diff options
| author | Sashi20 | 2022-03-16 00:20:09 +0550 |
|---|---|---|
| committer | Sashi20 | 2022-03-16 00:20:09 +0550 |
| commit | 4520fe5c33ef40d41b945c3f591a2a0e8d5e5678 (patch) | |
| tree | b58f0a3b6f0c3d0914dfe0ca1986b908a230269b | |
| parent | f4612288707890d9bf0a1029e106c676b93eb5e1 (diff) | |
| download | DWSIM-Flowsheets-4520fe5c33ef40d41b945c3f591a2a0e8d5e5678.tar.gz DWSIM-Flowsheets-4520fe5c33ef40d41b945c3f591a2a0e8d5e5678.tar.bz2 DWSIM-Flowsheets-4520fe5c33ef40d41b945c3f591a2a0e8d5e5678.zip | |
Added(A)/Deleted(D) following Flowsheet file
A Air_Liquefaction_Using_Linde_Single_Column_System_By_Mr_Srivatsa_Varadarajan/README.txt
R Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Abstract_AmmoniumChloride.pdf -> Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Abstract_AmmoniumChloride_.pdf
D Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Flowsheet__Production_of_AmmoniumChloride.dwxml
A Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Flowsheet__Production_of_AmmoniumChloride_.dwxmz
R "Ethanol_Extractive\r\nDistillation_With_Mixed_Glycols\r\nAs_Separating_Agent_By_Mr_Himanshu_Khadatkar/Abtract_EthanolExtractiveDistillation.pdf" -> Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Abstract.pdf
R "Ethanol_Extractive\r\nDistillation_With_Mixed_Glycols\r\nAs_Separating_Agent_By_Mr_Himanshu_Khadatkar/Flowsheet_EthanolExtractiveDistillation.dwxmz" -> Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/Flowsheet.dwxmz
A Ethanol_Extractive_Distillation_With_Mixed_Glycols_As_Separating_Agent_By_Mr_Himanshu_Khadatkar/README.txt
A Heterogeneous_Azeotropic_Distillation_Conventional_Had_For_Dehydration_Of_Tert_Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/ABSTRACT.pdf
A Heterogeneous_Azeotropic_Distillation_Conventional_Had_For_Dehydration_Of_Tert_Butanol_By_Mr_Richard_Carlos_Rojas_Quintero/Flowsheet.dwxmz
A Production_Of_Nitric_Acid_By_Ms_Vaishnavi_Tripathi/ABSTRACT.pdf
A Production_Of_Nitric_Acid_By_Ms_Vaishnavi_Tripathi/flowsheet.dwxmz
A Psd_For_Separating_Ternary_Systems_With_Three_Binary_Minimum_Azeotropes_Thf,_Water,_And_Ethanol_By_Mr_Hrithik_Seth/README.txt
R Pressure_Swing_Distillation_For_Separating_Ternary_Systems_With_Three_Binary_Minimum_Azeotropes_Thf_Water_And_Ethanol_By_Mr_Hrithik_Seth/abstract.pdf -> Psd_For_Separating_Ternary_Systems_With_Three_Binary_Minimum_Azeotropes_Thf,_Water,_And_Ethanol_By_Mr_Hrithik_Seth/abstract.pdf
R Pressure_Swing_Distillation_For_Separating_Ternary_Systems_With_Three_Binary_Minimum_Azeotropes_Thf_Water_And_Ethanol_By_Mr_Hrithik_Seth/flowsheet.dwxmz -> Psd_For_Separating_Ternary_Systems_With_Three_Binary_Minimum_Azeotropes_Thf,_Water,_And_Ethanol_By_Mr_Hrithik_Seth/flowsheet.dwxmz
A Rectisol_Wash_Process_For_Removal_Of_H2s_And_Co2_From_Sour_Syngas_By_Mr_Vengdhanathan_S/Abstract.pdf
A Rectisol_Wash_Process_For_Removal_Of_H2s_And_Co2_From_Sour_Syngas_By_Mr_Vengdhanathan_S/Flowsheet.dwxmz
A Triple_Effect_Evaporation_Of_Saline_Solution_By_Ms_Yutika_Naik/README.txt
17 files changed, 32 insertions, 20413 deletions
diff --git a/Air_Liquefaction_Using_Linde_Single_Column_System_By_Mr_Srivatsa_Varadarajan/README.txt b/Air_Liquefaction_Using_Linde_Single_Column_System_By_Mr_Srivatsa_Varadarajan/README.txt new file mode 100644 index 0000000..3300479 --- /dev/null +++ b/Air_Liquefaction_Using_Linde_Single_Column_System_By_Mr_Srivatsa_Varadarajan/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Air Liquefaction using Linde Single Column System +Proposar Name: Mr Srivatsa Varadarajan +University: Sastra Deemed University, Thanjavur + + +DWSIM Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Abstract_AmmoniumChloride.pdf b/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Abstract_AmmoniumChloride_.pdf Binary files differindex 2d862ea..a4ec35f 100644 --- a/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Abstract_AmmoniumChloride.pdf +++ b/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Abstract_AmmoniumChloride_.pdf diff --git a/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Flowsheet__Production_of_AmmoniumChloride.dwxml b/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Flowsheet__Production_of_AmmoniumChloride.dwxml deleted file mode 100644 index 242d532..0000000 --- a/Ammonium_Chloride_Production_From_Ammonia_By_Mr_V.p_Sudharsanarajan/Flowsheet__Production_of_AmmoniumChloride.dwxml +++ /dev/null @@ -1,20413 +0,0 @@ -<?xml version="1.0" encoding="utf-8"?>
-<DWSIM_Simulation_Data>
- <GeneralInfo>
- <BuildVersion>7.3.2.0</BuildVersion>
- <BuildDate>2000-01-03T00:00:00</BuildDate>
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- <SavedOn>2022-02-22T12:51:49.7281494-05:00</SavedOn>
- <SavedFromClassicUI>true</SavedFromClassicUI>
- </GeneralInfo>
- <SimulationObjects>
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- <Type>DWSIM.UnitOperations.Streams.EnergyStream</Type>
- <ObjectClass>Streams</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <ComponentDescription>CorrentedeEnergia</ComponentDescription>
- <ComponentName>EN-afd714fd-79ad-4f2b-95d5-c95c5f1b2e4a</ComponentName>
- <MobileCompatible>true</MobileCompatible>
- <Name2>EN-afd714fd-79ad-4f2b-95d5-c95c5f1b2e4a</Name2>
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- <ProductAuthor>Daniel Medeiros</ProductAuthor>
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- <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
