 5.000e-002 Start Up 27 28 0.1000 Design Flow Typical Operating Capacity 10.00 m3/h 29 CONDITIONS 30 31 Name 32 Vapour 19 24 pump4 0.0000 0.0000 33 Temperature - (C) 90.6744 90.7544 34 Pressure - (kPa) 25.0000 200.0000 * 35 - Molar Flow (kgmole/h) 1520.6411 1520.6411 - 36 Mass Flow (kg/h) 161256.3954 161256.3954 - 37 Std Ideal Liq Vol Flow (m3/h) 184.8789 184.8789 - 38 Molar Enthalpy (kJ/kgmole) 8059 8090 - 39 Molar Entropy (kJ/kgmole-C) -12.32 -12.30 - 40 Heat Flow (kJ/h) 1.2255e+07 1.2301e+07 4.6655e+04 41 PROPERTIES 42 43 Name 44 Molecular Weight 45 Molar Density 46 Mass Density 47 19 24 106.0 106.0 (kgmole/m3) 7.605 7.606 (kg/m3) 806.5 806.6 Act Volume Flow (m3/h) 199.9 199.9 48 Mass Enthalpy (kJ/kg) 76.00 76.29 49 Mass Entropy (kJ/kg-C) -0.1162 -0.1160 50 Heat Capacity (kJ/kgmole-C) 201.1 201.1 51 Mass Heat Capacity (kJ/kg-C) 1.897 1.896 52 LHV Vol Basis (Std) (MJ/m3) 4.379e+006 4.379e+006 53 HHV Vol Basis (Std) (MJ/m3) 4.582e+006 4.582e+006 54 HHV Mass Basis (Std) (kJ/kg) 4.320e+004 4.320e+004 55 CO2 Loading - - 56 CO2 Apparent Mole Conc (kgmole/m3) - - 57 CO2 Apparent Wt Conc (kgmol/kg) - - 58 LHV Mass Basis (Std) (kJ/kg) 4.129e+004 4.129e+004 59 Phase Fraction [Vol Basis] 0.0000 0.0000 60 Phase Fraction [Mass Basis] 0.0000 0.0000 61 Phase Fraction [Act Vol Basis] 0.0000 0.0000 62 Partial Pressure of CO2 0.0000 0.0000 63 Aspen Technology Inc Licensed to: LEGENDS (kPa) Aspen HYSYS Version 7.3 (25.0.0.7336) Page 224 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-101 (continued) PROPERTIES 10 11 Name 12 Cost Based on Flow 13 19 24 (Cost/s) 0.0000 Act Gas Flow (ACT_m3/h) - 0.0000 - 14 Avg Liq Density (kgmole/m3) 8.225 8.225 15 Specific Heat 16 Std Gas Flow 17 Std Ideal Liq Mass Density 18 Act Liq Flow 19 Z Factor 20 Watson K 21 User Property 22 Partial Pressure of H2S 23 24 25 Heat of Vap 26 Kinematic Viscosity 27 Liq Mass Density (Std Cond) 28 Liq Vol Flow (Std Cond) 29 Liquid Fraction 30 Molar Volume 31 Mass Heat of Vap 32 Phase Fraction [Molar Basis] 33 Surface Tension 34 Thermal Conductivity 35 Viscosity 36 Cv (Semi-Ideal) 37 Mass Cv (Semi-Ideal) 38 Cv 39 Mass Cv 40 Cv (Ent Method) 41 Mass Cv (Ent Method) 42 Cp/Cv (Ent Method) 43 Reid VP at 37.8 C 44 True VP at 37.8 C (kJ/kgmole-C) 201.1 201.1 (STD_m3/h) 3.595e+004 3.595e+004 (kg/m3) 872.2 872.2 (m3/s) 5.554e-002 5.553e-002 1.087e-003 8.690e-003 10.34 10.34 - - 0.0000 0.0000 Cp/(Cp - R) 1.043 1.043 Cp/Cv 1.291 1.291 (kJ/kgmole) 3.808e+004 3.406e+004 (kPa) (cSt) 0.3717 0.3715 (kg/m3) 874.3 874.3 (m3/h) 184.4 184.4 (m3/kgmole) (kJ/kg) 1.000 1.000 0.1315 0.1315 359.1 321.2 0.0000 0.0000 (dyne/cm) 21.51 21.50 (W/m-K) 0.1237 0.1236 (cP) 0.2998 0.2996 (kJ/kgmole-C) 192.8 192.8 (kJ/kg-C) 1.818 1.818 (kJ/kgmole-C) 155.8 155.8 (kJ/kg-C) 1.469 1.469 (kJ/kgmole-C) - 153.8 (kJ/kg-C) - 1.450 - 1.308 (kPa) 2.700 2.700 (kPa) 2.700 2.700 45 Liq Vol Flow - Sum(Std Cond) (m3/h) 184.4 184.4 46 Viscosity Index -15.80 -15.82 47 PERFORMANCE 48 49 Results 50 51 Total Head - 52 Total Fluid Head - 53 Pressure Head 22.13 m * 54 Velocity Head -1.274e-002 m * Delta P excluding Static Head Results - DYNAMICS 55 56 Dynamic Specifications 57 58 Head 59 Fluid Head (m) - Not Active (kJ/kg) - Not Active 60 Adiabatic Efficiency (rpm) - Not Active 61 Polytropic Efficiency (%) 75.00 Active 62 Pressure Increase (kPa) 175.0 63 Aspen Technology Inc Licensed to: LEGENDS Active Power Capacity Use Characteristic Curves Pump is Acting as a Turbine Aspen HYSYS Version 7.3 (25.0.0.7336) (kJ/h) 4.665e+004 (m3/h) 184.9 Not Active Not Active Not Active Page 225 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-101 (continued) Holdup Details 10 11 Phase Accumulation (kgmole/h) Moles (kgmole) 13 Vapour 0.0000 0.0000 * 0.0000 14 Liquid 0.0000 0.0000 * 0.0000 15 Aqueous 0.0000 0.0000 * 16 Total 0.0000 0.0000 12 17 Volume (m3) 0.0000 0.0000 NOTES 18 19 20 Pump: P-102 21 22 23 CONNECTIONS 24 25 Inlet Stream 26 Stream Name 27 28 From Unit Operation 20 Distillation 29 Outlet Stream 30 Stream Name 31 32 To Unit Operation 21 33 Energy Stream 34 Stream Name 35 36 From Unit Operation pump2 37 PARAMETERS 38 39 Adiabatic Efficiency (%): 75.00 Delta P: 145.0 kPa 40 42 Delta P: 43 Coefficient A: 145.0 kPa 0.0000 * Parameter Preferences 0.8158 kW 0.0000 * m Flow Basis Coefficient C: ActVolFlow 0.0000 * Units for Flow: m3/h User Variables 46 47 RATING 48 Head Offset: 0.0000 m 50 Efficiency Offset: 0.0000 Characteristic Curves 51 Speed: 52 Flow 53 Head 54 Efficiency (%) NPSH 55 56 0.8158 kW Duty: Coefficient B: Units for Delta P: 45 49 Duty: CURVES 41 44 T-101 NPSH Required - NPSH Available 0.2360 m Enable NPSH Curves: No NPSH Curves 57 58 59 Nozzle Paramaters 60 61 Base Elevation Relative to Ground Level 63 0.0000 m * 20 62 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) 21 Page 226 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-102 (continued) Diameter (m) 5.000e-002 5.000e-002 10 Elevation (Base) (m) 0.0000 0.0000 11 Elevation (Ground) (m) 0.0000 0.0000 12 Inertia 13 14 Rotational inertia (kg-m2) 0.5000 Radius of gyration (m) 15 Mass (kg) 50.00 Friction loss factor (kg-m2/s) Design Flow Typical Operating Capacity 10.00 m3/h 18 CONDITIONS 19 20 Name 21 Vapour 20 21 pump2 0.0000 0.0000 22 Temperature - (C) 123.2020 123.2724 23 Pressure - (kPa) 55.0000 200.0000 * 24 - Molar Flow (kgmole/h) 117.9432 117.9432 - 25 Mass Flow (kg/h) 12295.9000 12295.9000 - 26 Std Ideal Liq Vol Flow (m3/h) 13.5601 13.5601 - 27 Molar Enthalpy (kJ/kgmole) 1.174e+005 1.174e+005 - 28 Molar Entropy (kJ/kgmole-C) 459.4 459.4 - 29 Heat Flow (kJ/h) 1.3845e+07 1.3848e+07 2.9370e+03 30 PROPERTIES 31 32 Name 33 Molecular Weight 34 Molar Density 35 Mass Density 36 20 21 104.3 104.3 (kgmole/m3) 7.764 7.765 (kg/m3) 809.4 809.5 Act Volume Flow (m3/h) 15.19 15.19 37 Mass Enthalpy (kJ/kg) 1126 1126 38 Mass Entropy (kJ/kg-C) 4.406 4.407 39 Heat