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authorSashi202024-04-16 00:20:36 +0550
committerSashi202024-04-16 00:20:36 +0550
commit546b9fb398e5c3e30a6cab6e25ceb07140ee5530 (patch)
tree4357f92b74ed02b253410927c991045f9e7e7cfd
parent0229ac0e2b7376c5bc78bf1490ff19ca22162662 (diff)
downloadDWSIM-Flowsheets-546b9fb398e5c3e30a6cab6e25ceb07140ee5530.tar.gz
DWSIM-Flowsheets-546b9fb398e5c3e30a6cab6e25ceb07140ee5530.tar.bz2
DWSIM-Flowsheets-546b9fb398e5c3e30a6cab6e25ceb07140ee5530.zip
Added(A)/Deleted(D) following Flowsheet file
A Aspirin_Production_By_Ms_Nitharsana_And_Tharini/ABSTRACT.pdf A Aspirin_Production_By_Ms_Nitharsana_And_Tharini/FLOWSHEET.dwxmz A Aspirin_Production_By_Ms_Nitharsana_And_Tharini/user_defined_compound/Compound.zip D Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf D Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml M Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf M Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz R Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf -> Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/Abstract_2.pdf R Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz -> Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz A Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/README.txt
Diffstat
-rw-r--r--Aspirin_Production_By_Ms_Nitharsana_And_Tharini/ABSTRACT.pdfbin0 -> 249766 bytes
-rw-r--r--Aspirin_Production_By_Ms_Nitharsana_And_Tharini/FLOWSHEET.dwxmzbin0 -> 239463 bytes
-rw-r--r--Aspirin_Production_By_Ms_Nitharsana_And_Tharini/user_defined_compound/Compound.zip3
-rw-r--r--Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdfbin298877 -> 0 bytes
-rw-r--r--Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml13965
-rw-r--r--Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdfbin194181 -> 417838 bytes
-rw-r--r--Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmzbin102116 -> 99621 bytes
-rw-r--r--Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/Abstract_2.pdf (renamed from Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf)bin112681 -> 112681 bytes
-rw-r--r--Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz (renamed from Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz)bin53210 -> 53210 bytes
-rw-r--r--Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/README.txt8
10 files changed, 11 insertions, 13965 deletions
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diff --git a/Aspirin_Production_By_Ms_Nitharsana_And_Tharini/FLOWSHEET.dwxmz b/Aspirin_Production_By_Ms_Nitharsana_And_Tharini/FLOWSHEET.dwxmz
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Binary files differ
diff --git a/Aspirin_Production_By_Ms_Nitharsana_And_Tharini/user_defined_compound/Compound.zip b/Aspirin_Production_By_Ms_Nitharsana_And_Tharini/user_defined_compound/Compound.zip
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diff --git a/Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf b/Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf
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diff --git a/Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml b/Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>7.08711243250292E-09</MassFlow>
- <MolarFlow>2.52990084477533E-07</MolarFlow>
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- <VolumetricFlow>-8.80881049848287E-12</VolumetricFlow>
- <VolumetricFraction>-3.00133365651828E-06</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid1</ComponentName>
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- <Name>Liquid1</Name>
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- <Properties>
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- <density>992.880312614391</density>
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- <enthalpyF>-3139.9216633402</enthalpyF>
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- <entropyF>0.22359339973142</entropyF>
- <heatCapacityCp>0</heatCapacityCp>
- <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
- <kinematic_viscosity>6.60823464333775E-06</kinematic_viscosity>
- <massflow>0.0029140693846217</massflow>
- <massfraction>1</massfraction>
- <molar_enthalpy>4428.78407183885</molar_enthalpy>
- <molar_entropy>13.6588783726299</molar_entropy>
- <molarflow>0.0477027954263735</molarflow>
- <molarfraction>1</molarfraction>
- <molecularWeight>61.0880213324059</molecularWeight>
- <speedOfSound>NaN</speedOfSound>
- <surfaceTension>0.0454245135291819</surfaceTension>
- <thermalConductivity>0.243062055268972</thermalConductivity>
- <viscosity>0.00656118607850643</viscosity>
- <volumetric_flow>2.93496542090612E-06</volumetric_flow>
- <bulk_modulus>-707.906392210169</bulk_modulus>
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- <helmholtz_energy>-0.121796803594762</helmholtz_energy>
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- <isothermal_compressibility>-0.00141261614671663</isothermal_compressibility>
- <molar_gibbs_free_energy>8.68112995993981E-13</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-7.44032573621568</molar_helmholtz_energy>
- <molar_internal_energy>4421.34374610263</molar_internal_energy>
- <idealGasHeatCapacityCp>1.48518290399594</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.10088228324838</idealGasHeatCapacityRatio>
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- </Phase>
- <Phase>
- <ID>4</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
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- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
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- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
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- <VolumetricFlow>0</VolumetricFlow>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
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- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
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- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>2322.27760959675</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
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- <PartialVolume>-0.0350155913091071</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>-0.0497228838295276</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0615570993219995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>96488.3007612835</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
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- <PartialVolume>-0.0346913527806408</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid2</ComponentName>
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- <Name>Liquid2</Name>
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- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <surfaceTension>0</surfaceTension>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>5</ID>
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
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- <PartialVolume>0.0182531027228281</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155913091071</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0497228838295276</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0615570993219995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
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- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
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- <PartialVolume>-0.0346913527806408</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid3</ComponentName>
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- <Name>Liquid3</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>6</ID>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
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- <Name>Water</Name>
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- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155913091071</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
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- <PartialVolume>-0.0497228838295276</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
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- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
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- <PartialVolume>0.0615570993219995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
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- <PartialVolume>-0.0346913527806408</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Aqueous</ComponentName>
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- <Name>Aqueous</Name>
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- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
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- <Phase>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
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- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
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- <PartialVolume>0.0182531027228281</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
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- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155913091071</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
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- <Compound>
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- <Compound>
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- <ComponentName>Carbon dioxide</ComponentName>
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- <ComponentName>Sulfur dioxide</ComponentName>
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- <ComponentName>Monoethanolamine</ComponentName>
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- <ComponentName>Water</ComponentName>
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- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>NaN</MassFraction>
- <MoleFraction>NaN</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0.0265647773035096</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>NaN</MassFlow>
- <MolarFlow>NaN</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>46284.5784688987</PartialPressure>
- <PartialVolume>0.0183303060479418</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>1.21253204225363</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>NaN</MassFraction>
- <MoleFraction>NaN</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>77.2142096856098</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>NaN</MassFlow>
- <MolarFlow>NaN</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>450.242476336638</PartialPressure>
- <PartialVolume>-0.0350155913524995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>1.15105441306453</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>NaN</MassFraction>
- <MoleFraction>NaN</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>4.53852141658536</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>NaN</MassFlow>
- <MolarFlow>NaN</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>6659.07425640751</PartialPressure>
- <PartialVolume>-0.0508427234926757</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0.827074445666472</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>NaN</MassFraction>
- <MoleFraction>NaN</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0.000524876205513825</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>NaN</MassFlow>
- <MolarFlow>NaN</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>47930.6935199136</PartialPressure>
- <PartialVolume>0.0619774348694148</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>3.77083694454363</ActivityCoeff>
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- <MassFraction>NaN</MassFraction>
- <MoleFraction>NaN</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>85327.7407681554</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>NaN</MassFlow>
- <MolarFlow>NaN</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0.41127844360902</PartialPressure>
- <PartialVolume>-0.0346914052009311</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>OverallLiquid</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>OverallLiquid</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <density>0</density>
- <enthalpy>0</enthalpy>
- <entropy>0</entropy>
- <heatCapacityCp>0</heatCapacityCp>
- <heatCapacityCv>0</heatCapacityCv>
- <kinematic_viscosity>0</kinematic_viscosity>
- <massflow>0</massflow>
- <massfraction>0</massfraction>
- <molar_enthalpy>NaN</molar_enthalpy>
- <molar_entropy>NaN</molar_entropy>
- <molarflow>0</molarflow>
- <molarfraction>0</molarfraction>
- <molecularWeight>NaN</molecularWeight>
- <surfaceTension>NaN</surfaceTension>
- <thermalConductivity>0</thermalConductivity>
- <viscosity>0</viscosity>
- <volumetric_flow>0</volumetric_flow>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>NaN</molar_gibbs_free_energy>
- <molar_helmholtz_energy>NaN</molar_helmholtz_energy>