- <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
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- <TotalEnergyFlow>-10419.8050390665</TotalEnergyFlow>
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- <ReferenceSolvent></ReferenceSolvent>
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- <EditorState>{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0}</EditorState>
- <MobileCompatible>true</MobileCompatible>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
- <IsFunctional>true</IsFunctional>
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- <Type>DWSIM.Thermodynamics.BaseClasses.Compound</Type>
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- <ComponentName>Ammonia</ComponentName>
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- <PetroleumFraction>false</PetroleumFraction>
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- <Type>DWSIM.UnitOperations.UnitOperations.Vessel</Type>
- <ObjectClass>Separators</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>true</HasPropertiesForDynamicMode>
- <DimensionRatio>3</DimensionRatio>
- <SurgeFactor>1.2</SurgeFactor>
- <ResidenceTime>5</ResidenceTime>
- <PressureCalculation>Maximum</PressureCalculation>
- <OverrideT>false</OverrideT>
- <OverrideP>false</OverrideP>
- <FlashPressure>101325</FlashPressure>
- <FlashTemperature>298.15</FlashTemperature>
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- <MobileCompatible>true</MobileCompatible>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
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- <ErrorMessage></ErrorMessage>
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- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>SEP-d75ea10b-32ae-46df-b0e7-39ba0e55894c</Name>
- <ProductName>Gas-Liquid Separator</ProductName>
- <ProductDescription>Fluid phase separator (vapor/liquid)</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
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- <DynamicProperties>
- <Property>
- <Name>Vessel Orientation</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>0.0</Data>
- </Property>
- <Property>
- <Name>Operating Pressure</Name>
- <PropertyType>System.Double</PropertyType>
- <Data>0.0</Data>
- </Property>
- <Property>
- <Name>Liquid Level</Name>
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- </Property>
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- <Name>Volume</Name>
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- <DynamicPropertiesDescriptions>
- <Property>
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- <Data>"Vertical or Horizontal (V = 0, H = 1)"</Data>
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- <Property>
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- <PropertyType>System.String</PropertyType>
- <Data>"Current Vessel Operating Pressure"</Data>
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- <Data>"Minimum Dynamic Pressure for this Unit Operation."</Data>
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- <PropertyType>System.String</PropertyType>
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- </Property>
- <Property>
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- <PropertyType>System.String</PropertyType>
- <Data>"Empties the vessel's content on the next run."</Data>
- </Property>
- </DynamicPropertiesDescriptions>
- <DynamicPropertiesUnitTypes>
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- <Name>Reset Content</Name>
- <PropertyType>System.Int64</PropertyType>
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- </Property>
- </DynamicPropertiesUnitTypes>
- <AttachedUtilities />
- <PropertyPackage>PP-e6c896a7-bd6e-4d09-bfc9-d053037ad124</PropertyPackage>
- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
- <ObjectClass>Streams</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <OverrideSingleCompoundFlashBehavior>false</OverrideSingleCompoundFlashBehavior>
- <FloatingTableAmountBasis>DefaultBasis</FloatingTableAmountBasis>
- <DefinedFlow>Mass</DefinedFlow>
- <ForcePhase>GlobalDef</ForcePhase>
- <TotalEnergyFlow>-3.08315926191323E-06</TotalEnergyFlow>
- <AtEquilibrium>true</AtEquilibrium>
- <ComponentDescription>CorrentedeMatria</ComponentDescription>
- <ComponentName>MAT-3f114881-a0e9-4dde-89bd-3b1cb855595e</ComponentName>
- <Name2>MAT-3f114881-a0e9-4dde-89bd-3b1cb855595e</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}</EditorState>
- <MobileCompatible>true</MobileCompatible>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
- <StoreDetailedDebugReport>false</StoreDetailedDebugReport>
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- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>02/22/2022 12:51:34</LastUpdated>
- <ErrorMessage></ErrorMessage>
- <Annotation></Annotation>
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- <AttachedAdjustId></AttachedAdjustId>
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- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>MAT-3f114881-a0e9-4dde-89bd-3b1cb855595e</Name>
- <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>
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- <DynamicPropertiesDescriptions />
- <DynamicPropertiesUnitTypes />
- <AttachedUtilities />
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- <Phases>
- <Phase>
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- <Compounds>
- <Compound>