Capacity (kJ/kgmole-C) 202.6 202.5 40 Mass Heat Capacity (kJ/kg-C) 1.943 1.943 41 LHV Vol Basis (Std) (MJ/m3) 4.228e+006 4.228e+006 42 HHV Vol Basis (Std) (MJ/m3) 4.394e+006 4.394e+006 43 HHV Mass Basis (Std) (kJ/kg) 4.214e+004 4.214e+004 44 CO2 Loading - - 45 CO2 Apparent Mole Conc (kgmole/m3) - - 46 CO2 Apparent Wt Conc (kgmol/kg) - - 47 LHV Mass Basis (Std) (kJ/kg) 4.055e+004 4.055e+004 48 Phase Fraction [Vol Basis] 0.0000 0.0000 49 Phase Fraction [Mass Basis] 0.0000 0.0000 50 Phase Fraction [Act Vol Basis] 0.0000 0.0000 51 Partial Pressure of CO2 (kPa) 0.0000 0.0000 52 Cost Based on Flow (Cost/s) 0.0000 0.0000 53 Act Gas Flow (ACT_m3/h) - - 54 Avg Liq Density (kgmole/m3) 8.698 8.698 55 Specific Heat (kJ/kgmole-C) 202.6 202.5 56 Std Gas Flow (STD_m3/h) 2789 2789 57 Std Ideal Liq Mass Density (kg/m3) 906.8 906.8 58 Act Liq Flow (m3/s) 4.220e-003 4.219e-003 59 Z Factor 2.150e-003 7.814e-003 60 Watson K 10.01 10.01 61 User Property 62 Partial Pressure of H2S 63 5.000e-002 Start Up 16 17 0.1000 Aspen Technology Inc Licensed to: LEGENDS (kPa) - - 0.0000 0.0000 Aspen HYSYS Version 7.3 (25.0.0.7336) Page 227 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-102 (continued) PROPERTIES 10 11 Name 12 Cp/(Cp - R) 20 1.043 21 13 Cp/Cv 1.294 1.294 14 Heat of Vap (kJ/kgmole) 3.785e+004 3.504e+004 15 Kinematic Viscosity 16 Liq Mass Density (Std Cond) 17 Liq Vol Flow (Std Cond) 18 Liquid Fraction 19 Molar Volume 20 Mass Heat of Vap 21 Phase Fraction [Molar Basis] 22 Surface Tension 23 Thermal Conductivity 24 Viscosity 25 Cv (Semi-Ideal) 26 Mass Cv (Semi-Ideal) 27 Cv 28 Mass Cv 29 Cv (Ent Method) 30 Mass Cv (Ent Method) 31 Cp/Cv (Ent Method) 32 Reid VP at 37.8 C 33 True VP at 37.8 C 1.043 (cSt) 0.3097 0.3095 (kg/m3) 907.5 907.5 (m3/h) 13.55 13.55 (m3/kgmole) (kJ/kg) 1.000 1.000 0.1288 0.1288 363.1 336.1 0.0000 0.0000 (dyne/cm) 19.99 19.99 (W/m-K) 0.1216 0.1215 (cP) 0.2507 0.2506 (kJ/kgmole-C) 194.2 194.2 (kJ/kg-C) 1.863 1.863 (kJ/kgmole-C) 156.5 156.5 (kJ/kg-C) 1.501 1.501 (kJ/kgmole-C) - 158.7 (kJ/kg-C) - 1.522 - 1.277 (kPa) 1.906 1.906 (kPa) 1.906 1.906 34 Liq Vol Flow - Sum(Std Cond) (m3/h) 13.55 13.55 35 Viscosity Index -21.91 -21.93 36 PERFORMANCE 37 38 Results 39 40 Total Head - 41 Total Fluid Head - 42 Pressure Head 18.27 m * 43 -6.944e-005 m * Delta P excluding Static Head Results - DYNAMICS 44 45 Dynamic Specifications 46 47 Head 48 Fluid Head (m) - Not Active (kJ/kg) - Not Active 49 Adiabatic Efficiency (rpm) - Not Active 50 Polytropic Efficiency (%) 75.00 Active 51 Pressure Increase (kPa) 145.0 Active 52 Power Capacity (kJ/h) 2937 (m3/h) 13.56 Not Active Use Characteristic Curves Not Active Pump is Acting as a Turbine Not Active Holdup Details 53 54 Velocity Head Phase Accumulation (kgmole/h) Moles (kgmole) 56 Vapour 0.0000 0.0000 * 0.0000 57 Liquid 0.0000 0.0000 * 0.0000 58 Aqueous 0.0000 0.0000 * 59 Total 0.0000 0.0000 55 60 Volume (m3) 0.0000 0.0000 NOTES 61 62 