- <molar_internal_energy>NaN</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>2</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
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- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
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- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
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- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
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- <DiffusionCoefficient>1.83324442191774E-10</DiffusionCoefficient>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
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- <MassFraction>0.371015649265493</MassFraction>
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- <Molarity>10.247558118619</Molarity>
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- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0.0684592769896</MassFlow>
- <MolarFlow>1.5555568</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>28371</PartialPressure>
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- <VolumetricFraction>0.371015649265493</VolumetricFraction>
- <DiffusionCoefficient>7.26386790212642E-11</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0.089137741993155</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0.0385771779005746</MassFraction>
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- <Molarity>0.731968437044213</Molarity>
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- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0.00711820569456</MassFlow>
- <MolarFlow>0.1111112</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>2026.5</PartialPressure>
- <PartialVolume>52.7033352098547</PartialVolume>
- <VolumetricFlow>0.00585593081916921</VolumetricFlow>
- <VolumetricFraction>0.0385771779005746</VolumetricFraction>
- <DiffusionCoefficient>4.48764822025523E-11</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>1</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
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- <PartialVolume>50.2511877361376</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>3.99691475656972E-11</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
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- <Molarity>25.6188952965474</Molarity>
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- <MassFlow>0.1089410871528</MassFlow>
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- <Name>Nitrogen</Name>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Vapor</ComponentName>
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- <Name>Vapor</Name>
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- <Properties>
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- <molecularWeight>33.213316</molecularWeight>
- <speedOfSound>NaN</speedOfSound>
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- <molar_gibbs_free_energy>-5084.38820960058</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-7850.00166411104</molar_helmholtz_energy>
- <molar_internal_energy>3709.33845370623</molar_internal_energy>
- <idealGasHeatCapacityCp>0.963961140556312</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.35076696667345</idealGasHeatCapacityRatio>
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- <ComponentDescription></ComponentDescription>
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- <Compound>
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- <ComponentName>Sulfur dioxide</ComponentName>
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- <Name>Monoethanolamine</Name>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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- <Name>Nitrogen</Name>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid1</ComponentName>
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- <surfaceTension>0.0150336108555471</surfaceTension>
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- <molar_helmholtz_energy>0</molar_helmholtz_energy>
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- <idealGasHeatCapacityCp>1.41130821640742</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.1652965684796</idealGasHeatCapacityRatio>
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- <Phase>
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- <ComponentName>Water</ComponentName>
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- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
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- <MassFlow>0</MassFlow>
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- <Name>Water</Name>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
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- <DynamicProperties />
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- <Compound>
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- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>3842.55376191225</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155913524995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>-0.0508427234926757</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0619774348694148</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>149623.345545145</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346914052009311</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid2</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid2</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <surfaceTension>0</surfaceTension>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>5</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183303060479418</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155913524995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0508427234926757</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0619774348694148</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346914052009311</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid3</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid3</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>6</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0183303060479418</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155913524995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0508427234926757</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0619774348694148</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
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- <PartialVolume>-0.0346914052009311</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Aqueous</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Aqueous</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>7</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
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- <MassFlow>0</MassFlow>
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- <Name>Water</Name>
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- <PartialVolume>0.0183303060479418</PartialVolume>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
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- <FugacityCoeff>1</FugacityCoeff>
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- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
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- <PartialVolume>-0.0350155913524995</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
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- <MassFlow>0</MassFlow>
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- <Name>Sulfur dioxide</Name>
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- <PartialVolume>-0.0508427234926757</PartialVolume>
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- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
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- <Name>Monoethanolamine</Name>
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- <PartialVolume>0.0619774348694148</PartialVolume>
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- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
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- <PartialVolume>-0.0346914052009311</PartialVolume>
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- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Solid</ComponentName>
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- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
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- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
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- </Properties>
- </Phase>
- </Phases>
- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
- <ObjectClass>Streams</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
- <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mass</DefinedFlow>
- <ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-637.442971504406</TotalEnergyFlow>
- <AtEquilibrium>true</AtEquilibrium>
- <ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-913864fa-289f-465d-ab44-51ef0e4a8fbc</ComponentName>
- <Name2>MAT-913864fa-289f-465d-ab44-51ef0e4a8fbc</Name2>
- <code>0</code>
- <InputComposition />
- <IsElectrolyteStream>false</IsElectrolyteStream>
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- <enthalpy>194.455107341953</enthalpy>
- <enthalpyF>-3413.15840142928</enthalpyF>
- <entropy>1.04115381207016</entropy>
- <entropyF>0.827895575237749</entropyF>
- <heatCapacityCp>0.965856733894926</heatCapacityCp>
- <heatCapacityCv>0.71049223623676</heatCapacityCv>
- <jouleThomsonCoefficient>-9.54585666363771E-09</jouleThomsonCoefficient>
- <kinematic_viscosity>1.32169255154564E-05</kinematic_viscosity>
- <massflow>0.186760441952378</massflow>
- <massfraction>1</massfraction>
- <molar_enthalpy>6399.92367250975</molar_enthalpy>
- <molar_entropy>34.2665462464507</molar_entropy>
- <molarflow>5.67452420457363</molarflow>
- <molarfraction>1</molarfraction>
- <molecularWeight>32.9120883477509</molecularWeight>
- <speedOfSound>NaN</speedOfSound>
- <thermalConductivity>0.023007545535211</thermalConductivity>
- <viscosity>1.73950076089757E-05</viscosity>
- <volumetric_flow>0.141902717492612</volumetric_flow>
- <bulk_modulus>-135320.125921293</bulk_modulus>
- <gibbs_free_energy>-122.854152068868</gibbs_free_energy>
- <helmholtz_energy>-199.709399318849</helmholtz_energy>
- <internal_energy>117.599860091972</internal_energy>
- <isothermal_compressibility>-7.38988375300239E-06</isothermal_compressibility>
- <molar_gibbs_free_energy>-4043.38670677862</molar_gibbs_free_energy>
- <molar_helmholtz_energy>-6572.85339425824</molar_helmholtz_energy>
- <molar_internal_energy>3870.45698503013</molar_internal_energy>
- <idealGasHeatCapacityCp>0.963146369684847</idealGasHeatCapacityCp>
- <idealGasHeatCapacityRatio>1.35552463891503</idealGasHeatCapacityRatio>
- </Properties>
- </Phase>
- <Phase>
- <ID>3</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0181160870461316</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155916071534</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0475296063454627</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.060661778332129</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
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- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346913833362274</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid1</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid1</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <surfaceTension>0</surfaceTension>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>4</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0181160870461316</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155916071534</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0475296063454627</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.060661778332129</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346913833362274</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid2</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid2</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <surfaceTension>0</surfaceTension>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>5</ID>
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
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- <PartialVolume>0.0181160870461316</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155916071534</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0475296063454627</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.060661778332129</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
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- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
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- <PartialVolume>-0.0346913833362274</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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- <ComponentName>Liquid3</ComponentName>
