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authorSashi202024-02-16 00:20:16 +0550
committerSashi202024-02-16 00:20:16 +0550
commited80de3fbc4de714966d6b407715d100dddc5aa0 (patch)
treeeff941e4b4684bd5965e9b3fb1bb3b050c011593
parentb8b935e09486294452a19a7b8e7cc487cd500e5a (diff)
downloadDWSIM-Flowsheets-ed80de3fbc4de714966d6b407715d100dddc5aa0.tar.gz
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Added(A)/Deleted(D) following Flowsheet file
A Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf A Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml A Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmz A Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdf A Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdf A Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmz A Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Abstract.pdf A Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Flowsheet.dwxmz
Diffstat
-rw-r--r--Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdfbin0 -> 298877 bytes
-rw-r--r--Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml13965
-rw-r--r--Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.dwxmzbin0 -> 111487 bytes
-rw-r--r--Process_Flowdiagram_For_Manufacture_Of_Formaldehyde_By_Ms_Ranjana_Soni/formaldehyde.pdfbin0 -> 475172 bytes
-rw-r--r--Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/Abstract_2.pdfbin0 -> 112681 bytes
-rw-r--r--Rankine_Power_Plant_Cycle_Utilizing_Ammonia_With_Surface_And_Deep-Water_Heat_Exchange_By_Ms_Bellisima_Dunstan_Chatumba,_Emmanuel_Mtatiro/COMPLETE_FLOWSHEET.dwxmzbin0 -> 53210 bytes
-rw-r--r--Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Abstract.pdfbin0 -> 203370 bytes
-rw-r--r--Separation_Of_Separation_Of_Pyridine_And_Toluene_With_The_Help_Of_N_-_Propanol_By_Mr_Om_Pandey/Flowsheet.dwxmzbin0 -> 112575 bytes
8 files changed, 13965 insertions, 0 deletions
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
new file mode 100644
index 0000000..cc089da
--- /dev/null
+++ b/Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Abstract.pdf
Binary files differ
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
new file mode 100644
index 0000000..c892214
--- /dev/null
+++ b/Carbon_Capture_Process_From_Flue_Gas_By_Using_Mea_By_Mr_Abhishek_Anand/Flowsheet.dwxml
@@ -0,0 +1,13965 @@
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+<DWSIM_Simulation_Data>
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+ <BuildDate>2000-01-09T00:00:00</BuildDate>
+ <OSInfo>Microsoft Windows 10 Home, Version 10.0.19045.0, Win32NT Platform</OSInfo>
+ <SavedOn>2024-02-03T17:03:38.1873253+05:30</SavedOn>
+ <SavedFromClassicUI>true</SavedFromClassicUI>
+ </GeneralInfo>
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+Column Properties Profile
+========================================================
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+Stage P T mV wV rhoV etaV kV mL wL rhoL etaL kL sigma
+ Pa K mol/s kg/s kg/m3 Pa.s W/[m.K] mol/s kg/s kg/m3 Pa.s W/[m.K] N/m
+
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <ComponentName>OverallLiquid</ComponentName>
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+ <Compound>
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+ <Name>Sulfur dioxide</Name>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
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+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <Name>Monoethanolamine</Name>
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+ <Name>Nitrogen</Name>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
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+ <ComponentName>Water</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>Water</Name>
+ <PartialPressure>NaN</PartialPressure>
+ <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>
+ <Molality>0</Molality>
+ <FugacityCoeff>2322.27760959675</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>
+ <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>
+ <PartialPressure>0</PartialPressure>
+ <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>
+ <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>0.0182531027228281</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 />
+ </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>0.0615570993219995</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>
+ <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>-0.0346913527806408</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>
+ <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>0.0182531027228281</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 />
+ </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>0.0615570993219995</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>
+ <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>-0.0346913527806408</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>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>0.0182531027228281</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>
+ <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>-0.0350155913091071</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>1</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 />
+ </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>0.0615570993219995</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>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Nitrogen</Name>
+ <PartialPressure>0</PartialPressure>
+ <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>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>
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+ <molar_helmholtz_energy>0</molar_helmholtz_energy>
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+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</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>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Water</ComponentName>
+ <ActivityCoeff>0.955194295667027</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.407643228097578</MassFraction>
+ <MoleFraction>0.7</MoleFraction>
+ <Molarity>22256.5992107405</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.186958060297047</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.002101786870232</MassFlow>
+ <MolarFlow>0.1166669</MolarFlow>
+ <Name>Water</Name>
+ <PartialPressure>70927.5</PartialPressure>
+ <PartialVolume>0.0183303060479418</PartialVolume>
+ <VolumetricFlow>2.14037069987204E-06</VolumetricFlow>
+ <VolumetricFraction>0.408319521899221</VolumetricFraction>
+ <DiffusionCoefficient>2.01391410586202E-09</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</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>-0.0350155913524995</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</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>-0.0508427234926757</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>0.730612939890956</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.592356771902422</MassFraction>
+ <MoleFraction>0.3</MoleFraction>
+ <Molarity>9538.54251888878</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.00569285941594008</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.003054160108308</MassFlow>
+ <MolarFlow>0.0500001</MolarFlow>
+ <Name>Monoethanolamine</Name>
+ <PartialPressure>30397.5</PartialPressure>
+ <PartialVolume>0.0619774348694148</PartialVolume>
+ <VolumetricFlow>3.10153076473713E-06</VolumetricFlow>
+ <VolumetricFraction>0.591680478100779</VolumetricFraction>
+ <DiffusionCoefficient>1.78542894164771E-09</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>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>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>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>
+ <compressibilityFactor>0.000953212930857666</compressibilityFactor>
+ <density>983.602422393954</density>
+ <enthalpy>107.774661240083</enthalpy>
+ <enthalpyF>-7264.62647376222</enthalpyF>
+ <entropy>0.323647631351601</entropy>
+ <entropyF>-7.40109317394876</entropyF>
+ <heatCapacityCp>0</heatCapacityCp>
+ <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+ <kinematic_viscosity>1.84401349077913E-06</kinematic_viscosity>
+ <massflow>0.00515594697854</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>3334.07596575194</molar_enthalpy>
+ <molar_entropy>10.0122401373932</molar_entropy>
+ <molarflow>0.166667</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>30.93562</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <surfaceTension>0.059786847784746</surfaceTension>
+ <thermalConductivity>0.350867217203115</thermalConductivity>
+ <viscosity>0.00181377613645748</viscosity>
+ <volumetric_flow>5.24190146460918E-06</volumetric_flow>
+ <bulk_modulus>-481.294422016988</bulk_modulus>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>-0.0853071345678984</helmholtz_energy>
