************************************************************************************INPUT SUMMARY************************************************************************************------------------------------------------------------------------------------------FLUID PACKAGE: Basis-1------------------------------------------------------------------------------------Property Package Type: UniquacComponent List - 1: 1-Propanol /H2O /------------------------------------------------------------------------------------FLOWSHEET: Main------------------------------------------------------------------------------------Fluid Package: Basis-1UNIT OPERATION: E-100 (Heat Exchanger) TubeInletStream = Agua-e TubeOutletStream = Agua-s ShellInletStream = propanol-e ShellOutletStream = propanol-s NoOfTubes = 500 TubePitch = 23 mm ShellDiameter = 1000 mm TubeLength = 4 m TubeOuterDiameter = 19.05 mm TubeInnerDiameter = 16.5608 mm Solution Method = SimpleDesignObject HCurveName = Agua-e-Agua-s HCurveName = propanol-e-propanol-sSpecification Name = E-100 UASpecTypeSelection = UASTREAM: Agua-e (Material Stream) Temperature = 20 C Pressure = 500 kPa Composition Basis (In Mole Fractions ):1-Propanol = 0/ H2O = 1/ STREAM: Agua-s (Material Stream) Temperature = 40 CSTREAM: propanol-e (Material Stream) Vapour Fraction = 1 Pressure = 230.007742 kPa Mass Flow = 72575.5239 kg/h Composition Basis (In Mole Fractions ):1-Propanol = 1/ H2O = 0/ STREAM: propanol-s (Material Stream)################################################################################OUTPUT SUMMARY################################################################################ LEGENDS Case Name: ejemplo6_sesin3.hsc Burlington, MA USA Unit Set: SI Date/Time: Fri Aug 28 23:01:58 2015 -------------------------------------------------------------------------------Basis-1 (Fluid Package): Component List-------------------------------------------------------------------------------Fluid Package: Basis-1 COMPONENT LIST Component List - 1 [HYSYS Databanks] COMPONENT TYPE MOLECULAR BOILING PT IDEAL LIQ CRITICAL WEIGHT (C) DENSITY (kg/m3) TEMP (C) 1-Propanol Pure 60.10 97.15 804.0 263.6 H2O Pure 18.02 100.0 998.0 374.1 (Continued..) Component List - 1 [HYSYS Databanks] COMPONENT CRITICAL PRES CRITICAL VOL ACENTRICITY HEAT OF FORM (kPa) (m3/kgmole) (kJ/kgmole) 1-Propanol 5170 0.2190 0.6230 -2.566e+005 H2O 2.212e+004 5.710e-002 0.3440 -2.418e+005 -------------------------------------------------------------------------------Case (Simulation Case): Mass and Energy Balance, Utility Balance, Process CO2 Emissions-------------------------------------------------------------------------------Simulation Case: Case OVERALL MASS BALANCE In Stream Count Mass Flow Out Stream Count Mass Flow (kg/h) (kg/h) Agua-e Yes 6.986e+005 Agua-s Yes 6.986e+005 propanol-e Yes 7.258e+004 propanol-s Yes 7.258e+004 Total In MassFlow (kg/h) 7.712e+005 Total Out MassFlow (kg/h) 7.712e+005 Mass Imbalance (kg/h) 0.0000 Rel Mass Imbalance Pct (%) 0.00 OVERALL ENERGY BALANCE InStream Count Energy Flow OutStream Count Energy Flow (kJ/h) (kJ/h) Agua-e Yes -1.106e+10 Agua-s Yes -1.100e+10 propanol-e Yes -2.987e+08 propanol-s Yes -3.577e+08 Total In EnergyFlow (kJ/h) -1.136e+010 Total Out EnergyFlow (kJ/h) -1.136e+010 Energy Imbalance (kJ/h) -8.187e+004 Rel Energy Imbalance Pct (%) 0.00 OVERALL UTILITY BALANCE Utility Name Usage Info Energy Flow Mass Flow Cost Hot Utility Summary Cold Utility Summary Utility Flow --- Utility Flow --- Utility Cost --- Utility Cost --- Carbon Emiss. --- Carbon Emiss. --- Carbon Fees --- Carbon Fees --- PROCESS CO2 EMISSIONS Inlet Stream Count IFPP (1995) IFPP (2007) EPA (2009) (kg/h) (kg/h) (kg/h) Agua-e Yes 0.000e-01 0.000e-01 0.000e-01 propanol-e Yes 0.000e-01 0.000e-01 0.000e-01 Total from Inlets --- --- --- Total Carbon Fees --- --- --- from Inlets (Cost/hr) Outlet Stream Count IFPP (1995) IFPP (2007) EPA (2009) (kg/h) (kg/h) (kg/h) Agua-s Yes 0.000e-01 0.000e-01 0.000e-01 propanol-s Yes 0.000e-01 0.000e-01 0.000e-01 Total from Outlets --- --- --- Total Carbon Fees --- --- --- from Outlets (Cost/hr) -------------------------------------------------------------------------------Agua-e (Material Stream): Worksheet, Attachments-------------------------------------------------------------------------------Material Stream: Agua-e Fluid Package: Basis-1 Property Package: UNIQUAC - Ideal CONDITIONS OVERALL AQUEOUS PH. Vapour / Phase Fraction 0.0000 1.0000 Temperature: (C) 20.00 20.00 Pressure: (kPa) 500.0 500.0 Molar Flow (kgmole/h) 3.878e+004 3.878e+004 Mass Flow (kg/h) 6.986e+005 6.986e+005 Std Ideal Liq VolFlow (m3/h) 700.0 700.0 Molar Enthalpy (kJ/kgmole) -2.853e+05 -2.853e+05 Molar Entropy (kJ/kgmole-C) 5.275e+00 5.275e+00 Heat Flow (kJ/h) -1.106e+10 -1.106e+10 Liq VolFlow @Std Cond (m3/h) 688.4 688.4 PROPERTIES OVERALL AQUEOUS PH. Molecular Weight 18.02 18.02 Molar Density (kgmole/m3) 56.13 56.13 Mass Density (kg/m3) 1011 1011 Act. Volume Flow (m3/h) 690.9 690.9 Mass Enthalpy (kJ/kg) -1.584e+004 -1.584e+004 Mass Entropy (kJ/kg-C) 0.2928 0.2928 Heat Capacity (kJ/kgmole-C) 75.72 75.72 Mass Heat Capacity (kJ/kg-C) 4.203 4.203 LHV Molar Basis (Std) (kJ/kgmole) 0.0000 0.0000 HHV Molar Basis (Std) (kJ/kgmole) 4.101e+004 4.101e+004 HHV Mass Basis (Std) (kJ/kg) 2276 2276 CO2 Loading --- --- CO2 App ML Con (kgmole/m3) --- --- CO2 App WT Con (kgmol/kg) --- --- LHV Mass Basis (Std) (kJ/kg) 0.0000 0.0000 Phase Fraction [Vol. Basis] 0.0000 1.000 Phase Fraction [Mass Basis] 0.0000 1.000 Phase Fraction [Act. Vol. Basis] 0.0000 1.000 Mass Exergy (kJ/kg) 0.6065 --- Partial Pressure of CO2 (kPa) 0.0000 --- Cost Based on Flow (Cost/s) 0.0000 0.0000 Act. Gas Flow (ACT_m3/h) --- --- Avg. Liq. Density (kgmole/m3) 55.40 55.40 Specific Heat (kJ/kgmole-C) 75.72 75.72 Std. Gas Flow (STD_m3/h) 9.169e+005 9.169e+005 Std. Ideal Liq. Mass Density (kg/m3) 998.0 998.0 Act. Liq. Flow (m3/s) 0.1919 0.1919 Z Factor 3.655e-003 3.655e-003 Watson K --- --- User Property --- --- Partial Pressure of H2S (kPa) 0.0000 --- Cp/(Cp - R) 1.123 1.123 Cp/Cv 1.148 1.148 Heat of Vap. (kJ/kgmole) 3.795e+004 --- Kinematic Viscosity (cSt) 0.9907 0.9907 Liq. Mass Density (Std. Cond) (kg/m3) 1015 1015 Liq. Vol. Flow (Std. Cond) (m3/h) 688.4 688.4 Liquid Fraction 1.000 1.000 Molar Volume (m3/kgmole) 1.782e-002 1.782e-002 Mass Heat of Vap. (kJ/kg) 2107 --- Phase Fraction [Molar