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- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
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- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Name>Water</Name>
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- <PartialVolume>0.0181160870461316</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
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- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155916071534</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0475296063454627</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.060661778332129</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
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- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
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- </Compound>
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- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0182530668217087</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155915784445</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0497223505392422</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0615568933158706</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346913854570536</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid3</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid3</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>6</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0182530668217087</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155915784445</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0497223505392422</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0615568933158706</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346913854570536</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Aqueous</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Aqueous</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>7</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0182530668217087</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155915784445</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0497223505392422</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0615568933158706</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346913854570536</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Solid</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Solid</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- </Phases>
- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.Heater</Type>
- <ObjectClass>Exchangers</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
- <FixOnHeat>true</FixOnHeat>
- <Eficiencia>100</Eficiencia>
- <OutletVaporFraction>2.46118534176295E-06</OutletVaporFraction>
- <OutletTemperature>354.33</OutletTemperature>
- <CalcMode>OutletTemperature</CalcMode>
- <DeltaT>30.0878513391419</DeltaT>
- <DeltaQ>0.254059909379867</DeltaQ>
- <MobileCompatible>true</MobileCompatible>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>Aquecedor</ComponentDescription>
- <ComponentName>AQ-a0ad804b-a1ce-4722-88a1-a1cf95d5bd50</ComponentName>
- <IsDirty>true</IsDirty>
- <CanUsePreviousResults>false</CanUsePreviousResults>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>02/03/2024 15:34:32</LastUpdated>
- <ErrorMessage></ErrorMessage>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>AQ-a0ad804b-a1ce-4722-88a1-a1cf95d5bd50</Name>
- <UserDefinedChartNames />
- <ProductName>Heater</ProductName>
- <ProductDescription>Simple heater model</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>8.6.8.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <IsSource>false</IsSource>
- <IsSink>false</IsSink>
- <DynamicProperties>
- <Property>
- <Name>Flow Conductance</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>1.0</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>1.0</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>101325.0</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>-1.0</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>0.0</Data>
- </Property>
- </DynamicProperties>
- <DynamicPropertiesDescriptions>
- <Property>
- <Name>Flow Conductance</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Flow Conductance (inverse of Resistance) of this Unit Operation."</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Heater Volume"</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Initializes the volume content with information from the inlet stream, if the content is null."</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>System.String</PropertyType>
- <Data>"Empties the volume content on the next run."</Data>
- </Property>
- </DynamicPropertiesDescriptions>
- <DynamicPropertiesUnitTypes>
- <Property>
- <Name>Flow Conductance</Name>
- <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
- <Data>67</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
- <Data>63</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
- <Data>46</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
- <Data>66</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>DWSIM.Interfaces.Enums.UnitOfMeasure</PropertyType>
- <Data>66</Data>
- </Property>
- </DynamicPropertiesUnitTypes>
- <AttachedUtilities />
- <PropertyPackage>PP-1e37eef4-3b36-471d-bec1-e3a7631125c5</PropertyPackage>
- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
- <ObjectClass>Streams</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <ComponentDescription>CorrentedeEnergia</ComponentDescription>
- <ComponentName>EN-46cbf572-c01f-4e37-a8ed-ec90e9876fd8</ComponentName>
- <EnergyFlow>0.254059909379867</EnergyFlow>
- <MobileCompatible>true</MobileCompatible>
- <Name2>EN-46cbf572-c01f-4e37-a8ed-ec90e9876fd8</Name2>
- <code>0</code>
- <IsDirty>true</IsDirty>
- <CanUsePreviousResults>false</CanUsePreviousResults>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>02/03/2024 15:34:32</LastUpdated>
- <ErrorMessage></ErrorMessage>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
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- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>4353.92180045303</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155917089681</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>-0.0540460893138245</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>NaN</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0.0630518498814736</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>146707.500493725</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346914861424796</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid2</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid2</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <surfaceTension>0</surfaceTension>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>5</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0185565729086876</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155917089681</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0540460893138245</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0630518498814736</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346914861424796</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Liquid3</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Liquid3</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>6</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0185565729086876</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155917089681</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0540460893138245</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0630518498814736</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346914861424796</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Aqueous</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Aqueous</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- <Phase>
- <ID>7</ID>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Water</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Water</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0185565729086876</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Carbon dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Carbon dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0350155917089681</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Sulfur dioxide</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Sulfur dioxide</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0540460893138245</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Monoethanolamine</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Monoethanolamine</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0.0630518498814736</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>Infinity</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Nitrogen</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>1</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Nitrogen</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>-0.0346914861424796</PartialVolume>
- <VolumetricFlow>0</VolumetricFlow>
- <VolumetricFraction>0</VolumetricFraction>
- <DiffusionCoefficient>NaN</DiffusionCoefficient>
- <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
- <EntropyF_Dmol>0</EntropyF_Dmol>
- <DynamicProperties />
- </Compound>
- </Compounds>
- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Solid</ComponentName>
- <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
- <Name>Solid</Name>
- <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
- <Properties>
- <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
- <gibbs_free_energy>0</gibbs_free_energy>
- <helmholtz_energy>0</helmholtz_energy>
- <internal_energy>0</internal_energy>
- <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
- <molar_helmholtz_energy>0</molar_helmholtz_energy>
- <molar_internal_energy>0</molar_internal_energy>
- </Properties>
- </Phase>
- </Phases>
- </SimulationObject>
- </SimulationObjects>
- <Settings>
- <Type>DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables</Type>
- <SelectedPropertyPackage>
- <Type>DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage</Type>
- <ComponentName>NRTL</ComponentName>
- <ComponentDescription>Uses NRTL (Non-Random Two-Liquid) model to calculate liquid-phase activity coefficients.</ComponentDescription>
- <Tag>NRTL (1)</Tag>
- <UseHenryConstants>true</UseHenryConstants>
- <AutoEstimateMissingNRTLUNIQUACParameters>true</AutoEstimateMissingNRTLUNIQUACParameters>
- <SingleCompoundCheckThreshold>0.99999</SingleCompoundCheckThreshold>
- <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
- <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
- <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
- <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
- <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
- <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
- <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
- <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
- <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
- <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
- <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
- <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
- <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
- <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
- <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
- <EnthalpyEntropyCpCvCalculationMode>LiqCp_Excess</EnthalpyEntropyCpCvCalculationMode>
- <LiquidEnthalpyEntropyCpCvCalculationMode_EOS>EOS</LiquidEnthalpyEntropyCpCvCalculationMode_EOS>
- <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
- <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
- <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
- <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
- <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
- <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
- <ForcedSolids>[]</ForcedSolids>
- <PropertyOverrides>{}</PropertyOverrides>
- <InteractionParameters_PR />
- <InteractionParameters_NRTL />
- <FlashSettings>
- <Setting Name="Replace_PTFlash" Value="False" />
- <Setting Name="ValidateEquilibriumCalc" Value="False" />
- <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
- <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
- <Setting Name="ValidationGibbsTolerance" Value="0.01" />
- <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
- <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
- <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
- <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
- <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
- <Setting Name="NL_FastMode" Value="True" />
- <Setting Name="IO_FastMode" Value="True" />
- <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
- <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
- <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
- <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