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page 228 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-103 CONNECTIONS 10 11 Inlet Stream 12 Stream Name 13 14 From Unit Operation 17 Distillation 15 Outlet Stream 16 Stream Name 17 18 To Unit Operation 26 19 Energy Stream 20 Stream Name 21 22 From Unit Operation pump5 23 PARAMETERS 24 25 Adiabatic Efficiency (%): 75.00 Delta P: 155.0 kPa 26 28 Delta P: 29 Coefficient A: 155.0 kPa 0.0000 * Parameter Preferences 1.894e-002 kW 0.0000 * Units for Delta P: m Flow Basis Coefficient C: ActVolFlow 0.0000 * Units for Flow: m3/h User Variables 32 33 RATING 34 Head Offset: 0.0000 m 36 Efficiency Offset: 0.0000 Characteristic Curves 37 Speed: 38 Flow 39 Head 40 Efficiency (%) NPSH 41 42 1.894e-002 kW Duty: Coefficient B: 31 35 Duty: CURVES 27 30 T-100 NPSH Required - NPSH Available 2.095e-004 m Enable NPSH Curves: No NPSH Curves 43 44 45 Nozzle Paramaters 46 47 Base Elevation Relative to Ground Level 0.0000 m * 17 48 26 49 Diameter (m) 5.000e-002 5.000e-002 50 Elevation (Base) (m) 0.0000 0.0000 51 Elevation (Ground) (m) 0.0000 0.0000 52 Inertia 53 54 Rotational inertia (kg-m2) 0.5000 Radius of gyration (m) 55 Mass (kg) 50.00 Friction loss factor (kg-m2/s) 5.000e-002 Start Up 56 57 0.1000 Design Flow Typical Operating Capacity 10.00 m3/h 58 CONDITIONS 59 60 Name 61 Vapour 62 Temperature 63 Aspen Technology Inc Licensed to: LEGENDS (C) 17 26 pump5 0.0000 0.0000 - 70.1632 70.2407 - Aspen HYSYS Version 7.3 (25.0.0.7336) Page 229 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-103 (continued) CONDITIONS 10 11 Pressure (kPa) 45.0000 200.0000 * - 12 Molar Flow (kgmole/h) 3.0931 3.0931 - 13 Mass Flow (kg/h) 271.9789 271.9789 - 14 Std Ideal Liq Vol Flow (m3/h) 0.3111 0.3111 - 15 Molar Enthalpy (kJ/kgmole) 3.208e+004 3.210e+004 - 16 Molar Entropy (kJ/kgmole-C) -91.77 -91.75 - 17 Heat Flow (kJ/h) 9.9218e+04 9.9287e+04 6.8179e+01 18 PROPERTIES 19 20 Name 21 Molecular Weight 22 Molar Density 23 Mass Density 24 Act Volume Flow 25 Mass Enthalpy (kJ/kg) 364.8 365.1 26 Mass Entropy (kJ/kg-C) -1.044 -1.043 27 Heat Capacity (kJ/kgmole-C) 154.0 154.0 28 Mass Heat Capacity (kJ/kg-C) 1.751 1.751 29 LHV Vol Basis (Std) (MJ/m3) 3.594e+006 3.594e+006 30 HHV Vol Basis (Std) (MJ/m3) 3.746e+006 3.746e+006 31 HHV Mass Basis (Std) (kJ/kg) 4.260e+004 4.260e+004 32 CO2 Loading - - 33 CO2 Apparent Mole Conc (kgmole/m3) - - 34 CO2 Apparent Wt Conc (kgmol/kg) - - 35 LHV Mass Basis (Std) (kJ/kg) 4.087e+004 4.087e+004 36 Phase Fraction [Vol Basis] 0.0000 0.0000 37 Phase Fraction [Mass Basis] 0.0000 0.0000 38 Phase Fraction [Act Vol Basis] 0.0000 0.0000 39 Partial Pressure of CO2 (kPa) 0.0000 0.0000 40 Cost Based on Flow (Cost/s) 0.0000 0.0000 41 Act Gas Flow (ACT_m3/h) - - 42 Avg Liq Density (kgmole/m3) 9.943 9.943 43 Specific Heat (kJ/kgmole-C) 154.0 154.0 44 Std Gas Flow (STD_m3/h) 73.13 73.13 45 Std Ideal Liq Mass Density (kg/m3) 874.3 874.3 