Basis] 0.0000 1.0000 Surface Tension (dyne/cm) 72.96 72.96 Thermal Conductivity (W/m-K) 0.6034 0.6034 Viscosity (cP) 1.002 1.002 Cv (Semi-Ideal) (kJ/kgmole-C) 67.41 67.41 Mass Cv (Semi-Ideal) (kJ/kg-C) 3.742 3.742 Cv (kJ/kgmole-C) 65.96 65.96 Mass Cv (kJ/kg-C) 3.661 3.661 Cv (Ent. Method) (kJ/kgmole-C) --- --- Mass Cv (Ent. Method) (kJ/kg-C) --- --- Cp/Cv (Ent. Method) --- --- Reid VP at 37.8 C (kPa) 6.553 6.553 True VP at 37.8 C (kPa) 6.553 6.553 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 688.4 688.4 Viscosity Index 3.121 --- COMPOSITION Overall Phase Vapour Fraction 0.0000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 H2O 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 Total 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 Aqueous Phase Phase Fraction 1.000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 H2O 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 Total 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 K VALUE COMPONENTS MIXED LIGHT HEAVY 1-Propanol --- --- --- H2O 0.0000 --- 0.0000 UNIT OPERATIONS FEED TO PRODUCT FROM LOGICAL CONNECTION Heat Exchanger: E-100 UTILITIES ( No utilities reference this stream ) PROCESS UTILITY -------------------------------------------------------------------------------Agua-s (Material Stream): Worksheet, Attachments-------------------------------------------------------------------------------Material Stream: Agua-s Fluid Package: Basis-1 Property Package: UNIQUAC - Ideal CONDITIONS OVERALL AQUEOUS PH. Vapour / Phase Fraction 0.0000 1.0000 Temperature: (C) 40.00 40.00 Pressure: (kPa) 368.2 368.2 Molar Flow (kgmole/h) 3.878e+004 3.878e+004 Mass Flow (kg/h) 6.986e+005 6.986e+005 Std Ideal Liq VolFlow (m3/h) 700.0 700.0 Molar Enthalpy (kJ/kgmole) -2.838e+05 -2.838e+05 Molar Entropy (kJ/kgmole-C) 1.029e+01 1.029e+01 Heat Flow (kJ/h) -1.100e+10 -1.100e+10 Liq VolFlow @Std Cond (m3/h) 688.4 688.4 PROPERTIES OVERALL AQUEOUS PH. Molecular Weight 18.02 18.02 Molar Density (kgmole/m3) 55.29 55.29 Mass Density (kg/m3) 996.0 996.0 Act. Volume Flow (m3/h) 701.4 701.4 Mass Enthalpy (kJ/kg) -1.575e+004 -1.575e+004 Mass Entropy (kJ/kg-C) 0.5712 0.5712 Heat Capacity (kJ/kgmole-C) 76.14 76.14 Mass Heat Capacity (kJ/kg-C) 4.227 4.227 LHV Molar Basis (Std) (kJ/kgmole) 0.0000 0.0000 HHV Molar Basis (Std) (kJ/kgmole) 4.101e+004 4.101e+004 HHV Mass Basis (Std) (kJ/kg) 2276 2276 CO2 Loading --- --- CO2 App ML Con (kgmole/m3) --- --- CO2 App WT Con (kgmol/kg) --- --- LHV Mass Basis (Std) (kJ/kg) 0.0000 0.0000 Phase Fraction [Vol. Basis] 0.0000 1.000 Phase Fraction [Mass Basis] 0.0000 1.000 Phase Fraction [Act. Vol. Basis] 0.0000 1.000 Mass Exergy (kJ/kg) 1.916 --- Partial Pressure of CO2 (kPa) 0.0000 --- Cost Based on Flow (Cost/s) 0.0000 0.0000 Act. Gas Flow (ACT_m3/h) --- --- Avg. Liq. Density (kgmole/m3) 55.40 55.40 Specific Heat (kJ/kgmole-C) 76.14 76.14 Std. Gas Flow (STD_m3/h) 9.169e+005 9.169e+005 Std. Ideal Liq. Mass Density (kg/m3) 998.0 998.0 Act. Liq. Flow (m3/s) 0.1948 0.1948 Z Factor 2.558e-003 2.558e-003 Watson K --- --- User Property --- --- Partial Pressure of H2S (kPa) 0.0000 --- Cp/(Cp - R) 1.123 1.123 Cp/Cv 1.159 1.159 Heat of Vap. (kJ/kgmole) 3.857e+004 --- Kinematic Viscosity (cSt) 0.6540 0.6540 Liq. Mass Density (Std. Cond) (kg/m3) 1015 1015 Liq. Vol. Flow (Std. Cond) (m3/h) 688.4 688.4 Liquid Fraction 1.000 1.000 Molar Volume (m3/kgmole) 1.809e-002 1.809e-002 Mass Heat of Vap. (kJ/kg) 2141 --- Phase Fraction [Molar Basis] 0.0000 1.0000 Surface Tension (dyne/cm) 69.49 69.49 Thermal Conductivity (W/m-K) 0.6315 0.6315 Viscosity (cP) 0.6514 0.6514 Cv (Semi-Ideal) (kJ/kgmole-C) 67.83 67.83 Mass Cv (Semi-Ideal) (kJ/kg-C) 3.765 3.765 Cv (kJ/kgmole-C) 65.68 65.68 Mass Cv (kJ/kg-C) 3.646 3.646 Cv (Ent. Method) (kJ/kgmole-C) --- --- Mass Cv (Ent. Method) (kJ/kg-C) --- --- Cp/Cv (Ent. Method) --- --- Reid VP at 37.8 C (kPa) 6.553 6.553 True VP at 37.8 C (kPa) 6.553 6.553 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 688.4 688.4 Viscosity Index -3.308 --- COMPOSITION Overall Phase Vapour Fraction 0.0000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 H2O 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 Total 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 Aqueous Phase Phase Fraction 1.000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 H2O 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 Total 3.878e+004 1.0000 6.986e+005 1.0000 700.0 1.0000 K VALUE COMPONENTS MIXED LIGHT HEAVY 1-Propanol --- --- --- H2O 0.0000 --- 0.0000 UNIT OPERATIONS FEED TO PRODUCT FROM LOGICAL CONNECTION Heat Exchanger: E-100 UTILITIES ( No utilities reference this stream ) PROCESS UTILITY -------------------------------------------------------------------------------propanol-e (Material Stream): Worksheet, Attachments-------------------------------------------------------------------------------Material Stream: propanol-e Fluid Package: Basis-1 Property Package: UNIQUAC - Ideal CONDITIONS OVERALL VAPOUR PH. LIQUID PH. Vapour / Phase Fraction 1.0000 1.0000 0.0000 Temperature: (C) 120.6 120.6 120.6 Pressure: (kPa) 230.0 230.0 230.0 Molar Flow (kgmole/h) 1208 1208 0.0000 Mass Flow (kg/h) 7.258e+004 7.258e+004 0.0000 Std Ideal Liq VolFlow (m3/h) 90.27 90.27 0.0000 Molar Enthalpy (kJ/kgmole) -2.473e+05 -2.473e+05 -2.868e+05 Molar Entropy (kJ/kgmole-C) 1.856e+02 1.856e+02 9.889e+01 Heat Flow (kJ/h) -2.987e+08 -2.987e+08 0.000e-01 Liq VolFlow @Std Cond (m3/h) 90.18 90.18 0.0000 PROPERTIES OVERALL VAPOUR PH. LIQUID PH. Molecular Weight 60.10 60.10 60.10 Molar Density (kgmole/m3) 7.025e-002 7.025e-002 11.33 Mass Density (kg/m3) 4.222 4.222 680.7 Act. Volume Flow (m3/h) 1.719e+004 1.719e+004 0.0000 Mass Enthalpy (kJ/kg) -4115 -4115 -4772 Mass Entropy (kJ/kg-C) 3.088 3.088 1.646 Heat Capacity (kJ/kgmole-C) 107.3 107.3 208.0 Mass Heat Capacity (kJ/kg-C) 1.786 1.786 3.461 LHV Molar Basis (Std) (kJ/kgmole) 1.844e+006 1.844e+006 1.844e+006 HHV Molar Basis (Std) (kJ/kgmole) 2.008e+006 2.008e+006 2.008e+006 HHV Mass Basis (Std) (kJ/kg) 3.341e+004 3.341e+004 3.341e+004 CO2 Loading --- --- --- CO2 App ML Con (kgmole/m3) --- --- --- CO2 App WT Con (kgmol/kg) --- --- --- LHV Mass Basis (Std) (kJ/kg) 3.068e+004 3.068e+004 3.068e+004 Phase Fraction [Vol. Basis] 1.000 1.000 --- Phase Fraction [Mass Basis] 1.000 1.000 0.0000 Phase Fraction [Act. Vol. Basis] 1.000 1.000 0.0000 Mass Exergy (kJ/kg) 54.98 --- --- Partial Pressure of CO2 (kPa) 0.0000 --- --- Cost Based on Flow (Cost/s) 0.0000 0.0000 0.0000 Act. Gas Flow (ACT_m3/h) 1.719e+004 1.719e+004 --- Avg. Liq. Density (kgmole/m3) 13.38 13.38 13.38 Specific Heat (kJ/kgmole-C) 107.3 107.3 208.0 Std. Gas Flow (STD_m3/h) 2.855e+004 2.855e+004 0.0000 Std. Ideal Liq. Mass Density (kg/m3) 804.0 804.0 804.0 Act. Liq. Flow (m3/s) --- --- --- Z Factor --- 1.000 6.202e-003 Watson K 10.84 10.84 10.84 User Property --- --- --- Partial Pressure of H2S (kPa) 0.0000 --- --- Cp/(Cp - R) 1.084 1.084 1.042 Cp/Cv 1.084 1.084 1.827 Heat of Vap. (kJ/kgmole) 3.950e+004 --- --- Kinematic Viscosity (cSt) 1.892 1.892 0.5227 Liq. Mass Density (Std. Cond) (kg/m3) 804.8 804.8 804.8 Liq. Vol. Flow (Std. Cond) (m3/h) 90.18 90.18 0.0000 Liquid Fraction 0.0000 0.0000 1.000 Molar Volume (m3/kgmole) 14.23 14.23 8.828e-002 Mass Heat of Vap. (kJ/kg) 657.2 --- --- Phase Fraction [Molar Basis] 1.0000 1.0000 0.0000 Surface Tension (dyne/cm) --- --- 14.54 Thermal Conductivity (W/m-K) 1.949e-002 1.949e-002 0.1178 Viscosity (cP) 7.987e-003 7.987e-003 0.3558 Cv (Semi-Ideal) (kJ/kgmole-C) 99.02 99.02 199.7 Mass Cv (Semi-Ideal) (kJ/kg-C) 1.648 1.648 3.323 Cv (kJ/kgmole-C) 99.02 99.02 113.8 Mass Cv (kJ/kg-C) 1.648 1.648 1.894 Cv (Ent. Method) (kJ/kgmole-C) --- --- --- Mass Cv (Ent. Method) (kJ/kg-C) --- --- --- Cp/Cv (Ent. Method) --- --- --- Reid VP at 37.8 C (kPa) 6.192 6.192 6.192 True VP at 37.8 C (kPa) 6.192 6.192 6.192 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 90.18 90.18 0.0000 Viscosity Index -7.544 --- --- COMPOSITION Overall Phase Vapour Fraction 1.0000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Total 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 Vapour Phase Phase Fraction 1.000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Total 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 Liquid Phase Phase Fraction 0.0000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000 K VALUE COMPONENTS MIXED LIGHT HEAVY 1-Propanol 1.000 1.000 --- H2O --- --- --- UNIT OPERATIONS FEED TO PRODUCT FROM LOGICAL CONNECTION Heat Exchanger: E-100 UTILITIES ( No utilities reference this stream ) PROCESS UTILITY -------------------------------------------------------------------------------propanol-s (Material Stream): Worksheet, Attachments-------------------------------------------------------------------------------Material Stream: propanol-s Fluid Package: Basis-1 Property Package: UNIQUAC - Ideal CONDITIONS OVERALL LIQUID PH. Vapour / Phase Fraction 0.0000 1.0000 Temperature: (C) 73.79 73.79 Pressure: (kPa) 228.1 228.1 Molar Flow (kgmole/h) 1208 1208 Mass Flow (kg/h) 7.258e+004 7.258e+004 Std Ideal Liq VolFlow (m3/h) 90.27 90.27 Molar Enthalpy (kJ/kgmole) -2.962e+05 -2.962e+05 Molar Entropy (kJ/kgmole-C) 5.920e+01 5.920e+01 Heat Flow (kJ/h) -3.577e+08 -3.577e+08 Liq VolFlow @Std Cond (m3/h) 90.18 90.18 PROPERTIES OVERALL LIQUID PH. Molecular Weight 60.10 60.10 Molar Density (kgmole/m3) 12.29 12.29 Mass Density (kg/m3) 738.7 738.7 Act. Volume Flow (m3/h) 98.25 98.25 Mass Enthalpy (kJ/kg) -4928 -4928 Mass Entropy (kJ/kg-C) 0.9852 0.9852 Heat Capacity (kJ/kgmole-C) 191.8 191.8 Mass Heat Capacity (kJ/kg-C) 3.192 3.192 LHV Molar Basis (Std) (kJ/kgmole) 1.844e+006 1.844e+006 HHV Molar Basis (Std) (kJ/kgmole) 2.008e+006 2.008e+006 HHV Mass Basis (Std) (kJ/kg) 3.341e+004 3.341e+004 CO2 Loading --- --- CO2 App ML Con (kgmole/m3) --- --- CO2 App WT Con (kgmol/kg) --- --- LHV Mass Basis (Std) (kJ/kg) 3.068e+004 3.068e+004 Phase Fraction [Vol. Basis] 0.0000 1.000 Phase Fraction [Mass Basis] 0.0000 1.000 Phase Fraction [Act. Vol. Basis] 0.0000 1.000 Mass Exergy (kJ/kg) -130.9 --- Partial Pressure of CO2 (kPa) 0.0000 --- Cost Based on Flow (Cost/s) 0.0000 0.0000 Act. Gas Flow (ACT_m3/h) --- --- Avg. Liq. Density (kgmole/m3) 13.38 13.38 Specific Heat (kJ/kgmole-C) 191.8 191.8 Std. Gas Flow (STD_m3/h) 2.855e+004 2.855e+004 Std. Ideal Liq. Mass Density (kg/m3) 804.0 804.0 Act. Liq. Flow (m3/s) 2.729e-002 2.729e-002 Z Factor 6.432e-003 6.432e-003 Watson K 10.84 10.84 User Property --- --- Partial Pressure of H2S (kPa) 0.0000 --- Cp/(Cp - R) 1.045 1.045 Cp/Cv 1.833 1.833 Heat of Vap. (kJ/kgmole) 3.952e+004 --- Kinematic Viscosity (cSt) 0.9700 0.9700 Liq. Mass Density (Std. Cond) (kg/m3) 804.8 804.8 Liq. Vol. Flow (Std. Cond) (m3/h) 90.18 90.18 Liquid Fraction 1.000 1.000 Molar Volume (m3/kgmole) 8.136e-002 8.136e-002 Mass Heat of Vap. (kJ/kg) 657.7 --- Phase Fraction [Molar Basis] 0.0000 1.0000 Surface Tension (dyne/cm) 20.19 20.19 Thermal Conductivity (W/m-K) 0.1340 0.1340 Viscosity (cP) 0.7165 0.7165 Cv (Semi-Ideal) (kJ/kgmole-C) 183.5 183.5 Mass Cv (Semi-Ideal) (kJ/kg-C) 3.054 3.054 Cv (kJ/kgmole-C) 104.7 104.7 Mass Cv (kJ/kg-C) 1.742 1.742 Cv (Ent. Method) (kJ/kgmole-C) --- --- Mass Cv (Ent. Method) (kJ/kg-C) --- --- Cp/Cv (Ent. Method) --- --- Reid VP at 37.8 C (kPa) 6.192 6.192 True VP at 37.8 C (kPa) 6.192 6.192 Liq. Vol. Flow - Sum(Std. Cond) (m3/h) 90.18 90.18 Viscosity Index 2.829 --- COMPOSITION Overall Phase Vapour Fraction 0.0000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Total 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 Liquid Phase Phase Fraction 1.000 COMPONENTS MOLE FLOW MOLE FRAC MASS FLOW MASS FRAC LIQVOL FLOW LIQVOL FRAC (kgmole/h) (kg/h) (m3/h) 1-Propanol 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 H2O 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 Total 1208 1.0000 7.258e+004 1.0000 90.27 1.0000 K VALUE COMPONENTS MIXED LIGHT HEAVY 1-Propanol 0.0000 0.0000 --- H2O --- --- --- UNIT OPERATIONS FEED TO PRODUCT FROM LOGICAL CONNECTION Heat Exchanger: E-100 UTILITIES ( No utilities reference this stream ) PROCESS UTILITY -------------------------------------------------------------------------------E-100 (Heat Exchanger): Design, Rating, Details, Tables, HTFS Results, Exchanger Design and Rating-------------------------------------------------------------------------------Heat Exchanger: E-100 CONNECTIONS Tube Side Shell Side Inlet Outlet Inlet Outlet Name Agua-e Name Agua-s Name propanol-e Name propanol-s From Op. To Op. From Op. To Op. Op. Type Op. Type Op. Type Op. Type Temp 20.00 C Temp 40.00 C Temp 120.64 C Temp 73.79 C PARAMETERS Heat Exchanger Model: Simple Steady State Rating Tube Side Data Shell Side Data Heat Transfer Coeff 42356.12 kJ/h-m2-C Heat Transfer Coeff 10615.65 kJ/h-m2-C