- <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
- <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
- <Setting Name="ST_Number_of_Random_Tries" Value="20" />
- <Setting Name="CheckIncipientLiquidForStability" Value="False" />
- <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
- <Setting Name="PTFlash_DampingFactor" Value="1.0" />
- <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
- <Setting Name="ImmiscibleWaterOption" Value="False" />
- <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
- <Setting Name="UseIOFlash" Value="False" />
- <Setting Name="GibbsMinimizationExternalSolver" Value="" />
- <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
- <Setting Name="PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases" Value="False" />
- <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
- <Setting Name="FailSafeCalculationMode" Value="1" />
- </FlashSettings>
- </SelectedPropertyPackage>
- <SimulationMode></SimulationMode>
- <BackupFileName>69258485.dwbcs</BackupFileName>
- <FilePath>C:\Users\pc\AppData\Local\DWSIM\DWSIM12.dwxmz</FilePath>
- <FlowsheetQuickConnect>false</FlowsheetQuickConnect>
- <FlowsheetShowCalculationQueue>false</FlowsheetShowCalculationQueue>
- <FlowsheetShowConsoleWindow>false</FlowsheetShowConsoleWindow>
- <FlowsheetShowCOReportsWindow>false</FlowsheetShowCOReportsWindow>
- <FlowsheetShowWatchWindow>false</FlowsheetShowWatchWindow>
- <FlowsheetMultiSelectMode>false</FlowsheetMultiSelectMode>
- <FlowsheetSnapToGrid>false</FlowsheetSnapToGrid>
- <FlowsheetDisplayGrid>false</FlowsheetDisplayGrid>
- <FractionNumberFormat>G8</FractionNumberFormat>
- <Key>9E4057B968E8F3CFA0B7056FDEAE7201215A5F71</Key>
- <NumberFormat>G6</NumberFormat>
- <Password></Password>
- <SimulationAuthor>DESKTOP-TV6G6KQ\pc</SimulationAuthor>
- <SimulationComments></SimulationComments>
- <SimulationName>MySimulation_35</SimulationName>
- <UsePassword>false</UsePassword>
- <SelectedUnitSystem1>
- <Type>DWSIM.SharedClasses.SystemsOfUnits.SI</Type>
- <accel>m2/s</accel>
- <activity>Pa</activity>
- <activityCoefficient>-</activityCoefficient>
- <area>m2</area>
- <cakeresistance>m/kg</cakeresistance>
- <cinematic_viscosity>m2/s</cinematic_viscosity>
- <compressibility>1/Pa</compressibility>
- <compressibilityfactor>-</compressibilityfactor>
- <deltaP>Pa</deltaP>
- <deltaT>K.</deltaT>
- <density>kg/m3</density>
- <diameter>mm</diameter>
- <distance>m</distance>
- <enthalpy>kJ/kg</enthalpy>
- <entropy>kJ/[kg.K]</entropy>
- <excessEnthalpy>kJ/kg</excessEnthalpy>
- <excessEntropy>kJ/[kg.K]</excessEntropy>
- <force>N</force>
- <foulingfactor>K.m2/W</foulingfactor>
- <fugacity>Pa</fugacity>
- <fugacityCoefficient>-</fugacityCoefficient>
- <gor>m3/m3</gor>
- <head>m</head>
- <heat_transf_coeff>W/[m2.K]</heat_transf_coeff>
- <heatCapacityCp>kJ/[kg.K]</heatCapacityCp>
- <heatCapacityCv>kJ/[kg.K]</heatCapacityCv>
- <heatflow>kW</heatflow>
- <heat>kJ</heat>
- <idealGasHeatCapacity>kJ/[kg.K]</idealGasHeatCapacity>
- <jouleThomsonCoefficient>K/Pa</jouleThomsonCoefficient>
- <kvalue>-</kvalue>
- <logfugacityCoefficient>-</logfugacityCoefficient>
- <logKvalue>-</logKvalue>
- <mass>kg</mass>
- <mass_conc>kg/m3</mass_conc>
- <massflow>kg/s</massflow>
- <massfraction>-</massfraction>
- <mediumresistance>m-1</mediumresistance>
- <molar_conc>mol/m3</molar_conc>
- <molar_enthalpy>kJ/kmol</molar_enthalpy>
- <molar_entropy>kJ/[kmol.K]</molar_entropy>
- <molar_volume>m3/kmol</molar_volume>
- <molarflow>mol/s</molarflow>
- <molarfraction>-</molarfraction>
- <molecularWeight>kg/kmol</molecularWeight>
- <Name>SI</Name>
- <pdp_boilingPointTemperature>K</pdp_boilingPointTemperature>
- <pdp_meltingTemperature>K</pdp_meltingTemperature>
- <pressure>Pa</pressure>
- <reac_rate>mol/[m3.s]</reac_rate>
- <reac_rate_heterog>mol/[kg.s]</reac_rate_heterog>
- <spec_vol>m3/kg</spec_vol>
- <speedOfSound>m/s</speedOfSound>
- <surfaceTension>N/m</surfaceTension>
- <temperature>K</temperature>
- <thermalConductivity>W/[m.K]</thermalConductivity>
- <thermalConductivityOfLiquid>W/[m.K]</thermalConductivityOfLiquid>
- <thermalConductivityOfVapor>W/[m.K]</thermalConductivityOfVapor>
- <thickness>mm</thickness>
- <time>s</time>
- <vaporPressure>Pa</vaporPressure>
- <velocity>m/s</velocity>
- <viscosity>Pa.s</viscosity>
- <viscosityOfLiquid>Pa.s</viscosityOfLiquid>
- <viscosityOfVapor>Pa.s</viscosityOfVapor>
- <volume>m3</volume>
- <volumetricFlow>m3/s</volumetricFlow>
- <diffusivity>m2/s</diffusivity>
- <conductance>[kg/s]/[Pa^0.5]</conductance>
- <mole>mol</mole>
- </SelectedUnitSystem1>
- <SimultaneousAdjustSolverEnabled>true</SimultaneousAdjustSolverEnabled>
- <SpreadsheetUseRegionalSeparator>false</SpreadsheetUseRegionalSeparator>
- <EnergyBalanceCheck>ShowWarning</EnergyBalanceCheck>
- <MassBalanceCheck>ShowWarning</MassBalanceCheck>
- <EnergyBalanceRelativeTolerance>0.01</EnergyBalanceRelativeTolerance>
- <MassBalanceRelativeTolerance>0.01</MassBalanceRelativeTolerance>
- <DisplayCornerPropertyList>false</DisplayCornerPropertyList>
- <DisplayCornerPropertyListPosition>RightBottom</DisplayCornerPropertyListPosition>
- <DisplayFloatingPropertyTables>true</DisplayFloatingPropertyTables>
- <DisplayCornerPropertyListFontColor>DimGray</DisplayCornerPropertyListFontColor>
- <DisplayCornerPropertyListFontName>Consolas</DisplayCornerPropertyListFontName>
- <DisplayCornerPropertyListFontSize>8</DisplayCornerPropertyListFontSize>
- <DisplayCornerPropertyListPadding>4</DisplayCornerPropertyListPadding>
- <DefaultFloatingTableCompoundAmountBasis>Molar_Fractions</DefaultFloatingTableCompoundAmountBasis>
- <DisplayFloatingTableCompoundAmounts>true</DisplayFloatingTableCompoundAmounts>
- <SpreadsheetUnitLockingMode>true</SpreadsheetUnitLockingMode>
- <CompoundOrderingMode>AsAdded</CompoundOrderingMode>
- <FlowsheetControlPanelMode>false</FlowsheetControlPanelMode>
- <SkipEquilibriumCalculationOnDefinedStreams>true</SkipEquilibriumCalculationOnDefinedStreams>
- <ForceStreamPhase>None</ForceStreamPhase>
- <DisplayUserDefinedPropertiesEditor>false</DisplayUserDefinedPropertiesEditor>
- <LabelFontSize>10</LabelFontSize>
- <FlowsheetColorTheme>2</FlowsheetColorTheme>
- <RegularFontName>OpenSans_SemiCondensed-Regular</RegularFontName>
- <BoldFontName>OpenSans_SemiCondensed-SemiBold</BoldFontName>
- <ItalicFontName>OpenSans_SemiCondensed-Italic</ItalicFontName>
- <BoldItalicFontName>OpenSans_SemiCondensed-MediumItalic</BoldItalicFontName>
- <DisplayEnergyStreamPowerValue>true</DisplayEnergyStreamPowerValue>
- <DisplayMaterialStreamMassFlowValue>false</DisplayMaterialStreamMassFlowValue>
- <DisplayMaterialStreamMolarFlowValue>false</DisplayMaterialStreamMolarFlowValue>
- <DisplayMaterialStreamVolFlowValue>false</DisplayMaterialStreamVolFlowValue>
- <DisplayMaterialStreamTemperatureValue>false</DisplayMaterialStreamTemperatureValue>
- <DisplayMaterialStreamPressureValue>false</DisplayMaterialStreamPressureValue>
- <DisplayMaterialStreamEnergyFlowValue>false</DisplayMaterialStreamEnergyFlowValue>
- <AddObjectsWithStreams>2</AddObjectsWithStreams>
- <DisplayDynamicPropertyValues>true</DisplayDynamicPropertyValues>
- <CurrentWeather>
- <Type>DWSIM.SharedClasses.WeatherData</Type>
- <CurrentCondition>Sunny</CurrentCondition>
- <WindSpeed_km_h>5</WindSpeed_km_h>
- <RelativeHumidity_pct>30</RelativeHumidity_pct>
- <Temperature_C>30</Temperature_C>
- <SolarIrradiation_kWh_m2>1</SolarIrradiation_kWh_m2>
- <Latitude>0</Latitude>
- <Longitude>0</Longitude>
- <AtmosphericPressure_Pa>101325</AtmosphericPressure_Pa>
- </CurrentWeather>
- <CustomCalculationOrder />
- <SpecCalculationMode>AfterSourceObject</SpecCalculationMode>
- <ForceObjectSolving>true</ForceObjectSolving>
- <SaveFlowsheetMessagesInFile>true</SaveFlowsheetMessagesInFile>
- <RTFAnnotations></RTFAnnotations>
- <EnabledUndoRedo>false</EnabledUndoRedo>
- <VisibleProperties>
- <ObjectType Value="AbsorptionColumn">
- <PropertyID Value="PROP_AC_0" />
- <PropertyID Value="PROP_AC_1" />
- <PropertyID Value="PROP_AC_2" />
- <PropertyID Value="Estimated Height" />
- <PropertyID Value="Estimated Diameter" />
- <PropertyID Value="Number of Stages" />
- </ObjectType>
- <ObjectType Value="Adjust">
- <PropertyID Value="MinVal" />
- <PropertyID Value="MaxVal" />
- <PropertyID Value="AdjustValue" />
- <PropertyID Value="Tolerance" />
- <PropertyID Value="StepSize" />
- <PropertyID Value="MaximumIterations" />
- </ObjectType>
- <ObjectType Value="AnalogGauge">
- <PropertyID Value="Monitored Value" />
- </ObjectType>
- <ObjectType Value="CapeOpenUO" />
- <ObjectType Value="ComponentSeparator">
- <PropertyID Value="PROP_CP_0" />
- <PropertyID Value="SpecifiedStreamIndex" />
- </ObjectType>
- <ObjectType Value="Compressor">
- <PropertyID Value="PROP_CO_0" />
- <PropertyID Value="PROP_CO_1" />
- <PropertyID Value="PROP_CO_2" />
- <PropertyID Value="PROP_CO_3" />
- <PropertyID Value="PROP_CO_4" />
- <PropertyID Value="PolytropicEfficiency" />
- <PropertyID Value="AdiabaticCoefficient" />
- <PropertyID Value="PolytropicCoefficient" />
- <PropertyID Value="AdiabaticHead" />
- <PropertyID Value="PolytropicHead" />
- <PropertyID Value="RotationSpeed" />
- <PropertyID Value="PressureRatio" />
- </ObjectType>
- <ObjectType Value="Cooler">
- <PropertyID Value="Flow Conductance" />
- <PropertyID Value="Volume" />
- <PropertyID Value="Minimum Pressure" />
- <PropertyID Value="Initialize using Inlet Stream" />
- <PropertyID Value="Reset Content" />
- <PropertyID Value="PROP_CL_0" />
- <PropertyID Value="PROP_CL_1" />
- <PropertyID Value="PROP_CL_2" />
- <PropertyID Value="PROP_CL_3" />
- <PropertyID Value="PROP_CL_4" />
- <PropertyID Value="PROP_CL_5" />
- </ObjectType>
- <ObjectType Value="CustomUO" />
- <ObjectType Value="DigitalGauge">
- <PropertyID Value="Monitored Value" />
- </ObjectType>
- <ObjectType Value="DistillationColumn">
- <PropertyID Value="PROP_DC_2" />
- <PropertyID Value="PROP_DC_5" />
- <PropertyID Value="PROP_DC_6" />
- <PropertyID Value="PROP_DC_7" />
- <PropertyID Value="PROP_DC_8" />
- <PropertyID Value="Condenser_Specification_Value" />
- <PropertyID Value="Reboiler_Specification_Value" />
- <PropertyID Value="Global_Stage_Efficiency" />
- <PropertyID Value="Condenser_Calculated_Value" />
- <PropertyID Value="Reboiler_Calculated_Value" />
- <PropertyID Value="Estimated Height" />
- <PropertyID Value="Estimated Diameter" />
- </ObjectType>
- <ObjectType Value="DummyUnitOperation" />
- <ObjectType Value="EnergyRecycle">
- <PropertyID Value="PROP_ER_0" />
- <PropertyID Value="PROP_ER_1" />
- <PropertyID Value="PROP_ER_2" />
- </ObjectType>
- <ObjectType Value="EnergyStream">
- <PropertyID Value="PROP_ES_0" />
- </ObjectType>
- <ObjectType Value="ExcelUO">
- <PropertyID Value="Calc_dQ" />
- </ObjectType>
- <ObjectType Value="Expander">
- <PropertyID Value="PROP_TU_0" />
- <PropertyID Value="PROP_TU_1" />
- <PropertyID Value="PROP_TU_2" />
- <PropertyID Value="PROP_TU_3" />
- <PropertyID Value="PROP_TU_4" />
- <PropertyID Value="PolytropicEfficiency" />
- <PropertyID Value="AdiabaticCoefficient" />
- <PropertyID Value="PolytropicCoefficient" />
- <PropertyID Value="AdiabaticHead" />
- <PropertyID Value="PolytropicHead" />
- <PropertyID Value="RotationSpeed" />
- <PropertyID Value="PressureRatio" />
- </ObjectType>
- <ObjectType Value="Filter">
- <PropertyID Value="PROP_FT_0" />
- <PropertyID Value="PROP_FT_1" />
- <PropertyID Value="PROP_FT_2" />
- <PropertyID Value="PROP_FT_3" />
- <PropertyID Value="PROP_FT_4" />
- <PropertyID Value="PROP_FT_5" />
- <PropertyID Value="PROP_FT_6" />
- <PropertyID Value="PROP_FT_7" />
- </ObjectType>
- <ObjectType Value="Flowsheet" />
- <ObjectType Value="Heater">
- <PropertyID Value="Flow Conductance" />
- <PropertyID Value="Volume" />
- <PropertyID Value="Minimum Pressure" />
- <PropertyID Value="Initialize using Inlet Stream" />
- <PropertyID Value="Reset Content" />
- <PropertyID Value="PROP_HT_0" />
- <PropertyID Value="PROP_HT_1" />
- <PropertyID Value="PROP_HT_2" />
- <PropertyID Value="PROP_HT_3" />
- <PropertyID Value="PROP_HT_4" />
- <PropertyID Value="PROP_HT_5" />
- </ObjectType>
- <ObjectType Value="HeatExchanger">
- <PropertyID Value="PROP_HX_0" />
- <PropertyID Value="PROP_HX_1" />
- <PropertyID Value="PROP_HX_2" />
- <PropertyID Value="PROP_HX_3" />
- <PropertyID Value="PROP_HX_4" />
- <PropertyID Value="PROP_HX_25" />
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- <PropertyID Value="PROP_HX_28" />
- <PropertyID Value="PROP_HX_32" />
- <PropertyID Value="PROP_HX_33" />
- </ObjectType>
- <ObjectType Value="Input" />
- <ObjectType Value="LevelGauge">
- <PropertyID Value="Monitored Value" />
- </ObjectType>
- <ObjectType Value="MaterialStream">
- <PropertyID Value="PROP_MS_0" />
- <PropertyID Value="PROP_MS_1" />
- <PropertyID Value="PROP_MS_2" />
- <PropertyID Value="PROP_MS_3" />
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- <PropertyID Value="PROP_MS_154" />
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- <ObjectType Value="Mixer" />
- <ObjectType Value="OrificePlate">