46 Act Liq Flow (m3/s) 9.164e-005 9.163e-005 47 Z Factor 1.681e-003 7.471e-003 48 Watson K 10.01 10.01 49 User Property 50 Partial Pressure of H2S 51 52 53 Heat of Vap 54 Kinematic Viscosity 55 Liq Mass Density (Std Cond) 56 Liq Vol Flow (Std Cond) 57 Liquid Fraction 58 Molar Volume 59 Mass Heat of Vap 60 Phase Fraction [Molar Basis] 61 Surface Tension 62 Thermal Conductivity 63 17 26 87.93 87.93 (kgmole/m3) 9.376 9.377 (kg/m3) 824.4 824.5 (m3/h) 0.3299 0.3299 - - 0.0000 0.0000 Cp/(Cp - R) 1.057 1.057 Cp/Cv 1.482 1.482 (kJ/kgmole) 3.488e+004 3.236e+004 0.4200 Aspen Technology Inc Licensed to: LEGENDS (kPa) (cSt) 0.4203 (kg/m3) 879.3 879.3 (m3/h) 0.3093 0.3093 1.000 1.000 (m3/kgmole) 0.1067 0.1066 (kJ/kg) 396.6 368.1 0.0000 0.0000 (dyne/cm) 22.50 22.49 (W/m-K) 0.1228 0.1228 Aspen HYSYS Version 7.3 (25.0.0.7336) Page 230 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Pump: P-103 (continued) PROPERTIES 10 11 Name 12 Viscosity 17 13 Cv (Semi-Ideal) 14 Mass Cv (Semi-Ideal) 15 Cv 16 Mass Cv 17 Cv (Ent Method) 18 Mass Cv (Ent Method) 19 Cp/Cv (Ent Method) 20 Reid VP at 37.8 C 21 True VP at 37.8 C 26 (cP) 0.3465 0.3463 (kJ/kgmole-C) 145.7 145.6 (kJ/kg-C) 1.656 1.656 (kJ/kgmole-C) 103.9 103.9 (kJ/kg-C) 1.181 1.182 (kJ/kgmole-C) - 105.4 (kJ/kg-C) - 1.198 - 1.461 (kPa) 13.29 13.29 (kPa) 13.30 13.30 22 Liq Vol Flow - Sum(Std Cond) (m3/h) 0.3093 0.3093 23 Viscosity Index -12.48 -12.50 24 PERFORMANCE 25 26 Results 27 28 Total Head - 29 Total Fluid Head - 30 Pressure Head 19.17 m * 31 Velocity Head -1.778e-008 m * Delta P excluding Static Head Results - DYNAMICS 32 33 Dynamic Specifications 34 35 Head 36 Fluid Head (m) - Not Active (kJ/kg) - Not Active 37 Adiabatic Efficiency (rpm) - Not Active 38 Polytropic Efficiency (%) 75.00 Active 39 Pressure Increase (kPa) 155.0 Active 40 Power Capacity (kJ/h) 68.18 Not Active (m3/h) 0.3111 Use Characteristic Curves Not Active Pump is Acting as a Turbine Not Active Holdup Details 41 42 Phase Accumulation (kgmole/h) Moles (kgmole) 44 Vapour 0.0000 0.0000 * 0.0000 45 Liquid 0.0000 0.0000 * 0.0000 46 Aqueous 0.0000 0.0000 * 47 Total 0.0000 0.0000 43 48 Volume (m3) 0.0000 0.0000 NOTES 49 50 51 Recycle: RCY-1 52 53 54 CONNECTIONS 55 56 Inlet Stream 57 Stream Name 58 59 24 60 63 P-101 Outlet Stream 61 62 From Unit Operation Pump Stream Name Aspen Technology Inc Licensed to: LEGENDS To Unit Operation Aspen HYSYS Version 7.3 (25.0.0.7336) Page 231 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Recycle: RCY-1 (continued) 25 Mixer MIX-100 10 TOLERANCE 11 12 Vapour Fraction: 10.00 * Temperature: 10.00 * Pressure: 10.00 * 13 Flow: 10.00 * Enthalpy: 10.00 * Composition: 10.00 * Q Maximum: 0.0000 * 14 NUMERICAL 15 16 Acceleration Type: 17 Maximum Iterations: Wegstein 18 Wegstein Count: Iteration Type: 10 * Nested Iteration Count: 3* 0* Q Minimum: 19 -20.00 * Iteration History 20 21 Iteration 22 * Variable Outlet Value Inlet Value Converged - - 