+ <internal_energy>107.689354105515</internal_energy>
+ <isothermal_compressibility>-0.00207773029200971</isothermal_compressibility>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-2.63902909828137</molar_helmholtz_energy>
+ <molar_internal_energy>3331.43693665366</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.66303452370794</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.19275263058567</idealGasHeatCapacityRatio>
+ </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>
+ <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>Water</Name>
+ <PartialPressure>NaN</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>
+ <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>
+ <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>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>
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+ <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>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
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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>-0.0350155913524995</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>1</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>
+ <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>0.0619774348694148</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>
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+ <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>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.Thermodynamics.Streams.MaterialStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
+ <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
+ <DefinedFlow>Mole</DefinedFlow>
+ <ForcePhase>GlobalDef</ForcePhase>
+ <TotalEnergyFlow>-609.137421152788</TotalEnergyFlow>
+ <AtEquilibrium>true</AtEquilibrium>
+ <ComponentDescription>CorrentedeMatria</ComponentDescription>
+ <ComponentName>MAT-d25f0503-ca24-4931-8050-9ee961fb1d87</ComponentName>
+ <Name2>MAT-d25f0503-ca24-4931-8050-9ee961fb1d87</Name2>
+ <code>0</code>
+ <InputComposition />
+ <IsElectrolyteStream>false</IsElectrolyteStream>
+ <ReferenceSolvent></ReferenceSolvent>
+ <SpecType>Temperature_and_Pressure</SpecType>
+ <CompositionBasis>Molar_Fractions</CompositionBasis>
+ <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0,"ShowAsPercentage":0}</EditorState>
+ <MobileCompatible>true</MobileCompatible>
+ <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 15:34:31</LastUpdated>
+ <ErrorMessage></ErrorMessage>
+ <Annotation></Annotation>
+ <IsAdjustAttached>false</IsAdjustAttached>
+ <AttachedAdjustId></AttachedAdjustId>
+ <AdjustVarType>Manipulated</AdjustVarType>
+ <IsSpecAttached>false</IsSpecAttached>
+ <AttachedSpecId></AttachedSpecId>
+ <SpecVarType>Source</SpecVarType>
+ <Name>MAT-d25f0503-ca24-4931-8050-9ee961fb1d87</Name>
+ <UserDefinedChartNames />
+ <ProductName>Material Stream</ProductName>
+ <ProductDescription>Contains information about compounds flowing at specified state conditions</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 />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ <PropertyPackage>PP-1e37eef4-3b36-471d-bec1-e3a7631125c5</PropertyPackage>
+ <Phases>
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+ <lnKvalue>NaN</lnKvalue>
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+ <MolarFlow>0</MolarFlow>
+ <Name>Water</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Carbon dioxide</ComponentName>
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+ <Molarity>10.247558118619</Molarity>
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+ <MassFlow>0.0684592769896</MassFlow>
+ <MolarFlow>1.5555568</MolarFlow>
+ <Name>Carbon dioxide</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <ComponentName>Sulfur dioxide</ComponentName>
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+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.00711820569456</MassFlow>
+ <MolarFlow>0.1111112</MolarFlow>
+ <Name>Sulfur dioxide</Name>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <ComponentName>Monoethanolamine</ComponentName>
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+ <Molarity>0</Molarity>
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+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Monoethanolamine</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
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+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <MassFlow>0.1089410871528</MassFlow>
+ <MolarFlow>3.888892</MolarFlow>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <molarflow>5.55556</molarflow>
+ <molecularWeight>33.213316</molecularWeight>
+ <pressure>101325</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>333</temperature>
+ <thermalConductivity>0.0251318437852278</thermalConductivity>
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+ <FugacityCoeff>0.0265647773035096</FugacityCoeff>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <Molarity>0</Molarity>
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+ <FugacityCoeff>77.2142096856098</FugacityCoeff>
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+ <MolarFlow>NaN</MolarFlow>
+ <Name>Carbon dioxide</Name>
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+ <PartialVolume>-0.0350155913524995</PartialVolume>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <ComponentName>Sulfur dioxide</ComponentName>
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+ <Molarity>0</Molarity>
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+ <FugacityCoeff>4.53852141658536</FugacityCoeff>
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+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <Name>Sulfur dioxide</Name>
+ <PartialPressure>6659.07425640751</PartialPressure>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <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>
+ <PetroleumFraction>false</PetroleumFraction>
+ <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>
+ <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>Water</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>14.8206216418538</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>1.83324442191774E-10</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>0.00746754174834561</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.371015649265493</MassFraction>
+ <MoleFraction>0.28</MoleFraction>
+ <Molarity>10.247558118619</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.0684592769896</MassFlow>
+ <MolarFlow>1.5555568</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>28371</PartialPressure>
+ <PartialVolume>36.2052739756009</PartialVolume>
+ <VolumetricFlow>0.056319360128609</VolumetricFlow>
+ <VolumetricFraction>0.371015649265493</VolumetricFraction>
+ <DiffusionCoefficient>7.26386790212642E-11</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>0.089137741993155</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.0385771779005746</MassFraction>
+ <MoleFraction>0.02</MoleFraction>
+ <Molarity>0.731968437044213</Molarity>
+ <Molality>0</Molality>
+ <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>
+ <PartialPressure>0</PartialPressure>
+ <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>
+ <DynamicProperties />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Nitrogen</ComponentName>
+ <ActivityCoeff>8.78979993738132E-06</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.590407172833932</MassFraction>
+ <MoleFraction>0.7</MoleFraction>
+ <Molarity>25.6188952965474</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>1</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.1089410871528</MassFlow>
+ <MolarFlow>3.888892</MolarFlow>
+ <Name>Nitrogen</Name>
+ <PartialPressure>70927.5</PartialPressure>
+ <PartialVolume>23.0457701629898</PartialVolume>
+ <VolumetricFlow>0.0896225112206896</VolumetricFlow>
+ <VolumetricFraction>0.590407172833932</VolumetricFraction>
+ <DiffusionCoefficient>1.16854456023557E-10</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <compressibilityFactor>0.998934990262258</compressibilityFactor>
+ <density>1.21555495007878</density>
+ <enthalpy>194.95048035001</enthalpy>
+ <enthalpyF>-3301.22557144801</enthalpyF>
+ <entropy>1.04514505828139</entropy>
+ <entropyF>1.04514505828139</entropyF>
+ <heatCapacityCp>0.966018267943794</heatCapacityCp>
+ <heatCapacityCv>0.713711887584387</heatCapacityCv>
+ <jouleThomsonCoefficient>-6.15144757441045E-09</jouleThomsonCoefficient>
+ <kinematic_viscosity>1.54474552418893E-05</kinematic_viscosity>
+ <massflow>0.18451856983696</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>6474.95190821669</molar_enthalpy>
+ <molar_entropy>34.7127330865383</molar_entropy>