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- <PropertyID Value="PROP_OP_1" />
- <PropertyID Value="PROP_OP_2" />
- <PropertyID Value="PROP_OP_3" />
- <PropertyID Value="PROP_OP_4" />
- <PropertyID Value="PROP_OP_5" />
- <PropertyID Value="PROP_OP_6" />
- <PropertyID Value="PROP_OP_7" />
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- <ObjectType Value="PIDController">
- <PropertyID Value="Active" />
- <PropertyID Value="ManualOverride" />
- <PropertyID Value="LastError" />
- <PropertyID Value="CurrentError" />
- <PropertyID Value="CumulativeError" />
- <PropertyID Value="SetPointAbs" />
- <PropertyID Value="Kp" />
- <PropertyID Value="Ki" />
- <PropertyID Value="Kd" />
- <PropertyID Value="Output" />
- <PropertyID Value="OutputMin" />
- <PropertyID Value="OutputMax" />
- <PropertyID Value="OutputAbs" />
- </ObjectType>
- <ObjectType Value="Pipe">
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- <PropertyID Value="PressureDropStatic" />
- <PropertyID Value="PressureDropFriction" />
- <PropertyID Value="PROP_PS_1" />
- <PropertyID Value="PROP_PS_2" />
- <PropertyID Value="PROP_PS_8" />
- <PropertyID Value="PROP_PS_9" />
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- <ObjectType Value="Pump">
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- <PropertyID Value="PROP_PU_1" />
- <PropertyID Value="PROP_PU_2" />
- <PropertyID Value="PROP_PU_3" />
- <PropertyID Value="PROP_PU_4" />
- <PropertyID Value="PROP_PU_5" />
- <PropertyID Value="PROP_PU_6" />
- </ObjectType>
- <ObjectType Value="PythonController">
- <PropertyID Value="Active" />
- <PropertyID Value="SetPoint" />
- <PropertyID Value="Output" />
- </ObjectType>
- <ObjectType Value="Reactor_Conversion">
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- <PropertyID Value="Liquid Level" />
- <PropertyID Value="Volume" />
- <PropertyID Value="Height" />
- <PropertyID Value="Minimum Pressure" />
- <PropertyID Value="Initialize using Inlet Stream" />
- <PropertyID Value="Reset Contents" />
- <PropertyID Value="PROP_CR_0" />
- <PropertyID Value="Calculation Mode" />
- </ObjectType>
- <ObjectType Value="Reactor_CSTR">
- <PropertyID Value="Operating Pressure" />
- <PropertyID Value="Liquid Level" />
- <PropertyID Value="Height" />
- <PropertyID Value="Minimum Pressure" />
- <PropertyID Value="Initialize using Inlet Stream" />
- <PropertyID Value="Reset Contents" />
- <PropertyID Value="PROP_CS_0" />
- <PropertyID Value="PROP_CS_1" />
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- <PropertyID Value="Calculation Mode" />
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- <ObjectType Value="Reactor_Equilibrium">
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- <PropertyID Value="Liquid Level" />
- <PropertyID Value="Volume" />
- <PropertyID Value="Height" />
- <PropertyID Value="Minimum Pressure" />
- <PropertyID Value="Initialize using Inlet Stream" />
- <PropertyID Value="Reset Contents" />
- <PropertyID Value="PROP_EQ_0" />
- <PropertyID Value="PROP_EQ_1" />
- <PropertyID Value="Calculation Mode" />
- <PropertyID Value="Initial Gibbs Energy" />
- <PropertyID Value="Final Gibbs Energy" />
- </ObjectType>
- <ObjectType Value="Reactor_Gibbs">
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- <PropertyID Value="Liquid Level" />
- <PropertyID Value="Volume" />
- <PropertyID Value="Height" />
- <PropertyID Value="Minimum Pressure" />
- <PropertyID Value="Initialize using Inlet Stream" />
- <PropertyID Value="Reset Contents" />
- <PropertyID Value="PROP_GR_0" />
- <PropertyID Value="PROP_GR_1" />
- <PropertyID Value="Calculation Mode" />
- <PropertyID Value="Initial Gibbs Energy" />
- <PropertyID Value="Final Gibbs Energy" />
- <PropertyID Value="Element Balance Residue" />
- </ObjectType>
- <ObjectType Value="Reactor_PFR">
- <PropertyID Value="Max Sections" />
- <PropertyID Value="Reset Contents" />
- <PropertyID Value="PROP_PF_0" />
- <PropertyID Value="PROP_PF_1" />
- <PropertyID Value="PROP_PF_2" />
- <PropertyID Value="PROP_PF_3" />
- <PropertyID Value="PROP_PF_4" />
- <PropertyID Value="PROP_PF_5" />
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- <PropertyID Value="PROP_PF_8" />
- <PropertyID Value="PROP_PF_9" />
- <PropertyID Value="PROP_PF_10" />
- <PropertyID Value="Calculation Mode" />
- </ObjectType>
- <ObjectType Value="Recycle">
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- <PropertyID Value="PROP_RY_1" />
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- <PropertyID Value="PROP_RY_3" />
- <PropertyID Value="PROP_RY_4" />
- <PropertyID Value="PROP_RY_5" />
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- <ObjectType Value="ShortcutColumn">
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- <PropertyID Value="PROP_SC_14" />
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- <ObjectType Value="SolidsSeparator">
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- <PropertyID Value="PROP_SS_2" />
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- <ObjectType Value="Spec">
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- <PropertyID Value="SpecMax" />
- <PropertyID Value="Expression" />
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- <ObjectType Value="Splitter">
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- <PropertyID Value="PROP_SP_2" />
- </ObjectType>
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- <ObjectType>MaterialStream</ObjectType>
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- <Name>MAT-b77eb592-349c-4607-91c3-1395dae64026</Name>
- <Tag>S-06</Tag>
- <Width>20</Width>
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- <EnergyConnector>
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- <SpecialConnectors />
- </GraphicObject>
- <GraphicObject>
- <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
- <SemiTransparent>false</SemiTransparent>
- <LineWidth>1</LineWidth>
- <GradientMode>true</GradientMode>
- <LineColor>#ff4682b4</LineColor>
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- <Description>Material Stream</Description>
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- <ObjectType>MaterialStream</ObjectType>
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- <Height>20</Height>
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- <Tag>S-04</Tag>
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- <InputConnectors>
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- <PropertyPackages>
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- <Type>DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage</Type>
- <ComponentName>NRTL</ComponentName>
- <ComponentDescription>Uses NRTL (Non-Random Two-Liquid) model to calculate liquid-phase activity coefficients.</ComponentDescription>
- <Tag>NRTL (1)</Tag>
- <UseHenryConstants>true</UseHenryConstants>
- <AutoEstimateMissingNRTLUNIQUACParameters>true</AutoEstimateMissingNRTLUNIQUACParameters>
- <SingleCompoundCheckThreshold>0.99999</SingleCompoundCheckThreshold>
- <OverrideKvalFugCoeff>false</OverrideKvalFugCoeff>
- <OverrideEnthalpyCalculation>false</OverrideEnthalpyCalculation>
- <OverrideEntropyCalculation>false</OverrideEntropyCalculation>
- <LiquidDensityCalculationMode_Subcritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Subcritical>
- <LiquidDensityCalculationMode_Supercritical>Rackett_and_ExpData</LiquidDensityCalculationMode_Supercritical>
- <LiquidDensity_CorrectExpDataForPressure>true</LiquidDensity_CorrectExpDataForPressure>
- <LiquidDensity_UsePenelouxVolumeTranslation>true</LiquidDensity_UsePenelouxVolumeTranslation>
- <LiquidViscosityCalculationMode_Subcritical>ExpData</LiquidViscosityCalculationMode_Subcritical>
- <LiquidViscosityCalculationMode_Supercritical>Letsou_Stiel</LiquidViscosityCalculationMode_Supercritical>
- <LiquidViscosity_CorrectExpDataForPressure>true</LiquidViscosity_CorrectExpDataForPressure>
- <LiquidViscosity_MixingRule>MoleAverage</LiquidViscosity_MixingRule>
- <VaporPhaseFugacityCalculationMode>Ideal</VaporPhaseFugacityCalculationMode>
- <SolidPhaseFugacityCalculationMethod>FromLiquidFugacity</SolidPhaseFugacityCalculationMethod>
- <SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>false</SolidPhaseFugacity_UseIdealLiquidPhaseFugacity>
- <SolidPhaseEnthalpy_UsesCp>false</SolidPhaseEnthalpy_UsesCp>
- <EnthalpyEntropyCpCvCalculationMode>LiqCp_Excess</EnthalpyEntropyCpCvCalculationMode>
- <LiquidEnthalpyEntropyCpCvCalculationMode_EOS>EOS</LiquidEnthalpyEntropyCpCvCalculationMode_EOS>
- <LiquidFugacity_UsePoyntingCorrectionFactor>true</LiquidFugacity_UsePoyntingCorrectionFactor>
- <ActivityCoefficientModels_IgnoreMissingInteractionParameters>false</ActivityCoefficientModels_IgnoreMissingInteractionParameters>
- <IgnoreVaporFractionLimit>false</IgnoreVaporFractionLimit>
- <IgnoreSalinityLimit>false</IgnoreSalinityLimit>
- <CalculateAdditionalMaterialStreamProperties>true</CalculateAdditionalMaterialStreamProperties>
- <FlashCalculationApproach>NestedLoops</FlashCalculationApproach>
- <ForcedSolids>[]</ForcedSolids>
- <PropertyOverrides>{}</PropertyOverrides>
- <InteractionParameters_PR>
- <InteractionParameter Compound1="Nitrogen" Compound2="Carbon dioxide" Value="-0.0222" />
- <InteractionParameter Compound1="Nitrogen" Compound2="Sulfur dioxide" Value="0.08" />
- <InteractionParameter Compound1="Carbon dioxide" Compound2="Water" Value="-0.12155" />
- </InteractionParameters_PR>
- <InteractionParameters_NRTL>
- <InteractionParameter Compound1="Water" Compound2="Carbon dioxide" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Water" Compound2="Sulfur dioxide" ID1="" ID2="" A12="1E-10" A21="1E-10" B12="0" B21="0" C12="0" C21="0" alpha12="1E-10" />
- <InteractionParameter Compound1="Water" Compound2="Monoethanolamine" ID1="" ID2="" A12="-563.53058277974" A21="198.386951848461" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Water" Compound2="Nitrogen" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Carbon dioxide" Compound2="Sulfur dioxide" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Carbon dioxide" Compound2="Monoethanolamine" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Carbon dioxide" Compound2="Nitrogen" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Sulfur dioxide" Compound2="Monoethanolamine" ID1="" ID2="" A12="1E-10" A21="1E-10" B12="0" B21="0" C12="0" C21="0" alpha12="1E-10" />
- <InteractionParameter Compound1="Sulfur dioxide" Compound2="Nitrogen" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- <InteractionParameter Compound1="Monoethanolamine" Compound2="Nitrogen" ID1="" ID2="" A12="0.01" A21="0.01" B12="0" B21="0" C12="0" C21="0" alpha12="0.2" />
- </InteractionParameters_NRTL>
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- <Setting Name="ValidateEquilibriumCalc" Value="False" />
- <Setting Name="UsePhaseIdentificationAlgorithm" Value="False" />
- <Setting Name="CalculateBubbleAndDewPoints" Value="False" />
- <Setting Name="ValidationGibbsTolerance" Value="0.01" />
- <Setting Name="PHFlash_Maximum_Number_Of_External_Iterations" Value="100" />
- <Setting Name="PHFlash_External_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PHFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
- <Setting Name="PHFlash_Internal_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PTFlash_Maximum_Number_Of_External_Iterations" Value="100" />
- <Setting Name="PTFlash_External_Loop_Tolerance" Value="0.0001" />
- <Setting Name="PTFlash_Maximum_Number_Of_Internal_Iterations" Value="100" />
- <Setting Name="PTFlash_Internal_Loop_Tolerance" Value="0.0001" />
- <Setting Name="NL_FastMode" Value="True" />
- <Setting Name="IO_FastMode" Value="True" />
- <Setting Name="GM_OptimizationMethod" Value="IPOPT" />
- <Setting Name="ThreePhaseFlashStabTestSeverity" Value="0" />
- <Setting Name="ThreePhaseFlashStabTestCompIds" Value="" />
- <Setting Name="PVFlash_FixedDampingFactor" Value="1.0" />
- <Setting Name="PVFlash_MaximumTemperatureChange" Value="10.0" />
- <Setting Name="PVFlash_TemperatureDerivativeEpsilon" Value="0.1" />
- <Setting Name="ST_Number_of_Random_Tries" Value="20" />
- <Setting Name="CheckIncipientLiquidForStability" Value="False" />
- <Setting Name="PHFlash_MaximumTemperatureChange" Value="30.0" />
- <Setting Name="PTFlash_DampingFactor" Value="1.0" />
- <Setting Name="ForceEquilibriumCalculationType" Value="Default" />
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- <Setting Name="HandleSolidsInDefaultEqCalcMode" Value="False" />
- <Setting Name="UseIOFlash" Value="False" />
- <Setting Name="GibbsMinimizationExternalSolver" Value="" />
- <Setting Name="GibbsMinimizationExternalSolverConfigData" Value="" />
- <Setting Name="PHFlash_Use_Interpolated_Result_In_Oscillating_Temperature_Cases" Value="False" />
- <Setting Name="PVFlash_TryIdealCalcOnFailure" Value="True" />
- <Setting Name="FailSafeCalculationMode" Value="1" />
- </FlashSettings>
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- </PropertyPackages>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
- <Acentric_Factor>0.344</Acentric_Factor>