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- </Compound>
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- </Compound>
- <Compound>
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Mixture</ComponentName>
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- <Properties>
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- <ComponentName>Ammonium Chloride</ComponentName>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Vapor</ComponentName>
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- <compressibilityFactor>0.99214826871834</compressibilityFactor>
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- <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>Hydrogen chloride</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>Hydrogen chloride</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0</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>Ammonium Chloride</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>Ammonium Chloride</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</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>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>
- <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>Ammonia</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonia</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</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>Hydrogen chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Hydrogen chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</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>Ammonium Chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonium Chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</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>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>
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- <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>Ammonia</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonia</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</PartialVolume>
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- <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>Hydrogen chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Hydrogen chloride</Name>
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- <PartialVolume>0</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>Ammonium Chloride</ComponentName>
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- <PetroleumFraction>false</PetroleumFraction>
- <Molarity>0</Molarity>
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- <MassFlow>0</MassFlow>
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- <DynamicProperties />
- </Compound>
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
- <ComponentDescription></ComponentDescription>
- <ComponentName>Aqueous</ComponentName>
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- <Name>Aqueous</Name>
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- <Properties>
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- </Properties>
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- <Phase>
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- <Compound>
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- <ComponentName>Ammonia</ComponentName>
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- <FugacityCoeff>NaN</FugacityCoeff>
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- <Name>Ammonia</Name>
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- <DynamicProperties />
- </Compound>
- <Compound>
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- <ComponentName>Hydrogen chloride</ComponentName>
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- <FugacityCoeff>NaN</FugacityCoeff>
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- <Name>Hydrogen chloride</Name>
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- <DynamicProperties />
- </Compound>
- <Compound>
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- <ComponentName>Ammonium Chloride</ComponentName>
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- <DynamicProperties />
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- <Properties>DWSIM.Thermodynamics.BaseClasses.PhaseProperties</Properties>
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- </Properties>
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- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.Heater</Type>
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- <ExternalSolverID></ExternalSolverID>
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- <ComponentDescription>Aquecedor</ComponentDescription>
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- <Property>
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- <Property>
- <Name>Volume</Name>
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- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.Double</PropertyType>
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- <Property>
- <Name>Initialize using Inlet Stream</Name>
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- <Name>Reset Content</Name>
- <PropertyType>System.Double</PropertyType>
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- </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>System.Int64</PropertyType>
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- <AttachedUtilities />