+ <molarflow>5.55556</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>33.213316</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <thermalConductivity>0.0251318437852278</thermalConductivity>
+ <viscosity>1.87772306853989E-05</viscosity>
+ <volumetric_flow>0.151797802168468</volumetric_flow>
+ <bulk_modulus>-1262276.80897478</bulk_modulus>
+ <gibbs_free_energy>-153.082824057694</gibbs_free_energy>
+ <helmholtz_energy>-236.351036557477</helmholtz_energy>
+ <internal_energy>111.682267850227</internal_energy>
+ <isothermal_compressibility>-7.92219260379347E-07</isothermal_compressibility>
+ <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>
+ </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>
+ <MassFraction>0</MassFraction>
+ <MoleFraction>0</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.195833425719739</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>
+ <MassFraction>0.0277901221347548</MassFraction>
+ <MoleFraction>0.0398901098732776</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>15531085.0322431</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>0.971074160036559</MassFraction>
+ <MoleFraction>0.957548794276369</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>11.4339486011974</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0</MassFlow>
+ <MolarFlow>0</MolarFlow>
+ <Name>Sulfur dioxide</Name>
+ <PartialPressure>1109363.21658784</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>0.00780945174630694</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>
+ <MassFraction>0.00113571782868654</MassFraction>
+ <MoleFraction>0.00256109585035323</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>38827712.5806078</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>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>0.0150336108555471</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>
+ <idealGasHeatCapacityCp>1.41130821640742</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.1652965684796</idealGasHeatCapacityRatio>
+ </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>
+ <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>Water</Name>
+ <PartialPressure>NaN</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>
+ <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>
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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>
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+ <PartialVolume>-0.0346914052009311</PartialVolume>
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+ <DiffusionCoefficient>NaN</DiffusionCoefficient>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.0684590555585493</MassFlow>
+ <MolarFlow>1.55555176856245</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.0520159725431199</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>Sulfur dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.0380777749140225</MassFraction>
+ <MoleFraction>0.019562047397377</MoleFraction>
+ <Molarity>0.782263464779749</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.00711142207150602</MassFlow>
+ <MolarFlow>0.111005311447432</MolarFlow>
+ <Name>Sulfur dioxide</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.0054033397363718</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>Monoethanolamine</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.000787492172904758</MassFraction>
+ <MoleFraction>0.000424307549124958</MoleFraction>
+ <Molarity>0.0169675641188355</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.000147072386245731</MassFlow>
+ <MolarFlow>0.00240774345769289</MolarFlow>
+ <Name>Monoethanolamine</Name>
+ <PartialPressure>0</PartialPressure>
+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.000111747279339347</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>27.4053449677934</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>NaN</Kvalue>
+ <lnKvalue>NaN</lnKvalue>
+ <MassFlow>0.108941113058258</MassFlow>
+ <MolarFlow>3.88889292475236</MolarFlow>
+ <Name>Nitrogen</Name>
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+ <PartialVolume>0</PartialVolume>
+ <VolumetricFlow>0.0827747023300497</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>Infinity</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Mixture</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Mixture</Name>
+ <Properties1>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties1>
+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>1.3161160353543</density>
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+ <heatCapacityCp>0.965856733894926</heatCapacityCp>
+ <heatCapacityCv>0.71049223623676</heatCapacityCv>
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+ <molar_entropy>34.2665462464507</molar_entropy>
+ <molarflow>5.67452420457363</molarflow>
+ <molecularWeight>32.9120883477509</molecularWeight>
+ <pressure>101325</pressure>
+ <surfaceTension>NaN</surfaceTension>
+ <temperature>304.766938114461</temperature>
+ <thermalConductivity>0.023007545535211</thermalConductivity>
+ <volumetric_flow>0.141902717492612</volumetric_flow>
+ <gibbs_free_energy>-122.854152068868</gibbs_free_energy>
+ <helmholtz_energy>-199.709399318849</helmholtz_energy>
+ <internal_energy>117.599860091972</internal_energy>
+ <molar_gibbs_free_energy>-4043.38670677862</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-6572.85339425823</molar_helmholtz_energy>
+ <molar_internal_energy>3870.45698503013</molar_internal_energy>
+ </Properties>
+ </Phase>
+ <Phase>
+ <ID>1</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Water</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</MolarFlow>
+ <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 />
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Carbon dioxide</ComponentName>
+ <ActivityCoeff>0</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</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>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</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>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</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>
+ <MassFraction>NaN</MassFraction>
+ <MoleFraction>NaN</MoleFraction>
+ <Molarity>0</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>NaN</MassFlow>
+ <MolarFlow>NaN</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 />
+ </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>
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+ <Properties>
+ <Type>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Type>
+ <density>0</density>
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+ <entropy>0</entropy>
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+ <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>
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+ <ComponentName>Water</ComponentName>
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+ <lnKvalue>0</lnKvalue>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Carbon dioxide</ComponentName>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <ComponentName>Sulfur dioxide</ComponentName>
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+ <Name>Sulfur dioxide</Name>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
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+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
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+ <thermalConductivity>0.023007545535211</thermalConductivity>
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+ <idealGasHeatCapacityRatio>1.35552463891503</idealGasHeatCapacityRatio>
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+ <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>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>
+ <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>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>0.0181160870461316</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>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>0.0181160870461316</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>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <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>Infinity</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>6.93269197705042E-11</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>Infinity</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>4.28304633723866E-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>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>Infinity</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>3.81468650575455E-11</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>Infinity</PartialVolume>
+ <VolumetricFlow>0</VolumetricFlow>
+ <VolumetricFraction>0</VolumetricFraction>
+ <DiffusionCoefficient>1.11526800965083E-10</DiffusionCoefficient>
+ <EnthalpyF_Dmol>0</EnthalpyF_Dmol>