23 User Variables 24 25 CONDITIONS 26 27 Name 28 Vapour 29 Temperature 30 Pressure 31 Molar Flow (kgmole/h) 1520.6411 32 Mass Flow (kg/h) 161256.3954 161003.5996 33 Std Ideal Liq Vol Flow 184.5890 34 Molar Enthalpy 35 Molar Entropy 36 Heat Flow (C) (kPa) 24 25 0.0000 0.0000 90.7544 90.7544 * 200.0000 * 200.0000 * 1518.2574 * (m3/h) 184.8789 (kJ/kgmole) 8090 8090 (kJ/kgmole-C) -12.30 -12.30 (kJ/h) 1.2301e+07 1.2283e+07 37 PROPERTIES 38 39 Name 40 Molecular Weight 41 Molar Density 42 Mass Density 43 24 25 106.0 106.0 (kgmole/m3) 7.606 7.606 (kg/m3) 806.6 806.6 Act Volume Flow (m3/h) 199.9 199.6 44 Mass Enthalpy (kJ/kg) 76.29 76.29 45 Mass Entropy (kJ/kg-C) -0.1160 -0.1160 46 Heat Capacity (kJ/kgmole-C) 201.1 201.1 47 Mass Heat Capacity (kJ/kg-C) 1.896 1.896 48 LHV Vol Basis (Std) (MJ/m3) 4.379e+006 4.379e+006 49 HHV Vol Basis (Std) (MJ/m3) 4.582e+006 4.582e+006 50 HHV Mass Basis (Std) (kJ/kg) 4.320e+004 4.320e+004 51 CO2 Loading - - 52 CO2 Apparent Mole Conc (kgmole/m3) - - 53 CO2 Apparent Wt Conc (kgmol/kg) - - 54 LHV Mass Basis (Std) (kJ/kg) 4.129e+004 4.129e+004 55 Phase Fraction [Vol Basis] 0.0000 0.0000 56 Phase Fraction [Mass Basis] 0.0000 0.0000 57 Phase Fraction [Act Vol Basis] 0.0000 0.0000 58 Partial Pressure of CO2 (kPa) 0.0000 0.0000 59 Cost Based on Flow (Cost/s) 0.0000 0.0000 60 Act Gas Flow (ACT_m3/h) - - 61 Avg Liq Density (kgmole/m3) 8.225 8.225 62 Specific Heat 201.1 201.1 63 Aspen Technology Inc Licensed to: LEGENDS (kJ/kgmole-C) Aspen HYSYS Version 7.3 (25.0.0.7336) Page 232 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Recycle: RCY-1 (continued) PROPERTIES 10 11 Name 12 Std Gas Flow 24 13 Std Ideal Liq Mass Density 14 Act Liq Flow 15 Z Factor 16 Watson K 17 User Property 18 Partial Pressure of H2S 19 20 21 Heat of Vap 22 Kinematic Viscosity 23 Liq Mass Density (Std Cond) 24 Liq Vol Flow (Std Cond) 25 Liquid Fraction 26 Molar Volume 27 Mass Heat of Vap 28 Phase Fraction [Molar Basis] 29 Surface Tension 30 Thermal Conductivity 31 Viscosity 32 Cv (Semi-Ideal) 33 Mass Cv (Semi-Ideal) 34 Cv 35 Mass Cv 36 Cv (Ent Method) 37 Mass Cv (Ent Method) 38 Cp/Cv (Ent Method) 39 Reid VP at 37.8 C 40 True VP at 37.8 C (STD_m3/h) 25 3.595e+004 3.590e+004 (kg/m3) 872.2 872.2 (m3/s) 5.553e-002 5.545e-002 8.690e-003 8.690e-003 10.34 10.34 - - 0.0000 0.0000 Cp/(Cp - R) 1.043 1.043 Cp/Cv 1.291 1.291 (kJ/kgmole) 3.406e+004 3.406e+004 (kPa) (cSt) 0.3715 0.3715 (kg/m3) 874.3 874.3 (m3/h) 184.4 184.2 (m3/kgmole) (kJ/kg) 1.000 1.000 0.1315 0.1315 321.2 321.2 0.0000 0.0000 (dyne/cm) 21.50 21.50 (W/m-K) 0.1236 0.1236 (cP) 0.2996 0.2996 (kJ/kgmole-C) 192.8 192.8 (kJ/kg-C) 1.818 1.818 (kJ/kgmole-C) 155.8 155.8 (kJ/kg-C) 1.469 1.469 (kJ/kgmole-C) 153.8 161.1 (kJ/kg-C) 1.450 1.519 1.308 1.248 (kPa) 2.700 2.700 (kPa) 2.700 2.700 41 Liq Vol Flow - Sum(Std Cond) (m3/h) 184.4 184.2 42 Viscosity Index -15.82 -15.82 43 Valve: VLV-100 44 45 46 CONNECTIONS 47 48 Inlet Stream 49 