Tube Pressure Drop 131.81 kPa Shell Pressure Drop 1.95 kPa Fouling 0.00000 C-h-m2/kJ Fouling 0.00000 C-h-m2/kJ Tube Length 4.00 m Shell Passes 1 Tube O.D. 19.05 mm Shell Series 1 Tube Thickness 1.2446 mm Shell Parallel 1 Tube Pitch 23.0000 mm Baffle Type Single Orientation Horizontal Baffle Cut(%Area) 20.00 Passes Per Shell 2 Baffle Orientation Horizontal Tubes Per Shell 500 Spacing 800.0000 mm Layout Angle Triangular (30 degrees) Diameter 1000.0000 mm TEMA Type A E L Area 119.69 m2 SPECS Spec Value Curr Value Rel Error Active Estimate E-100 Heat Balance 0.0000 kJ/h -2.488e-007 kJ/h -4.219e-015 On Off E-100 UA 9.236e+005 kJ/C-h 9.236e+005 kJ/C-h 0.0000 On Off Detailed Specifications E-100 Heat Balance Type: Duty Pass: Error Spec Value: 0.0000 kJ/h E-100 UA Type: UA Pass: Overall Spec Value: 9.236e+005 kJ/C-h User Variables RATING Sizing Overall Data Configuration # of Shells in Series 1 Tube Passes per Shell 2 Elevation (Base) 0.0000 m # of Shells in Parallel 1 Exchange Orientation Horizontal First Tube Pass Flow Direction Counter TEMA Type: A E L Calculated Information Shell HT Coeff 1.062e+004 kJ/h-m2-C Tube HT Coeff 4.236e+004 kJ/h-m2-C Overall U 7717 kJ/h-m2-C Overall UA 9.236e+005 kJ/C-h Shell DP 1.952 kPa Tube DP 131.8 kPa Shell Vol per Shell 2.572 m3 Tube Vol per Shell 0.4308 m3 HT Area per Shell 119.7 m2 Shell Data Shell and Tube Bundle Shell Diameter 1000 Tube Pitch 23.00 Shell Fouling 0.0000 (mm) (mm) (C-h-m2/kJ) # of Tubes per Shell 500 Tube Layout Angle Triangular (30 degrees) Shell Baffles Shell Baffle Type Single Shell Baffle Orientation Horizontal Baffle Cut (%Area) 20.00 Baffle Spacing 800.0 mm Tube Data Dimensions OD 19.05 ID 16.56 Tube Thickness 1.245 Tube Length 4.000 (mm) (mm) (mm) (m) Tube Properties Tube Fouling 0.0000 Thermal Cond. 45.00 Wall Cp --- Wall Density --- (C-h-m2/kJ) (W/m-K) (kJ/kg-C) (kg/m3) Nozzle Parameters Base Elevation Relative to Ground Level 0.0000 m Agua-e propanol-e Agua-s Diameter (m) 5.000e-002 5.000e-002 5.000e-002 Elevation (Base) (m) 0.0000 0.0000 0.0000 Elevation (Ground) (m) 0.0000 0.0000 0.0000 Elevation (% of Height) (%) 0.00 0.00 0.00 propanol-s Diameter (m) 5.000e-002 Elevation (Base) (m) 0.0000 Elevation (Ground) (m) 0.0000 Elevation (% of Height) (%) 0.00 DETAILS Overall/Detailed Performance Duty: 5.898e+07 kJ/h UA Curv. Error: 0.00e-01 kJ/C-h Heat Leak: 0.000e-01 kJ/h Hot Pinch Temp: 73.79 C Heat Loss: 0.000e-01 kJ/h Cold Pinch Temp: 20.00 C UA: 9.236e+05 kJ/C-h Ft Factor: --- Min. Approach: 53.79 C Uncorrected Lmtd: 66.31 C Lmtd: 63.86 C TABLES Shell Side - Overall Phase Temperature Pressure Heat Flow Enthalpy (C) (kPa) (kJ/h) (kJ/kgmole) 73.79 230.01 0.00 -296151.42 120.64 230.01 11286280.92 -286805.84 120.64 230.01 58984383.23 -247309.53 UA Molar Vap Frac Mass Vap Frac Heat of Vap. (kJ/C-h) (kJ/kgmole) 0.00 0.0000 0.0000 --- 0.00 0.0000 0.0000 --- 0.00 1.0000 1.0000 --- Shell Side - Vapour Phase Mass Flow Molecular Wt Density Mass Sp Heat Viscosity Thermal Cond (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) --- --- --- --- --- --- 0.00 60.10 4.22 1.79 0.01 0.02 72575.52 60.10 4.22 1.79 0.01 0.02 Std Gas Flow Z