+ <EntropyF_Dmol>0</EntropyF_Dmol>
+ <DynamicProperties />
+ </Compound>
+ </Compounds>
+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Vapor</ComponentName>
+ <Compounds>System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]</Compounds>
+ <Name>Vapor</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>3</ID>
+ <Compounds>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
+ <ComponentDescription></ComponentDescription>
+ <ComponentName>Water</ComponentName>
+ <ActivityCoeff>0.481122339437237</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>4.47520006112097E-14</MassFraction>
+ <MoleFraction>1.51749579690431E-13</MoleFraction>
+ <Molarity>2.46640953601134E-09</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.0619787745639849</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>1.30410434881698E-16</MassFlow>
+ <MolarFlow>7.23887915601077E-15</MolarFlow>
+ <Name>Water</Name>
+ <PartialPressure>1.53760261621329E-08</PartialPressure>
+ <PartialVolume>0.0182530668217087</PartialVolume>
+ <VolumetricFlow>1.32618556613103E-19</VolumetricFlow>
+ <VolumetricFraction>4.51854031036032E-14</VolumetricFraction>
+ <DiffusionCoefficient>5.4345463706948E-10</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>28.2274112427611</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>6.35017315044182E-05</MassFraction>
+ <MoleFraction>8.81444944565744E-05</MoleFraction>
+ <Molarity>1.43262618662991</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>3162.52151943365</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>1.85048451647492E-07</MassFlow>
+ <MolarFlow>4.20473878702308E-06</MolarFlow>
+ <Name>Carbon dioxide</Name>
+ <PartialPressure>8.9312409008124</PartialPressure>
+ <PartialVolume>-0.0350155915784445</PartialVolume>
+ <VolumetricFlow>-1.4777385929161E-10</VolumetricFlow>
+ <VolumetricFraction>-5.03490730919838E-05</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>1.01475477774806</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.00232971194218149</MassFraction>
+ <MoleFraction>0.00222149627125372</MoleFraction>
+ <Molarity>36.1063246357005</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>8.96745736917361</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>6.78894224569864E-06</MassFlow>
+ <MolarFlow>0.000105971582168067</MolarFlow>
+ <Name>Sulfur dioxide</Name>
+ <PartialPressure>225.093109684783</PartialPressure>
+ <PartialVolume>-0.0497223505392422</PartialVolume>
+ <VolumetricFlow>-5.28856925499482E-09</VolumetricFlow>
+ <VolumetricFraction>-0.00180190570408193</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>1.00230618415452</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>0.997604354293432</MassFraction>
+ <MoleFraction>0.997685055769588</MoleFraction>
+ <Molarity>16215.5304845387</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>0.00443507396485214</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>0.00290708830681179</MassFlow>
+ <MolarFlow>0.0475923661153267</MolarFlow>
+ <Name>Monoethanolamine</Name>
+ <PartialPressure>101090.438275854</PartialPressure>
+ <PartialVolume>0.0615568933158706</PartialVolume>
+ <VolumetricFlow>2.94043184029424E-06</VolumetricFlow>
+ <VolumetricFraction>1.00185525612362</VolumetricFraction>
+ <DiffusionCoefficient>4.82546027095587E-10</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>1.76191241412004</ActivityCoeff>
+ <PetroleumFraction>false</PetroleumFraction>
+ <MassFraction>2.43203283693362E-06</MassFraction>
+ <MoleFraction>5.30346454995512E-06</MoleFraction>
+ <Molarity>0.0861980347266309</Molarity>
+ <Molality>0</Molality>
+ <FugacityCoeff>131403.939563236</FugacityCoeff>
+ <Kvalue>0</Kvalue>
+ <lnKvalue>0</lnKvalue>
+ <MassFlow>7.08711243250292E-09</MassFlow>
+ <MolarFlow>2.52990084477533E-07</MolarFlow>
+ <Name>Nitrogen</Name>
+ <PartialPressure>0.537373545524202</PartialPressure>
+ <PartialVolume>-0.0346913854570536</PartialVolume>
+ <VolumetricFlow>-8.80891199043205E-12</VolumetricFlow>
+ <VolumetricFraction>-3.00134648843334E-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>
+ <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>
+ <compressibilityFactor>0.00202655579575652</compressibilityFactor>
+ <density>992.873118051945</density>
+ <enthalpy>72.4491533059683</enthalpy>
+ <enthalpyF>-3139.97091438981</enthalpyF>
+ <entropy>0.2234445010165</entropy>
+ <entropyF>0.223444501015652</entropyF>
+ <heatCapacityCp>0</heatCapacityCp>
+ <jouleThomsonCoefficient>-Infinity</jouleThomsonCoefficient>
+ <kinematic_viscosity>6.60826285597271E-06</kinematic_viscosity>
+ <massflow>0.0029140693846217</massflow>
+ <massfraction>1</massfraction>
+ <molar_enthalpy>4425.77542266973</molar_enthalpy>
+ <molar_entropy>13.6497824447047</molar_entropy>
+ <molarflow>0.0477027954263735</molarflow>
+ <molarfraction>1</molarfraction>
+ <molecularWeight>61.0880213324059</molecularWeight>
+ <speedOfSound>NaN</speedOfSound>
+ <surfaceTension>0.0454250114102616</surfaceTension>
+ <thermalConductivity>0.24306156802104</thermalConductivity>
+ <viscosity>0.00656116654671647</viscosity>
+ <volumetric_flow>2.9349866882681E-06</volumetric_flow>
+ <bulk_modulus>-707.715717635281</bulk_modulus>
+ <gibbs_free_energy>0</gibbs_free_energy>
+ <helmholtz_energy>-0.0894285461445463</helmholtz_energy>
+ <internal_energy>72.3597247598237</internal_energy>
+ <isothermal_compressibility>-0.00141299673736418</isothermal_compressibility>
+ <molar_gibbs_free_energy>0</molar_gibbs_free_energy>
+ <molar_helmholtz_energy>-5.46301293460409</molar_helmholtz_energy>
+ <molar_internal_energy>4420.31240973513</molar_internal_energy>
+ <idealGasHeatCapacityCp>1.48516862145905</idealGasHeatCapacityCp>
+ <idealGasHeatCapacityRatio>1.10088335128415</idealGasHeatCapacityRatio>
+ </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>0.0182530668217087</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>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>0.0182530668217087</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>
+ <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>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>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-46cbf572-c01f-4e37-a8ed-ec90e9876fd8</Name>
+ <UserDefinedChartNames />
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</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 />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
+ <ObjectClass>Streams</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <ComponentDescription>CorrentedeEnergia</ComponentDescription>
+ <ComponentName>EN-e7423dc4-95af-4830-997f-4af297814d5a</ComponentName>
+ <EnergyFlow>0.00014352084905631</EnergyFlow>
+ <MobileCompatible>true</MobileCompatible>
+ <Name2>EN-e7423dc4-95af-4830-997f-4af297814d5a</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>
+ <SpecVarType>Source</SpecVarType>
+ <Name>EN-e7423dc4-95af-4830-997f-4af297814d5a</Name>
+ <UserDefinedChartNames />
+ <ProductName>Energy Stream</ProductName>
+ <ProductDescription>Energy flow from/to Unit Operations</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 />
+ <DynamicPropertiesDescriptions />
+ <DynamicPropertiesUnitTypes />
+ <AttachedUtilities />
+ </SimulationObject>
+ <SimulationObject>
+ <Type>DWSIM.UnitOperations.UnitOperations.Pump</Type>
+ <ObjectClass>PressureChangers</ObjectClass>
+ <SupportsDynamicMode>true</SupportsDynamicMode>
+ <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
+ <PumpType></PumpType>
+ <ImpellerDiameter>200</ImpellerDiameter>
+ <ImpellerSpeed>1450</ImpellerSpeed>
+ <DiameterUnit>mm</DiameterUnit>
+ <OutletTemperature>324.242148660858</OutletTemperature>
+ <CurveFlow>0</CurveFlow>
+ <CurveSysHead>0</CurveSysHead>
+ <CurvePower>0</CurvePower>
+ <CurveNPSHr>0</CurveNPSHr>
+ <CurveEff>0</CurveEff>
+ <CurveHead>0</CurveHead>
+ <Pout>138000</Pout>
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+ <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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+ <EntropyF_Dmol>0</EntropyF_Dmol>
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+ <Name>Sulfur dioxide</Name>
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+ <Name>Monoethanolamine</Name>
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+ <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>
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+ <ObjectType Value="AbsorptionColumn">
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+ <PropertyID Value="PROP_AC_1" />
+ <PropertyID Value="PROP_AC_2" />
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+ <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" />
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+ <ObjectType Value="AnalogGauge">
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+ <ObjectType Value="CapeOpenUO" />