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- <SimulationObject>
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- <SimulationObject>
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- <SimulationObject>
- <Type>DWSIM.Thermodynamics.Streams.MaterialStream</Type>
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- <MolarFlow>0</MolarFlow>
- <Name>Hydrogen chloride</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0</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>Ammonium Chloride</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>Ammonium Chloride</Name>
- <PartialPressure>NaN</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</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>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>
- <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>Ammonia</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonia</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</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>Hydrogen chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Hydrogen chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</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>Ammonium Chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonium Chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</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>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>Ammonia</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonia</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</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>Hydrogen chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Hydrogen chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</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>Ammonium Chloride</ComponentName>
- <ActivityCoeff>0</ActivityCoeff>
- <PetroleumFraction>false</PetroleumFraction>
- <MassFraction>0</MassFraction>
- <MoleFraction>0</MoleFraction>
- <Molarity>0</Molarity>
- <Molality>0</Molality>
- <FugacityCoeff>0</FugacityCoeff>
- <Kvalue>0</Kvalue>
- <lnKvalue>0</lnKvalue>
- <MassFlow>0</MassFlow>
- <MolarFlow>0</MolarFlow>
- <Name>Ammonium Chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</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>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>
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- <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>Ammonia</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>Ammonia</Name>
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- <PartialVolume>0</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>Hydrogen chloride</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>Hydrogen chloride</Name>
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- <PartialVolume>0</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>Ammonium Chloride</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>Ammonium Chloride</Name>
- <PartialPressure>0</PartialPressure>
- <PartialVolume>0</PartialVolume>
- <VolumetricFlow>0</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>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>1</OutletVaporFraction>
- <OutletTemperature>303.15</OutletTemperature>
- <CalcMode>OutletTemperature</CalcMode>
- <DeltaT>-3.68433620678843E-06</DeltaT>
- <DeltaQ>-1.12590038676139E-06</DeltaQ>
- <MobileCompatible>true</MobileCompatible>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>Aquecedor</ComponentDescription>
- <ComponentName>AQ-d209f95e-a899-419c-acf7-2cc549646b3e</ComponentName>
- <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>02/22/2022 12:51:34</LastUpdated>
- <ErrorMessage></ErrorMessage>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
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- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>AQ-d209f95e-a899-419c-acf7-2cc549646b3e</Name>
- <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>7.3.2.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <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>System.Int64</PropertyType>
- <Data>67</Data>
- </Property>
- <Property>
- <Name>Volume</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>63</Data>
- </Property>
- <Property>
- <Name>Minimum Pressure</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>46</Data>
- </Property>
- <Property>
- <Name>Initialize using Inlet Stream</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>66</Data>
- </Property>
- <Property>
- <Name>Reset Content</Name>
- <PropertyType>System.Int64</PropertyType>
- <Data>66</Data>
- </Property>
- </DynamicPropertiesUnitTypes>
- <AttachedUtilities />
- <PropertyPackage>PP-e6c896a7-bd6e-4d09-bfc9-d053037ad124</PropertyPackage>
- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.ComponentSeparator</Type>
- <ObjectClass>Separators</ObjectClass>
- <SpecifiedStreamIndex>0</SpecifiedStreamIndex>
- <EnergyImb>1.31443470168174E-06</EnergyImb>
- <MobileCompatible>true</MobileCompatible>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>ComponentSeparator</ComponentDescription>
- <ComponentName>CS-b42e8555-3e06-4492-b40f-c59f7a78894c</ComponentName>
- <DynamicsSpec>Pressure</DynamicsSpec>
- <DynamicsOnly>false</DynamicsOnly>
- <Visible>true</Visible>
- <OverrideCalculationRoutine>false</OverrideCalculationRoutine>
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- <IsFunctional>true</IsFunctional>