STREAM NAME 50 51 52 STREAM NAME 54 7.1 56 58 PFR-100 Physical Properties 59 Pressure Drop: 61 10.00 kPa * User Variables 62 63 TO UNIT OPERATION Plug Flow Reactor PARAMETERS 57 60 MIX-101 Outlet Stream 53 55 FROM UNIT OPERATION Mixer Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page 233 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Valve: VLV-100 (continued) RATING 10 11 Sizing 12 Sizing Conditions 13 14 Inlet Pressure 15 Valve Opening 170.0 kPa Molecular Weight 50.00 % * 10.00 kPa * Manufacturer: 17 Universal Gas Sizing Type: Linear 19 C1 25.00 Sizing Method: Km 0.9000 21 - Cv - Cv (standard) cal/min.sqrt(psi) Cg - Nozzle Parameters 22 Base Elevation Relative to Ground Level 0.0000 m * 24 7.1 25 Diameter (m) 5.000e-002 5.000e-002 26 Elevation (Base) (m) 0.0000 0.0000 27 Elevation (Ground) (m) 0.0000 0.0000 28 Elevation (% of Height) (%) 29 CONDITIONS 30 31 Name 32 Vapour 33 Temperature 34 Pressure 35 Molar Flow 36 Mass Flow 37 Std Ideal Liq Vol Flow 38 Molar Enthalpy 39 Molar Entropy 40 Heat Flow 7.1 1.0000 1.0000 354.9298 (C) 354.9752 (kPa) 170.0000 160.0000 (kgmole/h) 4641.6774 4641.6774 228100.9906 (kg/h) 228100.9906 (m3/h) 253.7437 253.7437 (kJ/kgmole) -1.138e+005 -1.138e+005 (kJ/kgmole-C) 196.0 196.5 (kJ/h) -5.2837e+08 -5.2837e+08 41 PROPERTIES 42 43 Name 44 Molecular Weight 45 Molar Density (kgmole/m3) 46 Mass Density (kg/m3) 1.607 1.512 47 Act Volume Flow (m3/h) 1.419e+005 1.508e+005 48 Mass Enthalpy (kJ/kg) -2316 -2316 49 Mass Entropy (kJ/kg-C) 3.989 3.999 50 Heat Capacity (kJ/kgmole-C) 109.6 109.6 51 Mass Heat Capacity (kJ/kg-C) 2.231 2.230 52 LHV Vol Basis (Std) (MJ/m3) 1.549e+006 1.549e+006 53 HHV Vol Basis (Std) (MJ/m3) 1.647e+006 1.647e+006 54 HHV Mass Basis (Std) (kJ/kg) 3.351e+004 3.351e+004 55 CO2 Loading - - 56 CO2 Apparent Mole Conc (kgmole/m3) - - 57 CO2 Apparent Wt Conc (kgmol/kg) - - 58 LHV Mass Basis (Std) (kJ/kg) 3.151e+004 3.151e+004 59 Phase Fraction [Vol Basis] 1.000 1.000 60 Phase Fraction [Mass Basis] 1.000 1.000 61 Phase Fraction [Act Vol Basis] 1.000 1.000 62 Partial Pressure of CO2 0.0000 0.0000 63 2.281e+005 kg/h Valve Operating Characteristic and Sizing Method 18 23 Current Flow Rate Valve Manufacturer and Valve Type 16 20 49.14 Delta P Aspen Technology Inc Licensed to: LEGENDS (kPa) 7.1 49.14 49.14 3.270e-002 3.077e-002 Aspen HYSYS Version 7.3 (25.0.0.7336) Page 234 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Valve: VLV-100 (continued) PROPERTIES 10 11 Name 12 Cost Based on Flow 13 Act Gas Flow 14 Avg Liq Density 15 Specific Heat 16 Std Gas Flow 17 Std Ideal Liq Mass Density 18 Act Liq Flow 19 Z Factor 20 Watson K 21 User Property 22 Partial Pressure of H2S 23 24 25 Heat of Vap 26 Kinematic Viscosity 27 Liq Mass Density (Std Cond) 28 Liq Vol Flow (Std Cond) 29 Liquid Fraction 30 Molar Volume 31 Mass Heat of Vap 32 Phase Fraction [Molar Basis] 33 Surface Tension 34 Thermal Conductivity 35 Viscosity 36 Cv (Semi-Ideal) 37 Mass Cv (Semi-Ideal) 38 Cv 39 Mass Cv 40 Cv (Ent Method) 41 Mass Cv (Ent Method) 42 Cp/Cv (Ent Method) 43 Reid VP at 37.8 C 44 True VP at 37.8 C 45 46 Viscosity Index 7.1 (Cost/s) 0.0000 0.0000 (ACT_m3/h) 1.419e+005 1.508e+005 18.29 (kgmole/m3) 18.29 (kJ/kgmole-C) 109.6 109.6 (STD_m3/h) 1.097e+005 1.097e+005 (kg/m3) 898.9 898.9 (m3/s) - - 0.9954 0.9957 10.34 10.34 - - 0.0000 0.0000 Cp/(Cp - R) 1.082 1.082 Cp/Cv 1.084 1.084 (kJ/kgmole) 4.020e+004 4.027e+004 (kPa) (cSt) 10.76 11.43 (kg/m3) 939.6 939.6 (m3/h) 242.8 242.8 0.0000 0.0000 (m3/kgmole) 30.58 32.50 (kJ/kg) 818.0 819.4 1.0000 1.0000 (dyne/cm) - - (W/m-K) 4.561e-002 4.559e-002 (cP) 1.729e-002 1.729e-002 (kJ/kgmole-C) 101.3 101.3 (kJ/kg-C) 2.062 2.061 (kJ/kgmole-C) 101.1 101.1 (kJ/kg-C) 2.058 2.058 (kJ/kgmole-C) - - (kJ/kg-C) - - - - (kPa) 2.723 2.723 (kPa) 9.195 9.195 Liq Vol Flow - Sum(Std Cond) (m3/h) 242.8 242.8 2.791 3.073 47 DYNAMICS 48 49 Dynamic Specifications 50 51 Total Delta P 52 Pressure Flow Relation (kPa) 10.00 * Not Active Active 53 Dynamic Parameters 54 55 Valve Opening 56 Conductance (%) (USGPM(60F,1psi)) 57 50.00 * - Mass Flow (kg/h) 2.281e+005 Friction Delta P (kPa) 10.00 (kg/hr/sqrt(kPa-kg/m3)) 0.0000 Pipe Model Parameters 58 59 Material 60 Roughness (m) 61 Pipe Length (m) 62 Feed Diameter (m) 63 Aspen Technology Inc Licensed to: LEGENDS Cast Iron 2.590e-004 0.0000 * 5.000e-002 Darcy Friction Factor Pipe k Velocity Reynolds Number Aspen HYSYS Version 7.3 (25.0.0.7336) (m/s) 2.008e+004 * 9.331e+007 * Page 235 of 236 * Specified by user LEGENDS Burlington, MA USA Case Name: TEST FINAL.HSC Unit Set: SI Date/Time: Mon Dec 10 20:32:46 2018 Valve: VLV-100 (continued) Hold-Up Volume: 0.0000 m3 10 11 * Phase Accumulation (kgmole/h) Moles (kgmole) 13 Vapour 0.0000 0.0000 * 0.0000 14 Liquid 0.0000 0.0000 * 0.0000 15 Aqueous 0.0000 0.0000 * 16 Total 0.0000 0.0000 12 17 19 Parameters Mode: Instantaneous 20 21 Actuator Time Constant (seconds) 22 Valve Stickiness Time Constant (seconds) 1.000 * Actuator Linear Rate 1.000 * - 23 Activator Position 24 25 Fail Position: None 26 Min (%) 27 28 30 0.0000 0.0000 Actuator Parameters 18 29 Volume (m3) Valve Actuator Max (%) Current (%) Desired (%) 0.00 * 100.00 * 50.00 * - 0.00 * 100.00 * 50.00 * 50.00 Offset (%) 0.00 * - 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page 236 of 236 * Specified by user * ... 61 Hydrogen - - - 62 Benzene 0.0000 0.0000 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) - Page of 236 * Specified by user 1 LEGENDS Burlington, MA USA... 1.285 1.285 63 Aspen Technology Inc Licensed to: LEGENDS 106.0 106.0 4.117e-002 4.117e-002 Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user 1 LEGENDS Burlington, MA USA Case... Sum(Std Cond) (m3/h) 199.1 199.1 - - 60 61 62 63 Aspen Technology Inc Licensed to: LEGENDS Aspen HYSYS Version 7.3 (25.0.0.7336) Page of 236 * Specified by user 1 LEGENDS Burlington, MA USA Case