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+ <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" />
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+ <PropertyID Value="Reset Content" />
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+ <PropertyID Value="PROP_CL_4" />
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+ <ObjectType Value="CustomUO" />
+ <ObjectType Value="DigitalGauge">
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+ </ObjectType>
+ <ObjectType Value="DistillationColumn">
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+ <PropertyID Value="Reboiler_Specification_Value" />
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+ <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">
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+ </ObjectType>
+ <ObjectType Value="Expander">
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+ <PropertyID Value="PROP_TU_2" />
+ <PropertyID Value="PROP_TU_3" />
+ <PropertyID Value="PROP_TU_4" />
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+ <PropertyID Value="PolytropicCoefficient" />
+ <PropertyID Value="AdiabaticHead" />
+ <PropertyID Value="PolytropicHead" />
+ <PropertyID Value="RotationSpeed" />
+ <PropertyID Value="PressureRatio" />
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+ <ObjectType Value="Filter">
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+ <PropertyID Value="PROP_FT_7" />
+ </ObjectType>
+ <ObjectType Value="Flowsheet" />
+ <ObjectType Value="Heater">
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+ <PropertyID Value="Minimum Pressure" />
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+ <ObjectType Value="HeatExchanger">
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+ <ObjectType Value="Input" />
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+ <ObjectType Value="MaterialStream">
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+ <ObjectType Value="Mixer" />
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+ <ObjectType Value="PIDController">
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+ <ObjectType Value="Pipe">
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+ <ObjectType Value="Pump">
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+ <ObjectType Value="PythonController">
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+ <PropertyID Value="Final Gibbs Energy" />
+ <PropertyID Value="Element Balance Residue" />
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+ <PropertyID Value="Actual Flow Coefficient" />
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+ <ObjectType Value="Vessel">
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+ <PropertyID Value="Reset Content" />
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+ <ObjectType Value="NeuralNetworkUnitOperation">
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+ <PropertyID Value="Status" />
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+ <PropertyID Value="Number of Network Objects" />
+ <PropertyID Value="Mass Balance Residual" />
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+ <PropertyID Value="Energy Balance Residual" />
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+ <ObjectType Value="HydroelectricTurbine">
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+ <PropertyID Value="Generated Power" />
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+ <PropertyID Value="JMax" />
+ <PropertyID Value="N" />
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+ <ObjectType Value="SolarPanel">
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+ <PropertyID Value="User-Defined Solar Irradiation" />
+ <PropertyID Value="Actual Solar Irradiation" />
+ <PropertyID Value="Panel Area" />
+ <PropertyID Value="Number of Panels" />
+ <PropertyID Value="Generated Power" />
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+ <ObjectType Value="WaterElectrolyzer">
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+ <PropertyID Value="Reversible Voltage" />
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+ <PropertyID Value="Cell Voltage" />
+ <PropertyID Value="Waste Heat" />
+ <PropertyID Value="Current" />
+ <PropertyID Value="Electron Transfer" />
+ <PropertyID Value="Efficiency" />
+ <PropertyID Value="Input Efficiency" />
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+ <ObjectType Value="WindTurbine">
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+ <PropertyID Value="Actual Air Pressure" />
+ <PropertyID Value="User-Defined Relative Humidity" />
+ <PropertyID Value="Actual Relative Humidity" />
+ <PropertyID Value="Disk Area" />
+ <PropertyID Value="Rotor Diameter" />
+ <PropertyID Value="Number of Units" />
+ <PropertyID Value="Generated Power" />
+ <PropertyID Value="Maximum Theoretical Power" />
+ <PropertyID Value="Calculated Air Density" />
+ </ObjectType>
+ <ObjectType Value="Reactor_ReaktoroGibbs" />
+ </VisibleProperties>
+ </Settings>
+ <DynamicProperties />
+ <GraphicObjects>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
+ <FillColor>#ffffffff</FillColor>
+ <FillColorDark>#ffffffff</FillColorDark>
+ <GradientColor1>#ffd3d3d3</GradientColor1>
+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-11374d2f-d253-4ab2-87b0-d0bc95305655</Name>
+ <Tag>S-05</Tag>
+ <Width>20</Width>
+ <X>692.9401</X>
+ <Y>275.0369</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="BB-b6d3f736-727a-496f-9208-0f3e6b7854a4" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="AQ-a0ad804b-a1ce-4722-88a1-a1cf95d5bd50" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.AbsorptionColumnGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
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+ <Fill>true</Fill>
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+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Absorption Column</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>AbsorptionColumn</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>180</Height>
+ <IsConnector>false</IsConnector>
+ <Name>ABS-12c8d14c-498b-4d5d-a685-7a0eca300a7d</Name>
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+ <Y>148.2879</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-5df78176-dfb7-4371-8aa0-21cb07aed80f" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-d25f0503-ca24-4931-8050-9ee961fb1d87" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-913864fa-289f-465d-ab44-51ef0e4a8fbc" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-4f13085e-f0a3-4844-9dde-48b2e89a4758" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ <Connector IsAttached="false" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <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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+ <Fill>true</Fill>
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+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-5df78176-dfb7-4371-8aa0-21cb07aed80f</Name>
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+ <Width>20</Width>
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+ <Y>130.6628</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="false" />
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+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="ABS-12c8d14c-498b-4d5d-a685-7a0eca300a7d" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <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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+ <Fill>true</Fill>
+ <FillColor>#ffffffff</FillColor>
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+ <GradientColor1>#ffd3d3d3</GradientColor1>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-d25f0503-ca24-4931-8050-9ee961fb1d87</Name>
+ <Tag>S-02</Tag>
+ <Width>20</Width>
+ <X>156.4407</X>
+ <Y>311.9119</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="false" />
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+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="ABS-12c8d14c-498b-4d5d-a685-7a0eca300a7d" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <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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+ <Fill>true</Fill>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-913864fa-289f-465d-ab44-51ef0e4a8fbc</Name>
+ <Tag>S-03</Tag>
+ <Width>20</Width>
+ <X>486.9396</X>
+ <Y>174.2878</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="ABS-12c8d14c-498b-4d5d-a685-7a0eca300a7d" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ </InputConnectors>
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+ <Connector IsAttached="false" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.PumpGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
+ <FillColor>#ffffffff</FillColor>
+ <FillColorDark>#ffffffff</FillColorDark>