Factor Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (STD_m3/h) (kPa) (C) --- --- --- --- --- --- 0.00 1.00 5170.00 263.65 0.24 0.62 28554.44 1.00 5170.00 263.65 0.24 0.62 Shell Side - Light Liquid Phase Mass Flow Density Mass Sp Heat Viscosity Thermal Cond Surface Tens (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) (dyne/cm) 72575.52 738.68 3.19 0.72 0.13 20.19 72575.52 680.75 3.46 0.36 0.12 14.54 0.00 680.74 3.46 0.36 0.12 --- Molecular Wt Sp Gravity Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (kPa) (C) 60.10 0.74 5170.00 263.65 0.24 0.62 60.10 0.68 5170.00 263.65 0.24 0.62 60.10 0.68 5170.00 263.65 0.24 0.62 Shell Side - Heavy Liquid Phase Mass Flow Density Mass Sp Heat Viscosity Thermal Cond Surface Tens (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) (dyne/cm) --- --- --- --- --- 20.19 --- --- --- --- --- 14.54 --- --- --- --- --- --- Molecular Wt Sp Gravity Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (kPa) (C) --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- Shell Side - Mixed Liquid Mass Flow Density Mass Sp Heat Viscosity Thermal Cond Surface Tens (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) (dyne/cm) --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- Molecular Wt Sp Gravity Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (kPa) (C) --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- --- Tube Side - Overall Phase Temperature Pressure Heat Flow Enthalpy (C) (kPa) (kJ/h) (kJ/kgmole) 20.00 500.00 0.00 -285274.80 40.00 500.00 58984383.23 -283753.76 UA Molar Vap Frac Mass Vap Frac Heat of Vap. (kJ/C-h) (kJ/kgmole) 0.00 0.0000 0.0000 --- 0.00 0.0000 0.0000 --- Tube Side - Vapour Phase Mass Flow Molecular Wt Density Mass Sp Heat Viscosity Thermal Cond (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) --- --- --- --- --- --- --- --- --- --- --- --- Std Gas Flow Z Factor Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (STD_m3/h) (kPa) (C) --- --- --- --- --- --- --- --- --- --- --- --- Tube Side - Light Liquid Phase Mass Flow Density Mass Sp Heat Viscosity Thermal Cond Surface Tens (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) (dyne/cm) --- --- --- --- --- 72.96 --- --- --- --- --- 69.49 Molecular Wt Sp Gravity Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (kPa) (C) --- --- --- --- --- --- --- --- --- --- --- --- Tube Side - Heavy Liquid Phase Mass Flow Density Mass Sp Heat Viscosity Thermal Cond Surface Tens (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) (dyne/cm) 698610.52 1011.20 4.20 1.00 0.60 72.96 698610.52 996.08 4.23 0.65 0.63 69.49 Molecular Wt Sp Gravity Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (kPa) (C) 18.02 1.01 22120.00 374.15 0.26 0.34 18.02 1.00 22120.00 374.15 0.26 0.34 Tube Side - Mixed Liquid Mass Flow Density Mass Sp Heat Viscosity Thermal Cond Surface Tens (kg/h) (kg/m3) (kJ/kg-C) (cP) (W/m-K) (dyne/cm) --- --- --- --- --- --- --- --- --- --- --- --- Molecular Wt Sp Gravity Pseudo Pc Pseudo Tc Pseudo Zc Pseudo Omega (kPa) (C) --- --- --- --- --- --- --- --- --- --- --- --- HTFS Exchanger Design and Rating -------------------------------------------------------------------------------Aspen Technology Inc. Aspen HYSYS Version 8.6 (32.0.0.8628)