- <BO_BSW>0</BO_BSW>
- <BO_GOR>0</BO_GOR>
- <BO_OilVisc1>0</BO_OilVisc1>
- <BO_OilVisc2>0</BO_OilVisc2>
- <BO_OilViscTemp1>0</BO_OilViscTemp1>
- <BO_OilViscTemp2>0</BO_OilViscTemp2>
- <BO_PNA_A>0</BO_PNA_A>
- <BO_PNA_N>0</BO_PNA_N>
- <BO_PNA_P>0</BO_PNA_P>
- <BO_SGG>0</BO_SGG>
- <BO_SGO>0</BO_SGO>
- <CAS_Number>7732-18-5</CAS_Number>
- <Chao_Seader_Acentricity>0.328</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>18.0674</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0.0114198721442</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
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- <Critical_Compressibility>0.229</Critical_Compressibility>
- <Critical_Pressure>22064000</Critical_Pressure>
- <Critical_Temperature>647.14</Critical_Temperature>
- <Critical_Volume>0.05595</Critical_Volume>
- <CurrentDB>ChemSep</CurrentDB>
- <Dipole_Moment>6.17E-30</Dipole_Moment>
- <Electrolyte_Cp0>0</Electrolyte_Cp0>
- <Electrolyte_DelGF>0</Electrolyte_DelGF>
- <Electrolyte_DelHF>0</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>6.00174</EnthalpyOfFusionAtTf>
- <Formula>HOH</Formula>
- <HVap_A>59640000</HVap_A>
- <HVap_B>0.86515</HVap_B>
- <HVap_C>-1.1134</HVap_C>
- <HVap_D>0.67764</HVap_D>
- <HVap_E>-0.026925</HVap_E>
- <HVap_TMAX>647.28</HVap_TMAX>
- <HVap_TMIN>273.15</HVap_TMIN>
- <HydrationNumber>0</HydrationNumber>
- <ID>1921</ID>
- <Ideal_Gas_Heat_Capacity_Const_A>33200</Ideal_Gas_Heat_Capacity_Const_A>
- <Ideal_Gas_Heat_Capacity_Const_B>-878.9001</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>8.436956</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>0.00207627</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>-6.467085E-07</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>16</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-13422.7167160322</IG_Enthalpy_of_Formation_25C>
- <IG_Entropy_of_Formation_25C>-2.4619941145636</IG_Entropy_of_Formation_25C>
- <IG_Gibbs_Energy_of_Formation_25C>-12688.673170775</IG_Gibbs_Energy_of_Formation_25C>
- <InChI></InChI>
- <Ion_CpAq_a>0</Ion_CpAq_a>
- <Ion_CpAq_b>0</Ion_CpAq_b>
- <Ion_CpAq_c>0</Ion_CpAq_c>
- <IsBlackOil>false</IsBlackOil>
- <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
- <IsFPROPSSupported>false</IsFPROPSSupported>
- <IsHydratedSalt>false</IsHydratedSalt>
- <IsHYPO>0</IsHYPO>
- <IsIon>false</IsIon>
- <IsModified>false</IsModified>
- <IsPF>0</IsPF>
- <IsSalt>false</IsSalt>
- <Liquid_Density_Const_A>32.51621</Liquid_Density_Const_A>
- <Liquid_Density_Const_B>-3.213004</Liquid_Density_Const_B>
- <Liquid_Density_Const_C>7.92411</Liquid_Density_Const_C>
- <Liquid_Density_Const_D>-7.359898</Liquid_Density_Const_D>
- <Liquid_Density_Const_E>2.703522</Liquid_Density_Const_E>
- <Liquid_Density_Tmax>647.29</Liquid_Density_Tmax>
- <Liquid_Density_Tmin>253.1</Liquid_Density_Tmin>
- <Liquid_Heat_Capacity_Const_A>75539</Liquid_Heat_Capacity_Const_A>
- <Liquid_Heat_Capacity_Const_B>-22297</Liquid_Heat_Capacity_Const_B>
- <Liquid_Heat_Capacity_Const_C>136.02</Liquid_Heat_Capacity_Const_C>
- <Liquid_Heat_Capacity_Const_D>-0.25622</Liquid_Heat_Capacity_Const_D>
- <Liquid_Heat_Capacity_Const_E>0.00018273</Liquid_Heat_Capacity_Const_E>
- <Liquid_Heat_Capacity_Tmax>533.15</Liquid_Heat_Capacity_Tmax>
- <Liquid_Heat_Capacity_Tmin>273.1</Liquid_Heat_Capacity_Tmin>
- <Liquid_Thermal_Conductivity_Const_A>-1.5697</Liquid_Thermal_Conductivity_Const_A>
- <Liquid_Thermal_Conductivity_Const_B>-55.141</Liquid_Thermal_Conductivity_Const_B>
- <Liquid_Thermal_Conductivity_Const_C>0.7832</Liquid_Thermal_Conductivity_Const_C>
- <Liquid_Thermal_Conductivity_Const_D>0.0011484</Liquid_Thermal_Conductivity_Const_D>
- <Liquid_Thermal_Conductivity_Const_E>-1.8151E-06</Liquid_Thermal_Conductivity_Const_E>
- <Liquid_Thermal_Conductivity_Tmax>633.15</Liquid_Thermal_Conductivity_Tmax>
- <Liquid_Thermal_Conductivity_Tmin>273.1</Liquid_Thermal_Conductivity_Tmin>
- <Liquid_Viscosity_Const_A>-133.7</Liquid_Viscosity_Const_A>
- <Liquid_Viscosity_Const_B>6785.7</Liquid_Viscosity_Const_B>
- <Liquid_Viscosity_Const_C>18.47</Liquid_Viscosity_Const_C>
- <Liquid_Viscosity_Const_D>-1.4736E-05</Liquid_Viscosity_Const_D>
- <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
- <LiquidDensityEquation>106</LiquidDensityEquation>
- <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
- <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
- <LiquidViscosityEquation>101</LiquidViscosityEquation>
- <Molar_Weight>18.01528</Molar_Weight>
- <MolarVolume_k1i>0</MolarVolume_k1i>
- <MolarVolume_k2i>0</MolarVolume_k2i>
- <MolarVolume_k3i>0</MolarVolume_k3i>
- <MolarVolume_v2i>0</MolarVolume_v2i>
- <MolarVolume_v3i>0</MolarVolume_v3i>
- <Name>Water</Name>
- <NBP>373.15</NBP>
- <NegativeIon></NegativeIon>
- <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
- <Normal_Boiling_Point>373.15</Normal_Boiling_Point>
- <OriginalDB>ChemSep</OriginalDB>
- <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
- <PC_SAFT_m>0</PC_SAFT_m>
- <PC_SAFT_sigma>0</PC_SAFT_sigma>
- <PositiveIon></PositiveIon>
- <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
- <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
- <SMILES>O</SMILES>
- <Solid_Density_Const_A>52.967</Solid_Density_Const_A>
- <Solid_Density_Const_B>-0.0075822</Solid_Density_Const_B>
- <Solid_Density_Const_C>0</Solid_Density_Const_C>
- <Solid_Density_Const_D>0</Solid_Density_Const_D>
- <Solid_Density_Const_E>0</Solid_Density_Const_E>
- <Solid_Density_Tmax>273.15</Solid_Density_Tmax>
- <Solid_Density_Tmin>233.15</Solid_Density_Tmin>
- <Solid_Heat_Capacity_Const_A>-262.51</Solid_Heat_Capacity_Const_A>
- <Solid_Heat_Capacity_Const_B>140.52</Solid_Heat_Capacity_Const_B>
- <Solid_Heat_Capacity_Const_C>-3.8869E-06</Solid_Heat_Capacity_Const_C>
- <Solid_Heat_Capacity_Const_D>-1.1996E-08</Solid_Heat_Capacity_Const_D>
- <Solid_Heat_Capacity_Const_E>7.1879E-11</Solid_Heat_Capacity_Const_E>
- <Solid_Heat_Capacity_Tmax>273.15</Solid_Heat_Capacity_Tmax>
- <Solid_Heat_Capacity_Tmin>3.15</Solid_Heat_Capacity_Tmin>
- <SolidDensityAtTs>0</SolidDensityAtTs>
- <SolidDensityEquation>2</SolidDensityEquation>
- <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
- <SolidTs>0</SolidTs>
- <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
- <StandardStateMolarVolume>0</StandardStateMolarVolume>
- <StoichSum>0</StoichSum>
- <Surface_Tension_Const_A>-0.031819</Surface_Tension_Const_A>
- <Surface_Tension_Const_B>167.09</Surface_Tension_Const_B>
- <Surface_Tension_Const_C>-3.6781</Surface_Tension_Const_C>
- <Surface_Tension_Const_D>0.0053717</Surface_Tension_Const_D>
- <Surface_Tension_Const_E>-8.4188E-06</Surface_Tension_Const_E>
- <Surface_Tension_Tmax>647.1</Surface_Tension_Tmax>
- <Surface_Tension_Tmin>265.1</Surface_Tension_Tmin>
- <SurfaceTensionEquation>16</SurfaceTensionEquation>
- <TemperatureOfFusion>273.15</TemperatureOfFusion>
- <UNIQUAC_Q>1.4</UNIQUAC_Q>
- <UNIQUAC_R>0.92</UNIQUAC_R>
- <Vapor_Pressure_Constant_A>74.55502</Vapor_Pressure_Constant_A>
- <Vapor_Pressure_Constant_B>-7295.586</Vapor_Pressure_Constant_B>
- <Vapor_Pressure_Constant_C>-7.442448</Vapor_Pressure_Constant_C>
- <Vapor_Pressure_Constant_D>4.2881E-06</Vapor_Pressure_Constant_D>
- <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
- <Vapor_Pressure_TMAX>647.29</Vapor_Pressure_TMAX>
- <Vapor_Pressure_TMIN>263.15</Vapor_Pressure_TMIN>
- <Vapor_Thermal_Conductivity_Const_A>6.5986E-06</Vapor_Thermal_Conductivity_Const_A>
- <Vapor_Thermal_Conductivity_Const_B>1.3947</Vapor_Thermal_Conductivity_Const_B>
- <Vapor_Thermal_Conductivity_Const_C>59.478</Vapor_Thermal_Conductivity_Const_C>
- <Vapor_Thermal_Conductivity_Const_D>-15484</Vapor_Thermal_Conductivity_Const_D>
- <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
- <Vapor_Thermal_Conductivity_Tmax>1073.15</Vapor_Thermal_Conductivity_Tmax>
- <Vapor_Thermal_Conductivity_Tmin>273.16</Vapor_Thermal_Conductivity_Tmin>
- <Vapor_Viscosity_Const_A>7.002327E-08</Vapor_Viscosity_Const_A>
- <Vapor_Viscosity_Const_B>0.934576</Vapor_Viscosity_Const_B>
- <Vapor_Viscosity_Const_C>195.6338</Vapor_Viscosity_Const_C>
- <Vapor_Viscosity_Const_D>-13045.99</Vapor_Viscosity_Const_D>
- <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
- <Vapor_Viscosity_Tmax>1073.15</Vapor_Viscosity_Tmax>
- <Vapor_Viscosity_Tmin>273.16</Vapor_Viscosity_Tmin>
- <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
- <VaporPressureEquation>101</VaporPressureEquation>
- <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
- <VaporViscosityEquation>102</VaporViscosityEquation>
- <Z_Rackett>0.2338</Z_Rackett>
- <FullerDiffusionVolume>13.11</FullerDiffusionVolume>
- <LennardJonesDiameter>2.52E-10</LennardJonesDiameter>
- <LennardJonesEnergy>775</LennardJonesEnergy>
- <Parachor>0.00926</Parachor>
- <Tag></Tag>
- <COSTALD_SRK_Acentric_Factor>-0.65445</COSTALD_SRK_Acentric_Factor>
- <COSTALD_Characteristic_Volume>0.04357</COSTALD_Characteristic_Volume>
- <IsSolid>false</IsSolid>
- <ChemSepFamily>84</ChemSepFamily>
- <DynamicProperties />
- <UNIFACGroups>
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- </UNIFACGroups>
- <MODFACGroups>
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- </MODFACGroups>
- <NISTMODFACGroups>
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- </NISTMODFACGroups>
- <Elements>
- <Item Name="H" Value="2" />
- <Item Name="O" Value="1" />
- </Elements>
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
- <Acentric_Factor>0.223621</Acentric_Factor>
- <BO_BSW>0</BO_BSW>
- <BO_GOR>0</BO_GOR>
- <BO_OilVisc1>0</BO_OilVisc1>
- <BO_OilVisc2>0</BO_OilVisc2>
- <BO_OilViscTemp1>0</BO_OilViscTemp1>
- <BO_OilViscTemp2>0</BO_OilViscTemp2>
- <BO_PNA_A>0</BO_PNA_A>
- <BO_PNA_N>0</BO_PNA_N>
- <BO_PNA_P>0</BO_PNA_P>
- <BO_SGG>0</BO_SGG>
- <BO_SGO>0</BO_SGO>
- <CAS_Number>124-38-9</CAS_Number>
- <Chao_Seader_Acentricity>0.231</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>37.2744</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0.0034785053748</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
- <CompCreatorStudyFile></CompCreatorStudyFile>
- <Critical_Compressibility>0.274</Critical_Compressibility>
- <Critical_Pressure>7383000</Critical_Pressure>
- <Critical_Temperature>304.21</Critical_Temperature>
- <Critical_Volume>0.094</Critical_Volume>
- <CurrentDB>ChemSep</CurrentDB>
- <Dipole_Moment>0</Dipole_Moment>
- <Electrolyte_Cp0>0</Electrolyte_Cp0>
- <Electrolyte_DelGF>0</Electrolyte_DelGF>
- <Electrolyte_DelHF>0</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>9.019</EnthalpyOfFusionAtTf>
- <Formula>OCO</Formula>
- <HVap_A>21092000</HVap_A>
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- <HVap_C>-0.46134</HVap_C>
- <HVap_D>0.43554</HVap_D>
- <HVap_E>0.037671</HVap_E>
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- <HydrationNumber>0</HydrationNumber>
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- <Ideal_Gas_Heat_Capacity_Const_B>-494.28</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>10.658</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>-2.7375E-05</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>3.3268E-09</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>16</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-8941.47854440518</IG_Enthalpy_of_Formation_25C>
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- <IG_Gibbs_Energy_of_Formation_25C>-8961.01977982027</IG_Gibbs_Energy_of_Formation_25C>
- <InChI></InChI>
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- <Ion_CpAq_c>0</Ion_CpAq_c>
- <IsBlackOil>false</IsBlackOil>
- <IsCOOLPROPSupported>true</IsCOOLPROPSupported>
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- <IsHydratedSalt>false</IsHydratedSalt>
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- <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
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- <Liquid_Heat_Capacity_Const_C>-6.9126</Liquid_Heat_Capacity_Const_C>
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- <Name>Carbon dioxide</Name>
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- <Normal_Boiling_Point>194.686</Normal_Boiling_Point>
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- <Dipole_Moment>5.44E-30</Dipole_Moment>
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- <Name>Sulfur dioxide</Name>
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- <SMILES>O=[S]=O</SMILES>
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- <Solid_Heat_Capacity_Const_C>-16.235</Solid_Heat_Capacity_Const_C>
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- <Solid_Heat_Capacity_Tmax>197.68</Solid_Heat_Capacity_Tmax>
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- <StandardStateMolarVolume>0</StandardStateMolarVolume>
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- <Surface_Tension_Const_A>-0.011604</Surface_Tension_Const_A>
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- <TemperatureOfFusion>200</TemperatureOfFusion>
- <UNIQUAC_Q>1.612</UNIQUAC_Q>