+ <GradientColor1>#ffd3d3d3</GradientColor1>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Adiabatic Pump</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Pump</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>40</Height>
+ <IsConnector>false</IsConnector>
+ <Name>BB-b6d3f736-727a-496f-9208-0f3e6b7854a4</Name>
+ <Tag>PUMP-1</Tag>
+ <Width>40</Width>
+ <X>580.3148</X>
+ <Y>267.2869</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-4f13085e-f0a3-4844-9dde-48b2e89a4758" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-e7423dc4-95af-4830-997f-4af297814d5a" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-11374d2f-d253-4ab2-87b0-d0bc95305655" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
+ <FillColor>#ffd3d3d3</FillColor>
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+ <GradientColor1>#ffd3d3d3</GradientColor1>
+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>true</IsEnergyStream>
+ <ObjectType>EnergyStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>EN-e7423dc4-95af-4830-997f-4af297814d5a</Name>
+ <Tag>E1</Tag>
+ <Width>20</Width>
+ <X>553.4399</X>
+ <Y>343.163</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="false" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="BB-b6d3f736-727a-496f-9208-0f3e6b7854a4" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.HeaterGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
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+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream Heater</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>Heater</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>25</Height>
+ <IsConnector>false</IsConnector>
+ <Name>AQ-a0ad804b-a1ce-4722-88a1-a1cf95d5bd50</Name>
+ <Tag>HT-1</Tag>
+ <Width>25</Width>
+ <X>762.5905</X>
+ <Y>274.7369</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="MAT-11374d2f-d253-4ab2-87b0-d0bc95305655" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ <Connector IsAttached="true" ConnType="ConEn" AttachedFromObjID="EN-46cbf572-c01f-4e37-a8ed-ec90e9876fd8" AttachedFromConnIndex="0" AttachedFromEnergyConn="True" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="MAT-b77eb592-349c-4607-91c3-1395dae64026" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
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+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Energy Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>true</IsEnergyStream>
+ <ObjectType>EnergyStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>EN-46cbf572-c01f-4e37-a8ed-ec90e9876fd8</Name>
+ <Tag>E2</Tag>
+ <Width>20</Width>
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+ <Y>345.413</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="false" />
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+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="AQ-a0ad804b-a1ce-4722-88a1-a1cf95d5bd50" AttachedToConnIndex="1" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <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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+ <FillColor>#ffffffff</FillColor>
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+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-b77eb592-349c-4607-91c3-1395dae64026</Name>
+ <Tag>S-06</Tag>
+ <Width>20</Width>
+ <X>856.1907</X>
+ <Y>176.537</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="AQ-a0ad804b-a1ce-4722-88a1-a1cf95d5bd50" AttachedFromConnIndex="0" AttachedFromEnergyConn="False" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="false" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ <GraphicObject>
+ <Type>DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic</Type>
+ <SemiTransparent>false</SemiTransparent>
+ <LineWidth>1</LineWidth>
+ <GradientMode>true</GradientMode>
+ <LineColor>#ff4682b4</LineColor>
+ <LineColorDark>#fff5f5f5</LineColorDark>
+ <Fill>true</Fill>
+ <FillColor>#ffffffff</FillColor>
+ <FillColorDark>#ffffffff</FillColorDark>
+ <GradientColor1>#ffd3d3d3</GradientColor1>
+ <GradientColor2>#ffffffff</GradientColor2>
+ <FontSize>10</FontSize>
+ <OverrideColors>false</OverrideColors>
+ <FontStyle>Bold</FontStyle>
+ <Calculated>true</Calculated>
+ <Active>true</Active>
+ <Description>Material Stream</Description>
+ <FlippedH>false</FlippedH>
+ <FlippedV>false</FlippedV>
+ <IsEnergyStream>false</IsEnergyStream>
+ <ObjectType>MaterialStream</ObjectType>
+ <Shape>0</Shape>
+ <ShapeOverride>DefaultShape</ShapeOverride>
+ <Status>Calculated</Status>
+ <AutoSize>false</AutoSize>
+ <Height>20</Height>
+ <IsConnector>false</IsConnector>
+ <Name>MAT-4f13085e-f0a3-4844-9dde-48b2e89a4758</Name>
+ <Tag>S-04</Tag>
+ <Width>20</Width>
+ <X>463.375</X>
+ <Y>293.75</Y>
+ <Selected>false</Selected>
+ <Rotation>0</Rotation>
+ <DrawMode>2</DrawMode>
+ <InputConnectors>
+ <Connector IsAttached="true" ConnType="ConIn" AttachedFromObjID="ABS-12c8d14c-498b-4d5d-a685-7a0eca300a7d" AttachedFromConnIndex="1" AttachedFromEnergyConn="False" />
+ </InputConnectors>
+ <OutputConnectors>
+ <Connector IsAttached="true" ConnType="ConOut" AttachedToObjID="BB-b6d3f736-727a-496f-9208-0f3e6b7854a4" AttachedToConnIndex="0" AttachedToEnergyConn="False" />
+ </OutputConnectors>
+ <EnergyConnector>
+ <Connector IsAttached="false" />
+ </EnergyConnector>
+ <SpecialConnectors />
+ </GraphicObject>
+ </GraphicObjects>
+ <PropertyPackages>
+ <PropertyPackage>
+ <ID>PP-1e37eef4-3b36-471d-bec1-e3a7631125c5</ID>
+ <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>
+ <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>
+ </PropertyPackage>
+ </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>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <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>
+ <Item GroupID="17" Value="1" />
+ </UNIFACGroups>
+ <MODFACGroups>
+ <Item GroupID="16" Value="1" />
+ </MODFACGroups>
+ <NISTMODFACGroups>
+ <Item GroupID="16" Value="1" />
+ </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>
+ <HVap_B>0.35366</HVap_B>
+ <HVap_C>-0.46134</HVap_C>
+ <HVap_D>0.43554</HVap_D>
+ <HVap_E>0.037671</HVap_E>
+ <HVap_TMAX>304.21</HVap_TMAX>
+ <HVap_TMIN>216.58</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>909</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>28933</Ideal_Gas_Heat_Capacity_Const_A>
+ <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>
+ <IG_Entropy_of_Formation_25C>0.0655416247361437</IG_Entropy_of_Formation_25C>
+ <IG_Gibbs_Energy_of_Formation_25C>-8961.01977982027</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>2.768</Liquid_Density_Const_A>
+ <Liquid_Density_Const_B>0.26212</Liquid_Density_Const_B>
+ <Liquid_Density_Const_C>304.21</Liquid_Density_Const_C>
+ <Liquid_Density_Const_D>0.2908</Liquid_Density_Const_D>
+ <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+ <Liquid_Density_Tmax>304.21</Liquid_Density_Tmax>
+ <Liquid_Density_Tmin>216.58</Liquid_Density_Tmin>
+ <Liquid_Heat_Capacity_Const_A>80592</Liquid_Heat_Capacity_Const_A>
+ <Liquid_Heat_Capacity_Const_B>108.83</Liquid_Heat_Capacity_Const_B>
+ <Liquid_Heat_Capacity_Const_C>-6.9126</Liquid_Heat_Capacity_Const_C>
+ <Liquid_Heat_Capacity_Const_D>0.059647</Liquid_Heat_Capacity_Const_D>
+ <Liquid_Heat_Capacity_Const_E>6.9922E-06</Liquid_Heat_Capacity_Const_E>
+ <Liquid_Heat_Capacity_Tmax>290</Liquid_Heat_Capacity_Tmax>
+ <Liquid_Heat_Capacity_Tmin>216.58</Liquid_Heat_Capacity_Tmin>
+ <Liquid_Thermal_Conductivity_Const_A>-0.24975</Liquid_Thermal_Conductivity_Const_A>
+ <Liquid_Thermal_Conductivity_Const_B>-55.106</Liquid_Thermal_Conductivity_Const_B>
+ <Liquid_Thermal_Conductivity_Const_C>0.41735</Liquid_Thermal_Conductivity_Const_C>
+ <Liquid_Thermal_Conductivity_Const_D>-0.0051067</Liquid_Thermal_Conductivity_Const_D>
+ <Liquid_Thermal_Conductivity_Const_E>2.0157E-06</Liquid_Thermal_Conductivity_Const_E>
+ <Liquid_Thermal_Conductivity_Tmax>300</Liquid_Thermal_Conductivity_Tmax>
+ <Liquid_Thermal_Conductivity_Tmin>216.58</Liquid_Thermal_Conductivity_Tmin>
+ <Liquid_Viscosity_Const_A>-7.7022</Liquid_Viscosity_Const_A>
+ <Liquid_Viscosity_Const_B>-166.34</Liquid_Viscosity_Const_B>
+ <Liquid_Viscosity_Const_C>0.38094</Liquid_Viscosity_Const_C>
+ <Liquid_Viscosity_Const_D>-4.018E-05</Liquid_Viscosity_Const_D>
+ <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+ <LiquidDensityEquation>105</LiquidDensityEquation>
+ <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
+ <LiquidThermalConductivityEquation>16</LiquidThermalConductivityEquation>
+ <LiquidViscosityEquation>101</LiquidViscosityEquation>
+ <Molar_Weight>44.0095</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>Carbon dioxide</Name>
+ <NBP>194.686</NBP>
+ <NegativeIon></NegativeIon>
+ <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
+ <Normal_Boiling_Point>194.686</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=C=O</SMILES>