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- <Vapor_Pressure_Constant_A>53.52766</Vapor_Pressure_Constant_A>
- <Vapor_Pressure_Constant_B>-4260.124</Vapor_Pressure_Constant_B>
- <Vapor_Pressure_Constant_C>-4.670429</Vapor_Pressure_Constant_C>
- <Vapor_Pressure_Constant_D>3.0272E-06</Vapor_Pressure_Constant_D>
- <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
- <Vapor_Pressure_TMAX>430.75</Vapor_Pressure_TMAX>
- <Vapor_Pressure_TMIN>195.12</Vapor_Pressure_TMIN>
- <Vapor_Thermal_Conductivity_Const_A>23.316</Vapor_Thermal_Conductivity_Const_A>
- <Vapor_Thermal_Conductivity_Const_B>-0.95324</Vapor_Thermal_Conductivity_Const_B>
- <Vapor_Thermal_Conductivity_Const_C>-1567.4</Vapor_Thermal_Conductivity_Const_C>
- <Vapor_Thermal_Conductivity_Const_D>1330100</Vapor_Thermal_Conductivity_Const_D>
- <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
- <Vapor_Thermal_Conductivity_Tmax>900</Vapor_Thermal_Conductivity_Tmax>
- <Vapor_Thermal_Conductivity_Tmin>197.67</Vapor_Thermal_Conductivity_Tmin>
- <Vapor_Viscosity_Const_A>1.2144E-06</Vapor_Viscosity_Const_A>
- <Vapor_Viscosity_Const_B>0.53923</Vapor_Viscosity_Const_B>
- <Vapor_Viscosity_Const_C>315.41</Vapor_Viscosity_Const_C>
- <Vapor_Viscosity_Const_D>-2659.7</Vapor_Viscosity_Const_D>
- <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
- <Vapor_Viscosity_Tmax>1250</Vapor_Viscosity_Tmax>
- <Vapor_Viscosity_Tmin>197.67</Vapor_Viscosity_Tmin>
- <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
- <VaporPressureEquation>101</VaporPressureEquation>
- <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
- <VaporViscosityEquation>102</VaporViscosityEquation>
- <Z_Rackett>0</Z_Rackett>
- <FullerDiffusionVolume>41.8</FullerDiffusionVolume>
- <LennardJonesDiameter>4.04E-10</LennardJonesDiameter>
- <LennardJonesEnergy>347</LennardJonesEnergy>
- <Parachor>0.0181</Parachor>
- <Tag></Tag>
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- <COSTALD_Characteristic_Volume>0.12522</COSTALD_Characteristic_Volume>
- <IsSolid>false</IsSolid>
- <ChemSepFamily>24</ChemSepFamily>
- <DynamicProperties />
- <UNIFACGroups />
- <MODFACGroups />
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- <Item Name="S" Value="1" />
- </Elements>
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
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- <BO_GOR>0</BO_GOR>
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- <BO_OilVisc2>0</BO_OilVisc2>
- <BO_OilViscTemp1>0</BO_OilViscTemp1>
- <BO_OilViscTemp2>0</BO_OilViscTemp2>
- <BO_PNA_A>0</BO_PNA_A>
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- <BO_PNA_P>0</BO_PNA_P>
- <BO_SGG>0</BO_SGG>
- <BO_SGO>0</BO_SGO>
- <CAS_Number>141-43-5</CAS_Number>
- <Chao_Seader_Acentricity>0.446737</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>60.3415</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0.00760246818</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
- <CompCreatorStudyFile></CompCreatorStudyFile>
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- <Critical_Pressure>8030000</Critical_Pressure>
- <Critical_Temperature>671.4</Critical_Temperature>
- <Critical_Volume>0.225</Critical_Volume>
- <CurrentDB>ChemSep</CurrentDB>
- <Dipole_Moment>2.59E-30</Dipole_Moment>
- <Electrolyte_Cp0>0</Electrolyte_Cp0>
- <Electrolyte_DelGF>0</Electrolyte_DelGF>
- <Electrolyte_DelHF>0</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>20.496</EnthalpyOfFusionAtTf>
- <Formula>HOCH2CH2NH2</Formula>
- <HVap_A>101203100</HVap_A>
- <HVap_B>1.976961</HVap_B>
- <HVap_C>-4.399887</HVap_C>
- <HVap_D>4.906054</HVap_D>
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- <Ideal_Gas_Heat_Capacity_Const_A>50668</Ideal_Gas_Heat_Capacity_Const_A>
- <Ideal_Gas_Heat_Capacity_Const_B>-516.86</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>12.167</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>8.641E-05</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>2.8656E-10</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>16</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-3208.74454922705</IG_Enthalpy_of_Formation_25C>
- <IG_Entropy_of_Formation_25C>-5.09007279094121</IG_Entropy_of_Formation_25C>
- <IG_Gibbs_Energy_of_Formation_25C>-1691.13934660793</IG_Gibbs_Energy_of_Formation_25C>
- <InChI></InChI>
- <Ion_CpAq_a>0</Ion_CpAq_a>
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- <Ion_CpAq_c>0</Ion_CpAq_c>
- <IsBlackOil>false</IsBlackOil>
- <IsCOOLPROPSupported>false</IsCOOLPROPSupported>
- <IsFPROPSSupported>false</IsFPROPSSupported>
- <IsHydratedSalt>false</IsHydratedSalt>
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- <IsIon>false</IsIon>
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- <Liquid_Heat_Capacity_Const_C>-0.0607137</Liquid_Heat_Capacity_Const_C>
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- <Liquid_Heat_Capacity_Const_E>-1.7988E-05</Liquid_Heat_Capacity_Const_E>
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- <Name>Monoethanolamine</Name>
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- <CAS_Number>7727-37-9</CAS_Number>
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- <Liquid_Viscosity_Const_A>3.4358</Liquid_Viscosity_Const_A>
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- <Molar_Weight>28.0134</Molar_Weight>
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- <Name>Nitrogen</Name>
- <NBP>77.35</NBP>
- <NegativeIon></NegativeIon>
- <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
- <Normal_Boiling_Point>77.35</Normal_Boiling_Point>
- <OriginalDB>ChemSep</OriginalDB>
- <PC_SAFT_epsilon_k>0</PC_SAFT_epsilon_k>
- <PC_SAFT_m>0</PC_SAFT_m>
- <PC_SAFT_sigma>0</PC_SAFT_sigma>
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- <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
- <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
- <SMILES>N#N</SMILES>
- <Solid_Density_Const_A>37.87</Solid_Density_Const_A>
- <Solid_Density_Const_B>-0.06027</Solid_Density_Const_B>
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- <Solid_Density_Const_E>0</Solid_Density_Const_E>
- <Solid_Density_Tmax>63.15</Solid_Density_Tmax>
- <Solid_Density_Tmin>20.65</Solid_Density_Tmin>
- <Solid_Heat_Capacity_Const_A>383890</Solid_Heat_Capacity_Const_A>
- <Solid_Heat_Capacity_Const_B>-28798</Solid_Heat_Capacity_Const_B>
- <Solid_Heat_Capacity_Const_C>875.74</Solid_Heat_Capacity_Const_C>
- <Solid_Heat_Capacity_Const_D>-11.589</Solid_Heat_Capacity_Const_D>
- <Solid_Heat_Capacity_Const_E>0.057106</Solid_Heat_Capacity_Const_E>
- <Solid_Heat_Capacity_Tmax>63</Solid_Heat_Capacity_Tmax>
- <Solid_Heat_Capacity_Tmin>32.8</Solid_Heat_Capacity_Tmin>
- <SolidDensityAtTs>0</SolidDensityAtTs>
- <SolidDensityEquation>2</SolidDensityEquation>
- <SolidHeatCapacityEquation>100</SolidHeatCapacityEquation>
- <SolidTs>0</SolidTs>
- <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
- <StandardStateMolarVolume>0</StandardStateMolarVolume>
- <StoichSum>0</StoichSum>
- <Surface_Tension_Const_A>-0.0025409</Surface_Tension_Const_A>
- <Surface_Tension_Const_B>96.836</Surface_Tension_Const_B>
- <Surface_Tension_Const_C>-7.6473</Surface_Tension_Const_C>
- <Surface_Tension_Const_D>0.05313</Surface_Tension_Const_D>
- <Surface_Tension_Const_E>-0.00036553</Surface_Tension_Const_E>
- <Surface_Tension_Tmax>126.2</Surface_Tension_Tmax>
- <Surface_Tension_Tmin>63.15</Surface_Tension_Tmin>
- <SurfaceTensionEquation>16</SurfaceTensionEquation>
- <TemperatureOfFusion>63.149</TemperatureOfFusion>
- <UNIQUAC_Q>1.088</UNIQUAC_Q>
- <UNIQUAC_R>1.0415</UNIQUAC_R>
- <Vapor_Pressure_Constant_A>42.32946</Vapor_Pressure_Constant_A>
- <Vapor_Pressure_Constant_B>-965.9771</Vapor_Pressure_Constant_B>
- <Vapor_Pressure_Constant_C>-4.321774</Vapor_Pressure_Constant_C>
- <Vapor_Pressure_Constant_D>7.97271E-05</Vapor_Pressure_Constant_D>
- <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
- <Vapor_Pressure_TMAX>126.26</Vapor_Pressure_TMAX>
- <Vapor_Pressure_TMIN>60.81</Vapor_Pressure_TMIN>
- <Vapor_Thermal_Conductivity_Const_A>0.0003395</Vapor_Thermal_Conductivity_Const_A>
- <Vapor_Thermal_Conductivity_Const_B>0.76921</Vapor_Thermal_Conductivity_Const_B>
- <Vapor_Thermal_Conductivity_Const_C>19.592</Vapor_Thermal_Conductivity_Const_C>
- <Vapor_Thermal_Conductivity_Const_D>293.93</Vapor_Thermal_Conductivity_Const_D>
- <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
- <Vapor_Thermal_Conductivity_Tmax>2000</Vapor_Thermal_Conductivity_Tmax>
- <Vapor_Thermal_Conductivity_Tmin>50</Vapor_Thermal_Conductivity_Tmin>
- <Vapor_Viscosity_Const_A>4.6051E-07</Vapor_Viscosity_Const_A>
- <Vapor_Viscosity_Const_B>0.65049</Vapor_Viscosity_Const_B>
- <Vapor_Viscosity_Const_C>5.8019</Vapor_Viscosity_Const_C>
- <Vapor_Viscosity_Const_D>2822.7</Vapor_Viscosity_Const_D>
- <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
- <Vapor_Viscosity_Tmax>1970</Vapor_Viscosity_Tmax>
- <Vapor_Viscosity_Tmin>63.15</Vapor_Viscosity_Tmin>
- <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
- <VaporPressureEquation>101</VaporPressureEquation>
- <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
- <VaporViscosityEquation>102</VaporViscosityEquation>
- <Z_Rackett>0.2906</Z_Rackett>
- <FullerDiffusionVolume>18.5</FullerDiffusionVolume>
- <LennardJonesDiameter>3.710301E-10</LennardJonesDiameter>
- <LennardJonesEnergy>94.45061</LennardJonesEnergy>
- <Parachor>0.0107</Parachor>
- <Tag></Tag>
- <COSTALD_SRK_Acentric_Factor>0.0357998</COSTALD_SRK_Acentric_Factor>
- <COSTALD_Characteristic_Volume>0.0901499</COSTALD_Characteristic_Volume>
- <IsSolid>false</IsSolid>
- <ChemSepFamily>74</ChemSepFamily>
- <DynamicProperties />
- <UNIFACGroups />
- <MODFACGroups />
- <NISTMODFACGroups />
- <Elements>
- <Item Name="N" Value="2" />
- </Elements>
- </Compound>
- </Compounds>
- <ReactionSets>
- <ReactionSet>
- <ID>DefaultSet</ID>
- <Name>Default Set</Name>
- <Description>Default Reaction Set</Description>
- <Reactions />
- </ReactionSet>
- </ReactionSets>
- <Reactions />
- <StoredSolutions />
- <DynamicsManager>
- <Type>DWSIM.DynamicsManager.Manager</Type>
- <Description></Description>
- <CurrentSchedule></CurrentSchedule>
- <ScheduleList />
- <EventSetList />
- <IntegratorList />
- </DynamicsManager>
- <OptimizationCases>
- <OptimizationCase>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.OptimizationCase</Type>
- <name>optcase0</name>
- <description></description>
- <stats></stats>
- <solvm>AL_BRENT</solvm>
- <maxits>100</maxits>
- <tolerance>1E-06</tolerance>
- <epsX>0.001</epsX>
- <epsF>0.001</epsF>
- <epsG>0.001</epsG>
- <epsilon>0.001</epsilon>
- <barriermultiplier>0.0001</barriermultiplier>
- <numdevscheme>2</numdevscheme>
- <boundvariables>false</boundvariables>
- <objfunctype>Variable</objfunctype>
- <type>Minimization</type>
- <expression></expression>
- <Variables />
- </OptimizationCase>
- </OptimizationCases>
- <SensitivityAnalysis>
- <SensitivityAnalysisCase>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SensitivityAnalysisCase</Type>
- <iv1>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
- <objectID></objectID>
- <objectTAG></objectTAG>
- <propID></propID>
- <unit></unit>
- <points>5</points>
- <name></name>
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- <currentvalue>0</currentvalue>
- </iv1>
- <iv2>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
- <objectID></objectID>
- <objectTAG></objectTAG>
- <propID></propID>
- <unit></unit>
- <points>5</points>
- <name></name>
- <id></id>
- <currentvalue>0</currentvalue>
- </iv2>
- <dv>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
- <objectID></objectID>
- <objectTAG></objectTAG>
- <propID></propID>
- <unit></unit>
- <points>5</points>
- <name></name>
- <id></id>
- <currentvalue>0</currentvalue>
- </dv>
- <name>SACase0</name>
- <description></description>
- <stats></stats>
- <numvar>1</numvar>
- <depvartype>Variable</depvartype>
- <expression></expression>
- <IV1>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
- <objectID></objectID>
- <objectTAG></objectTAG>
- <propID></propID>
- <unit></unit>
- <points>5</points>
- <name></name>
- <id></id>
- <currentvalue>0</currentvalue>
- </IV1>
- <IV2>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
- <objectID></objectID>
- <objectTAG></objectTAG>
- <propID></propID>
- <unit></unit>
- <points>5</points>
- <name></name>
- <id></id>
- <currentvalue>0</currentvalue>
- </IV2>
- <DV>
- <Type>DWSIM.SharedClasses.Flowsheet.Optimization.SAVariable</Type>
- <objectID></objectID>
- <objectTAG></objectTAG>
- <propID></propID>
- <unit></unit>
- <points>5</points>
- <name></name>
- <id></id>
- <currentvalue>0</currentvalue>
- </DV>
- <Variables />
- <DepVariables />
- </SensitivityAnalysisCase>
- </SensitivityAnalysis>
- <PetroleumAssays />
- <WatchItems />
- <ScriptItems />
- <ChartItems />
- <Spreadsheet>