+ <Solid_Density_Const_A>42.04</Solid_Density_Const_A>
+ <Solid_Density_Const_B>-0.034421</Solid_Density_Const_B>
+ <Solid_Density_Const_C>-0.0002847</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>216.58</Solid_Density_Tmax>
+ <Solid_Density_Tmin>143.1</Solid_Density_Tmin>
+ <Solid_Heat_Capacity_Const_A>-18283</Solid_Heat_Capacity_Const_A>
+ <Solid_Heat_Capacity_Const_B>1360.3</Solid_Heat_Capacity_Const_B>
+ <Solid_Heat_Capacity_Const_C>-12.153</Solid_Heat_Capacity_Const_C>
+ <Solid_Heat_Capacity_Const_D>0.051584</Solid_Heat_Capacity_Const_D>
+ <Solid_Heat_Capacity_Const_E>-7.6997E-05</Solid_Heat_Capacity_Const_E>
+ <Solid_Heat_Capacity_Tmax>216.58</Solid_Heat_Capacity_Tmax>
+ <Solid_Heat_Capacity_Tmin>25</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>-0.011629</Surface_Tension_Const_A>
+ <Surface_Tension_Const_B>-183.67</Surface_Tension_Const_B>
+ <Surface_Tension_Const_C>0.069773</Surface_Tension_Const_C>
+ <Surface_Tension_Const_D>-0.012408</Surface_Tension_Const_D>
+ <Surface_Tension_Const_E>-1.8232E-06</Surface_Tension_Const_E>
+ <Surface_Tension_Tmax>304.21</Surface_Tension_Tmax>
+ <Surface_Tension_Tmin>216.58</Surface_Tension_Tmin>
+ <SurfaceTensionEquation>16</SurfaceTensionEquation>
+ <TemperatureOfFusion>216.58</TemperatureOfFusion>
+ <UNIQUAC_Q>1.292</UNIQUAC_Q>
+ <UNIQUAC_R>1.2986</UNIQUAC_R>
+ <Vapor_Pressure_Constant_A>95.478</Vapor_Pressure_Constant_A>
+ <Vapor_Pressure_Constant_B>-4070</Vapor_Pressure_Constant_B>
+ <Vapor_Pressure_Constant_C>-12.07</Vapor_Pressure_Constant_C>
+ <Vapor_Pressure_Constant_D>2.9505E-05</Vapor_Pressure_Constant_D>
+ <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
+ <Vapor_Pressure_TMAX>304.21</Vapor_Pressure_TMAX>
+ <Vapor_Pressure_TMIN>216.4</Vapor_Pressure_TMIN>
+ <Vapor_Thermal_Conductivity_Const_A>5.804</Vapor_Thermal_Conductivity_Const_A>
+ <Vapor_Thermal_Conductivity_Const_B>-0.44522</Vapor_Thermal_Conductivity_Const_B>
+ <Vapor_Thermal_Conductivity_Const_C>794.13</Vapor_Thermal_Conductivity_Const_C>
+ <Vapor_Thermal_Conductivity_Const_D>2139600</Vapor_Thermal_Conductivity_Const_D>
+ <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
+ <Vapor_Thermal_Conductivity_Tmax>1500</Vapor_Thermal_Conductivity_Tmax>
+ <Vapor_Thermal_Conductivity_Tmin>180</Vapor_Thermal_Conductivity_Tmin>
+ <Vapor_Viscosity_Const_A>2.2464E-06</Vapor_Viscosity_Const_A>
+ <Vapor_Viscosity_Const_B>0.45495</Vapor_Viscosity_Const_B>
+ <Vapor_Viscosity_Const_C>292.64</Vapor_Viscosity_Const_C>
+ <Vapor_Viscosity_Const_D>1669.1</Vapor_Viscosity_Const_D>
+ <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
+ <Vapor_Viscosity_Tmax>1900</Vapor_Viscosity_Tmax>
+ <Vapor_Viscosity_Tmin>170</Vapor_Viscosity_Tmin>
+ <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+ <VaporPressureEquation>101</VaporPressureEquation>
+ <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
+ <VaporViscosityEquation>102</VaporViscosityEquation>
+ <Z_Rackett>0.270937</Z_Rackett>
+ <FullerDiffusionVolume>26.9</FullerDiffusionVolume>
+ <LennardJonesDiameter>4.011624E-10</LennardJonesDiameter>
+ <LennardJonesEnergy>187.9268</LennardJonesEnergy>
+ <Parachor>0.0132</Parachor>
+ <Tag></Tag>
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+ <COSTALD_Characteristic_Volume>0.104698</COSTALD_Characteristic_Volume>
+ <IsSolid>false</IsSolid>
+ <ChemSepFamily>24</ChemSepFamily>
+ <DynamicProperties />
+ <UNIFACGroups />
+ <MODFACGroups />
+ <NISTMODFACGroups />
+ <Elements>
+ <Item Name="C" Value="1" />
+ <Item Name="O" Value="2" />
+ </Elements>
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+ <Acentric_Factor>0.245381</Acentric_Factor>
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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>
+ <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>7446-09-5</CAS_Number>
+ <Chao_Seader_Acentricity>0.2462</Chao_Seader_Acentricity>
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+ <Chao_Seader_Solubility_Parameter>0.0029313330734</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
+ <CompCreatorStudyFile></CompCreatorStudyFile>
+ <Critical_Compressibility>0.269</Critical_Compressibility>
+ <Critical_Pressure>7884100</Critical_Pressure>
+ <Critical_Temperature>430.75</Critical_Temperature>
+ <Critical_Volume>0.122</Critical_Volume>
+ <CurrentDB>ChemSep</CurrentDB>
+ <Dipole_Moment>5.44E-30</Dipole_Moment>
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+ <Electrolyte_DelGF>0</Electrolyte_DelGF>
+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
+ <EnthalpyOfFusionAtTf>7.401</EnthalpyOfFusionAtTf>
+ <Formula>OSO</Formula>
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+ <HVap_B>1.8091</HVap_B>
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+ <HVap_D>2.2271</HVap_D>
+ <HVap_E>-0.64793</HVap_E>
+ <HVap_TMAX>430.75</HVap_TMAX>
+ <HVap_TMIN>197.67</HVap_TMIN>
+ <HydrationNumber>0</HydrationNumber>
+ <ID>910</ID>
+ <Ideal_Gas_Heat_Capacity_Const_A>33406</Ideal_Gas_Heat_Capacity_Const_A>
+ <Ideal_Gas_Heat_Capacity_Const_B>-516.38</Ideal_Gas_Heat_Capacity_Const_B>
+ <Ideal_Gas_Heat_Capacity_Const_C>10.524</Ideal_Gas_Heat_Capacity_Const_C>
+ <Ideal_Gas_Heat_Capacity_Const_D>1.3143E-05</Ideal_Gas_Heat_Capacity_Const_D>
+ <Ideal_Gas_Heat_Capacity_Const_E>-6.1535E-08</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>16</IdealgasCpEquation>
+ <IG_Enthalpy_of_Formation_25C>-4633.50597373244</IG_Enthalpy_of_Formation_25C>
+ <IG_Entropy_of_Formation_25C>0.171722156752365</IG_Entropy_of_Formation_25C>
+ <IG_Gibbs_Energy_of_Formation_25C>-4684.70493476815</IG_Gibbs_Energy_of_Formation_25C>
+ <InChI></InChI>
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+ <IsBlackOil>false</IsBlackOil>
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+ <IsHydratedSalt>false</IsHydratedSalt>
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+ <IsSalt>false</IsSalt>
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+ <Liquid_Density_Const_D>0.27051</Liquid_Density_Const_D>
+ <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
+ <Liquid_Density_Tmax>430.75</Liquid_Density_Tmax>
+ <Liquid_Density_Tmin>197.67</Liquid_Density_Tmin>
+ <Liquid_Heat_Capacity_Const_A>86911</Liquid_Heat_Capacity_Const_A>
+ <Liquid_Heat_Capacity_Const_B>53691</Liquid_Heat_Capacity_Const_B>
+ <Liquid_Heat_Capacity_Const_C>-599.94</Liquid_Heat_Capacity_Const_C>
+ <Liquid_Heat_Capacity_Const_D>2.2025</Liquid_Heat_Capacity_Const_D>
+ <Liquid_Heat_Capacity_Const_E>-0.0025885</Liquid_Heat_Capacity_Const_E>
+ <Liquid_Heat_Capacity_Tmax>350</Liquid_Heat_Capacity_Tmax>
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+ <Liquid_Thermal_Conductivity_Const_B>-2.2484</Liquid_Thermal_Conductivity_Const_B>
+ <Liquid_Thermal_Conductivity_Const_C>-0.50659</Liquid_Thermal_Conductivity_Const_C>
+ <Liquid_Thermal_Conductivity_Const_D>-0.0009424</Liquid_Thermal_Conductivity_Const_D>
+ <Liquid_Thermal_Conductivity_Const_E>-1.0218E-06</Liquid_Thermal_Conductivity_Const_E>
+ <Liquid_Thermal_Conductivity_Tmax>400</Liquid_Thermal_Conductivity_Tmax>
+ <Liquid_Thermal_Conductivity_Tmin>197.67</Liquid_Thermal_Conductivity_Tmin>
+ <Liquid_Viscosity_Const_A>50.887</Liquid_Viscosity_Const_A>
+ <Liquid_Viscosity_Const_B>-1574</Liquid_Viscosity_Const_B>
+ <Liquid_Viscosity_Const_C>-9.4517</Liquid_Viscosity_Const_C>
+ <Liquid_Viscosity_Const_D>1.5898E-07</Liquid_Viscosity_Const_D>
+ <Liquid_Viscosity_Const_E>2</Liquid_Viscosity_Const_E>
+ <LiquidDensityEquation>105</LiquidDensityEquation>
+ <LiquidHeatCapacityEquation>16</LiquidHeatCapacityEquation>
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+ <LiquidViscosityEquation>101</LiquidViscosityEquation>
+ <Molar_Weight>64.0638</Molar_Weight>
+ <MolarVolume_k1i>0</MolarVolume_k1i>
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+ <MolarVolume_v2i>0</MolarVolume_v2i>
+ <MolarVolume_v3i>0</MolarVolume_v3i>
+ <Name>Sulfur dioxide</Name>
+ <NBP>263.13</NBP>
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+ <Normal_Boiling_Point>263.13</Normal_Boiling_Point>
+ <OriginalDB>ChemSep</OriginalDB>
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+ <PositiveIon></PositiveIon>
+ <PositiveIonStoichCoeff>0</PositiveIonStoichCoeff>
+ <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
+ <SMILES>O=[S]=O</SMILES>
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+ <Solid_Density_Const_B>-0.018032</Solid_Density_Const_B>
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+ <Solid_Heat_Capacity_Const_B>1707.9</Solid_Heat_Capacity_Const_B>
+ <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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+ <SolidDensityAtTs>0</SolidDensityAtTs>
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+ <TemperatureOfFusion>200</TemperatureOfFusion>
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+ <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>