- <RGFData>{"MAIN":"{\"?xml\":{\"@version\":\"1.0\"},\"grid\":{\"@xmlns:xsd\":\"http://www.w3.org/2001/XMLSchema\",\"@xmlns:xsi\":\"http://www.w3.org/2001/XMLSchema-instance\",\"head\":{\"meta\":{\"culture\":\"en-IN\",\"editor\":\"ReoGrid Core\",\"core-ver\":\"2.1.0.0\"},\"rows\":\"65536\",\"cols\":\"100\",\"default-row-height\":\"20\",\"default-col-width\":\"70\",\"focus-forward-direction\":\"down\",\"settings\":{\"@meta\":\"30475026398\"},\"script\":null},\"style\":{\"@font\":\"Arial\",\"@font-size\":\"10\",\"@align\":\"general\",\"@valign\":\"middle\"},\"rows\":null,\"cols\":null,\"v-borders\":null,\"h-borders\":null,\"cells\":null}}"}</RGFData>
- </Spreadsheet>
- <PanelLayout>&lt;?xml version="1.0" encoding="utf-8"?&gt;
-&lt;!--DockPanel configuration file. Author: Weifen Luo, all rights reserved.--&gt;
-&lt;!--!!! AUTOMATICALLY GENERATED FILE. DO NOT MODIFY !!!--&gt;
-&lt;DockPanel FormatVersion="1.0" DockLeftPortion="450" DockRightPortion="0.203007518796992" DockTopPortion="0.25" DockBottomPortion="0.0508763545923176" ActiveDocumentPane="0" ActivePane="0"&gt;
- &lt;Contents Count="14"&gt;
- &lt;Content ID="0" PersistString="DWSIM.LogPanel" AutoHidePortion="0.152227705943669" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="1" PersistString="DWSIM.MaterialStreamPanel" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
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- &lt;Content ID="3" PersistString="DWSIM.FormCharts" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="4" PersistString="DWSIM.FormDynamicsManager" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="5" PersistString="DWSIM.FormDynamicsIntegratorControl" AutoHidePortion="0.369804903093313" IsHidden="True" IsFloat="False" /&gt;
- &lt;Content ID="6" PersistString="DWSIM.FormFileExplorer" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="7" PersistString="DWSIM.FlowsheetSurface_SkiaSharp" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="8" PersistString="DWSIM.FormNewSpreadsheet" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="9" PersistString="DWSIM.FormScript" AutoHidePortion="0.25" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="10" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /&gt;
- &lt;Content ID="11" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /&gt;
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- &lt;Content ID="13" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /&gt;
- &lt;/Contents&gt;
- &lt;Panes Count="6"&gt;
- &lt;Pane ID="0" DockState="Document" ActiveContent="7"&gt;
- &lt;Contents Count="7"&gt;
- &lt;Content ID="0" RefID="6" /&gt;
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- &lt;Content ID="0" RefID="10" /&gt;
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- &lt;Content ID="3" RefID="13" /&gt;
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- &lt;DockWindows&gt;
- &lt;DockWindow ID="0" DockState="Document" ZOrderIndex="1"&gt;
- &lt;NestedPanes Count="1"&gt;
- &lt;Pane ID="0" RefID="0" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
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- &lt;/DockWindow&gt;
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- &lt;/DockWindow&gt;
- &lt;DockWindow ID="2" DockState="DockRight" ZOrderIndex="4"&gt;
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-&lt;/DockPanel&gt;</PanelLayout>
- <MessagesLog>
- <Message>[03-02-2024 14:22:02] Estimated NRTL IP set for Water/Monoethanolamine: -563.53/198.39/0.2</Message>
- <Message>[03-02-2024 14:22:02] The flowsheet was calculated successfully. [3.678s]</Message>
- <Message>[03-02-2024 14:22:14] The flowsheet was calculated successfully. [0.05993s]</Message>
- <Message>[03-02-2024 14:22:23] The flowsheet was calculated successfully. [0.02294s]</Message>
- <Message>[03-02-2024 14:22:39] The flowsheet was calculated successfully. [0.03161s]</Message>
- <Message>[03-02-2024 14:23:20] The flowsheet was calculated successfully. [0.02622s]</Message>
- <Message>[03-02-2024 14:23:58] The flowsheet was calculated successfully. [0.01497s]</Message>
- <Message>[03-02-2024 14:24:16] It is recommended that the column propertiy editing be carried out with the calculator disabled.</Message>
- <Message>[03-02-2024 14:24:16] When editing the column connections, remember to click any cell other than the one being edited, so that changes are recognized by DWSIM.</Message>
- <Message>[03-02-2024 14:24:16] Remember to set the pressure of the intermediate stages of the column.</Message>
- <Message>[03-02-2024 14:25:23] The flowsheet was calculated successfully. [0.6281s]</Message>
- <Message>[03-02-2024 14:26:45] It is recommended that the column propertiy editing be carried out with the calculator disabled.</Message>
- <Message>[03-02-2024 14:26:45] When editing the column connections, remember to click any cell other than the one being edited, so that changes are recognized by DWSIM.</Message>
- <Message>[03-02-2024 14:26:45] Remember to set the pressure of the intermediate stages of the column.</Message>
- <Message>[03-02-2024 14:28:48] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:28:48] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381)</Message>
- <Message>[03-02-2024 14:29:01] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:29:01] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381)</Message>
- <Message>[03-02-2024 14:29:28] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:29:28] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381)</Message>
- <Message>[03-02-2024 14:30:19] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:30:19] Error in 'ABS-2': Please set the Column Stage for Feed Stream '8'. (RigorousColumn.vb, 4381)</Message>
- <Message>[03-02-2024 14:31:11] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:31:11] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:31:11] Error in 'ABS-2': Converged to an invalid temperature at stage 6 (Tcalc = -64.2553174521587 K). (SumRates.vb, 720)</Message>
- <Message>[03-02-2024 14:31:34] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:31:34] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:31:34] Error in 'ABS-2': Converged to an invalid temperature at stage 4 (Tcalc = -24.0692138664524 K). (SumRates.vb, 720)</Message>
- <Message>[03-02-2024 14:31:38] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:31:39] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:31:39] Error in 'ABS-2': Converged to an invalid temperature at stage 4 (Tcalc = -24.0692138664524 K). (SumRates.vb, 720)</Message>
- <Message>[03-02-2024 14:32:12] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:32:12] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:32:12] Error in 'ABS-2': Converged to an invalid temperature at stage 7 (Tcalc = -134.736524832954 K). (SumRates.vb, 720)</Message>
- <Message>[03-02-2024 14:32:23] The flowsheet was calculated successfully. [0.9824s]</Message>
- <Message>[03-02-2024 14:34:17] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:34:17] Error in 'PUMP-1': Check the connections of the object. (Pump.vb, 511)</Message>
- <Message>[03-02-2024 14:34:59] The flowsheet was calculated successfully. [1.49s]</Message>
- <Message>[03-02-2024 14:36:11] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:36:11] Error in 'HT-1': Check the connections of the object. (Heater.vb, 360)</Message>
- <Message>[03-02-2024 14:36:58] The flowsheet was calculated successfully. [1.303s]</Message>
- <Message>[03-02-2024 14:43:57] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:43:57] Error in 'ABS-1': Please set the Column Stage for Feed Stream 'S-06'. (RigorousColumn.vb, 4381)</Message>
- <Message>[03-02-2024 14:44:29] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:44:31] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:44:31] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 14:46:34] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:46:36] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:46:36] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 14:47:09] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 14:47:12] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 14:47:12] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 15:09:15] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 15:09:17] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:09:17] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 15:10:21] File C:\Users\pc\AppData\Local\DWSIM\DWSIM12.dwxmz saved successfully.</Message>
- <Message>[03-02-2024 15:11:55] The flowsheet was calculated successfully. [0.3253s]</Message>
- <Message>[03-02-2024 15:12:01] The flowsheet was calculated successfully. [1.27s]</Message>
- <Message>[03-02-2024 15:13:36] The flowsheet was calculated successfully. [1.417s]</Message>
- <Message>[03-02-2024 15:17:38] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 15:17:38] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:17:38] Error in 'ABS-2': Converged to an invalid temperature at stage 8 (Tcalc = -6.83388802861742 K). (SumRates.vb, 720)</Message>
- <Message>[03-02-2024 15:17:42] ABS-2: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 15:17:43] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:17:43] Error in 'ABS-2': Converged to an invalid temperature at stage 8 (Tcalc = -6.83388802861742 K). (SumRates.vb, 720)</Message>
- <Message>[03-02-2024 15:17:55] The flowsheet was calculated successfully. [1.082s]</Message>
- <Message>[03-02-2024 15:18:11] The flowsheet was calculated successfully. [1.467s]</Message>
- <Message>[03-02-2024 15:22:58] The flowsheet was calculated successfully. [0.01858s]</Message>
- <Message>[03-02-2024 15:23:38] The flowsheet was calculated successfully. [0.01359s]</Message>
- <Message>[03-02-2024 15:23:56] The flowsheet was calculated successfully. [0.01962s]</Message>
- <Message>[03-02-2024 15:24:10] The flowsheet was calculated successfully. [0.02029s]</Message>
- <Message>[03-02-2024 15:25:42] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 15:25:44] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:25:44] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 15:27:33] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:27:33] Error in 'PUMP-1': Check the connections of the object. (Pump.vb, 451)</Message>
- <Message>[03-02-2024 15:28:10] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 15:28:13] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:28:13] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 15:29:57] The flowsheet was calculated successfully. [0.02471s]</Message>
- <Message>[03-02-2024 15:31:00] The flowsheet was calculated successfully. [0.01522s]</Message>
- <Message>[03-02-2024 15:32:45] ABS-1: Column Solver did not converge. Will reset some parameters and try again shortly...</Message>
- <Message>[03-02-2024 15:32:47] Errors occurred during the calculation of the flowsheet, please read the following messages for more details.</Message>
- <Message>[03-02-2024 15:32:47] Error in 'ABS-1': Solver reached the maximum number of iterations without converging. (SumRates.vb, 808)</Message>
- <Message>[03-02-2024 15:34:32] The flowsheet was calculated successfully. [1.034s]</Message>
- <Message>[03-02-2024 17:01:57] File C:\Users\pc\AppData\Local\DWSIM\DWSIM12.dwxmz saved successfully.</Message>
- </MessagesLog>
-</DWSIM_Simulation_Data> \ No newline at end of file
diff --git a/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf
index 32a518d..8050927 100644
--- a/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf
+++ b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Abstract.pdf
Binary files differ
diff --git a/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz
index 54c3c86..59d5f74 100644
--- a/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz
+++ b/Process_Development_For_Production_Of_900_Tpd_Of_Phthalic_Anhydride_By_Oxidation_Of_O-Xylene_By_Mr_Achanta_Srinivasa_Kalyan/Flowsheet.dwxmz
Binary files differ
diff --git a/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf b/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/Abstract_2.pdf
index 4452778..4452778 100644
--- a/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf
+++ b/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/Abstract_2.pdf
Binary files differ
diff --git a/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz b/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz
index 46f4ed1..46f4ed1 100644
--- a/Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz
+++ b/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz
Binary files differ
diff --git a/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/README.txt b/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/README.txt
new file mode 100644
index 0000000..f51aeed
--- /dev/null
+++ b/Rankine_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_D._Chatumba_&_Emmanuel_Mtatiro/README.txt
@@ -0,0 +1,8 @@
+About the flowsheet
+
+Title Of The Flowsheet Project: Rankine Cycle utilizing Ammonia with Surface and Deep-Water Heat Exchange
+Proposar Name: Ms Bellisima D. Chatumba & Emmanuel Mtatiro
+University: Marwadi University, Rajkot
+
+
+DWSIM Flowsheet Project By FOSSEE, IIT Bombay
generated by cgit (git 2.34.1) at 2024-12-19 09:52:42 +0000