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+ <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>
+ <COSTALD_SRK_Acentric_Factor>0.256</COSTALD_SRK_Acentric_Factor>
+ <COSTALD_Characteristic_Volume>0.12522</COSTALD_Characteristic_Volume>
+ <IsSolid>false</IsSolid>
+ <ChemSepFamily>24</ChemSepFamily>
+ <DynamicProperties />
+ <UNIFACGroups />
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+ <NISTMODFACGroups />
+ <Elements>
+ <Item Name="O" Value="2" />
+ <Item Name="S" Value="1" />
+ </Elements>
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
+ <Acentric_Factor>0.550815</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>
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+ <BO_SGO>0</BO_SGO>
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+ <Chao_Seader_Solubility_Parameter>0.00760246818</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
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+ <Critical_Compressibility>0.284</Critical_Compressibility>
+ <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>
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+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
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+ <Formula>HOCH2CH2NH2</Formula>
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+ <Ideal_Gas_Heat_Capacity_Const_E>2.8656E-10</Ideal_Gas_Heat_Capacity_Const_E>
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+ <IG_Gibbs_Energy_of_Formation_25C>-1691.13934660793</IG_Gibbs_Energy_of_Formation_25C>
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+ <Name>Monoethanolamine</Name>
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+ <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
+ <Vapor_Viscosity_Tmin>283.65</Vapor_Viscosity_Tmin>
+ <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
+ <VaporPressureEquation>10</VaporPressureEquation>
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+ <VaporViscosityEquation>102</VaporViscosityEquation>
+ <Z_Rackett>0.266147</Z_Rackett>
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+ <Parachor>0.0284</Parachor>
+ <Tag></Tag>
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+ <COSTALD_Characteristic_Volume>0.20696</COSTALD_Characteristic_Volume>
+ <IsSolid>false</IsSolid>
+ <ChemSepFamily>68</ChemSepFamily>
+ <DynamicProperties />
+ <UNIFACGroups>
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+ </NISTMODFACGroups>
+ <Elements>
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+ <Item Name="O" Value="1" />
+ </Elements>
+ </Compound>
+ <Compound>
+ <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
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+ <BO_OilViscTemp2>0</BO_OilViscTemp2>
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+ <BO_SGG>0</BO_SGG>
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+ <CAS_Number>7727-37-9</CAS_Number>
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+ <Chao_Seader_Solubility_Parameter>0.00216918504124</Chao_Seader_Solubility_Parameter>
+ <Charge>0</Charge>
+ <ChemicalStructure></ChemicalStructure>
+ <Comments></Comments>
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+ <Critical_Compressibility>0.289</Critical_Compressibility>
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+ <Critical_Temperature>126.2</Critical_Temperature>
+ <Critical_Volume>0.0901</Critical_Volume>
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+ <Electrolyte_DelHF>0</Electrolyte_DelHF>
+ <EnthalpyOfFusionAtTf>0.72</EnthalpyOfFusionAtTf>
+ <Formula>N2</Formula>
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+ <Ideal_Gas_Heat_Capacity_Const_B>-2305.946</Ideal_Gas_Heat_Capacity_Const_B>
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+ <Ideal_Gas_Heat_Capacity_Const_E>1.706099E-07</Ideal_Gas_Heat_Capacity_Const_E>
+ <IdealgasCpEquation>16</IdealgasCpEquation>
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+ <IG_Gibbs_Energy_of_Formation_25C>0</IG_Gibbs_Energy_of_Formation_25C>
+ <InChI></InChI>
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+ <IsBlackOil>false</IsBlackOil>
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+ <Liquid_Heat_Capacity_Const_C>-0.9071</Liquid_Heat_Capacity_Const_C>
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+ <MolarVolume_v3i>0</MolarVolume_v3i>
+ <Name>Nitrogen</Name>
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+ <Normal_Boiling_Point>77.35</Normal_Boiling_Point>
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+ <SMILES>N#N</SMILES>
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+ <Solid_Heat_Capacity_Const_C>875.74</Solid_Heat_Capacity_Const_C>
+ <Solid_Heat_Capacity_Const_D>-11.589</Solid_Heat_Capacity_Const_D>
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+ <Solid_Heat_Capacity_Tmax>63</Solid_Heat_Capacity_Tmax>
+ <Solid_Heat_Capacity_Tmin>32.8</Solid_Heat_Capacity_Tmin>
+ <SolidDensityAtTs>0</SolidDensityAtTs>
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+ <StandardStateMolarVolume>0</StandardStateMolarVolume>
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+ <Surface_Tension_Const_A>-0.0025409</Surface_Tension_Const_A>
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+ <SurfaceTensionEquation>16</SurfaceTensionEquation>
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+ <Vapor_Pressure_Constant_D>7.97271E-05</Vapor_Pressure_Constant_D>
+ <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
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+ <Vapor_Pressure_TMIN>60.81</Vapor_Pressure_TMIN>
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+ <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>
+ <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>
+ <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;
+ &lt;Content ID="2" PersistString="DWSIM.WatchPanel" AutoHidePortion="0.152227705943669" IsHidden="True" IsFloat="False" /&gt;
+ &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;
+ &lt;Content ID="12" PersistString="DWSIM.Thermodynamics.MaterialStreamEditor" AutoHidePortion="450" IsHidden="False" IsFloat="False" /&gt;
+ &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;
+ &lt;Content ID="1" RefID="7" /&gt;
+ &lt;Content ID="2" RefID="4" /&gt;
+ &lt;Content ID="3" RefID="1" /&gt;
+ &lt;Content ID="4" RefID="8" /&gt;
+ &lt;Content ID="5" RefID="3" /&gt;
+ &lt;Content ID="6" RefID="9" /&gt;
+ &lt;/Contents&gt;
+ &lt;/Pane&gt;
+ &lt;Pane ID="1" DockState="DockBottom" ActiveContent="0"&gt;
+ &lt;Contents Count="1"&gt;
+ &lt;Content ID="0" RefID="0" /&gt;
+ &lt;/Contents&gt;
+ &lt;/Pane&gt;
+ &lt;Pane ID="2" DockState="DockBottom" ActiveContent="-1"&gt;
+ &lt;Contents Count="1"&gt;
+ &lt;Content ID="0" RefID="2" /&gt;
+ &lt;/Contents&gt;
+ &lt;/Pane&gt;
+ &lt;Pane ID="3" DockState="Float" ActiveContent="-1"&gt;
+ &lt;Contents Count="1"&gt;
+ &lt;Content ID="0" RefID="5" /&gt;
+ &lt;/Contents&gt;
+ &lt;/Pane&gt;
+ &lt;Pane ID="4" DockState="DockBottom" ActiveContent="-1"&gt;
+ &lt;Contents Count="1"&gt;
+ &lt;Content ID="0" RefID="5" /&gt;
+ &lt;/Contents&gt;
+ &lt;/Pane&gt;
+ &lt;Pane ID="5" DockState="DockLeft" ActiveContent="13"&gt;
+ &lt;Contents Count="4"&gt;
+ &lt;Content ID="0" RefID="10" /&gt;
+ &lt;Content ID="1" RefID="11" /&gt;
+ &lt;Content ID="2" RefID="12" /&gt;
+ &lt;Content ID="3" RefID="13" /&gt;
+ &lt;/Contents&gt;
+ &lt;/Pane&gt;
+ &lt;/Panes&gt;
+ &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;
+ &lt;/NestedPanes&gt;
+ &lt;/DockWindow&gt;
+ &lt;DockWindow ID="1" DockState="DockLeft" ZOrderIndex="3"&gt;
+ &lt;NestedPanes Count="1"&gt;
+ &lt;Pane ID="0" RefID="5" PrevPane="-1" Alignment="Bottom" Proportion="0.5" /&gt;
+ &lt;/NestedPanes&gt;
+ &lt;/DockWindow&gt;
+ &lt;DockWindow ID="2" DockState="DockRight" ZOrderIndex="4"&gt;
+ &lt;NestedPanes Count="0" /&gt;
+ &lt;/DockWindow&gt;
+ &lt;DockWindow ID="3" DockState="DockTop" ZOrderIndex="5"&gt;
+ &lt;NestedPanes Count="0" /&gt;
+ &lt;/DockWindow&gt;
+ &lt;DockWindow ID="4" DockState="DockBottom" ZOrderIndex="2"&gt;
+ &lt;NestedPanes Count="3"&gt;
+ &lt;Pane ID="0" RefID="1" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
+ &lt;Pane ID="1" RefID="4" PrevPane="1" Alignment="Top" Proportion="0.5" /&gt;
+ &lt;Pane ID="2" RefID="2" PrevPane="1" Alignment="Right" Proportion="0.261838440111421" /&gt;
+ &lt;/NestedPanes&gt;
+ &lt;/DockWindow&gt;
+ &lt;/DockWindows&gt;
+ &lt;FloatWindows Count="1"&gt;
+ &lt;FloatWindow ID="0" Bounds="336, 370, 900, 155" ZOrderIndex="0"&gt;
+ &lt;NestedPanes Count="1"&gt;
+ &lt;Pane ID="0" RefID="3" PrevPane="-1" Alignment="Right" Proportion="0.5" /&gt;
+ &lt;/NestedPanes&gt;
+ &lt;/FloatWindow&gt;
+ &lt;/FloatWindows&gt;
+&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
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generated by cgit (git 2.34.1) at 2024-12-19 09:59:28 +0000