- <SupportsDynamicMode>false</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <PreferredFlashAlgorithmTag></PreferredFlashAlgorithmTag>
- <Calculated>true</Calculated>
- <DebugMode>false</DebugMode>
- <LastUpdated>02/22/2022 12:51:34</LastUpdated>
- <ErrorMessage></ErrorMessage>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>CS-b42e8555-3e06-4492-b40f-c59f7a78894c</Name>
- <ProductName>Compound Separator</ProductName>
- <ProductDescription>Model for a hypothetical compound separation process</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>7.3.2.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <DynamicProperties />
- <DynamicPropertiesDescriptions />
- <DynamicPropertiesUnitTypes />
- <AttachedUtilities />
- <PropertyPackage>PP-e6c896a7-bd6e-4d09-bfc9-d053037ad124</PropertyPackage>
- <SeparationSpecs>
- <SeparationSpec ID="Ammonia" CompID="Ammonia" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="0" />
- <SeparationSpec ID="Hydrogen chloride" CompID="Hydrogen chloride" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="0" />
- <SeparationSpec ID="Ammonium Chloride" CompID="Ammonium Chloride" SepSpec="PercentInletMassFlow" SpecUnit="%" SpecValue="100" />
- </SeparationSpecs>
- </SimulationObject>
- <SimulationObject>
- <Type>DWSIM.UnitOperations.UnitOperations.Mixer</Type>
- <ObjectClass>MixersSplitters</ObjectClass>
- <SupportsDynamicMode>true</SupportsDynamicMode>
- <HasPropertiesForDynamicMode>false</HasPropertiesForDynamicMode>
- <PressureCalculation>Average</PressureCalculation>
- <MobileCompatible>true</MobileCompatible>
- <ExternalSolverID></ExternalSolverID>
- <ExternalSolverConfigData></ExternalSolverConfigData>
- <ComponentDescription>Misturador</ComponentDescription>
- <ComponentName>MIST-e1a341e2-fcb1-4c98-9376-49c8d646aefa</ComponentName>
- <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>02/22/2022 12:51:34</LastUpdated>
- <ErrorMessage></ErrorMessage>
- <Annotation></Annotation>
- <IsAdjustAttached>false</IsAdjustAttached>
- <AttachedAdjustId></AttachedAdjustId>
- <AdjustVarType>Manipulated</AdjustVarType>
- <IsSpecAttached>false</IsSpecAttached>
- <AttachedSpecId></AttachedSpecId>
- <SpecVarType>Source</SpecVarType>
- <Name>MIST-e1a341e2-fcb1-4c98-9376-49c8d646aefa</Name>
- <ProductName>Stream Mixer</ProductName>
- <ProductDescription>Mixes multiple Material Streams into a single one</ProductDescription>
- <ProductAuthor>Daniel Medeiros</ProductAuthor>
- <ProductContactInfo>https://dwsim.inforside.com.br</ProductContactInfo>
- <ProductPage>https://dwsim.inforside.com.br</ProductPage>
- <ProductVersion>7.3.2.0</ProductVersion>
- <ProductAssembly>DWSIM.SharedClasses</ProductAssembly>
- <DynamicProperties />
- <DynamicPropertiesDescriptions />
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- <surfaceTension>NaN</surfaceTension>
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- <Compound>
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- <Compound>
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- <Compound>
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- <ComponentDescription></ComponentDescription>
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- <Compound>
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- <ComponentDescription></ComponentDescription>
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- </Compound>
- <Compound>
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- <ComponentDescription></ComponentDescription>
- <ComponentName>Hydrogen chloride</ComponentName>
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- <PartialVolume>6.52607187587008E-05</PartialVolume>
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- </Compound>
- <Compound>
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- <ComponentDescription></ComponentDescription>
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- <ComponentDescription></ComponentDescription>
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- <DynamicProperties />
- </Compound>
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-Temperature Difference 0.254397 -92.0489 K.
-Outlet Pressure 100000 100000 Pa
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- <Shape>0</Shape>
- <ShapeOverride>DefaultShape</ShapeOverride>
- <Status>NotCalculated</Status>
- <AutoSize>true</AutoSize>
- <Height>180</Height>
- <IsConnector>false</IsConnector>
- <Name>MASTERTABLE-20161365-174e-4a22-92d1-76100144c470</Name>
- <Tag></Tag>
- <Width>250</Width>
- <X>315.0616</X>
- <Y>345.8109</Y>
- <Selected>false</Selected>
- <Rotation>0</Rotation>
- <DrawMode>0</DrawMode>
- <InputConnectors />
- <OutputConnectors />
- <EnergyConnector>
- <Connector IsAttached="false" />
- </EnergyConnector>
- <SpecialConnectors />
- <Objects>
- <EXP-01>true</EXP-01>
- <EXP-02>true</EXP-02>
- </Objects>
- <Properties>
- <PROP_TU_0>true</PROP_TU_0>
- <PROP_TU_1>true</PROP_TU_1>
- <PROP_TU_2>true</PROP_TU_2>
- <PROP_TU_3>false</PROP_TU_3>
- <PROP_TU_4>true</PROP_TU_4>
- <PolytropicEfficiency>true</PolytropicEfficiency>
- <AdiabaticCoefficient>true</AdiabaticCoefficient>
- <PolytropicCoefficient>true</PolytropicCoefficient>
- <AdiabaticHead>false</AdiabaticHead>
- <PolytropicHead>false</PolytropicHead>
- <RotationSpeed>true</RotationSpeed>
- </Properties>
- <SortableItems>
- <SortableItem>Name | ASC</SortableItem>
- <SortableItem>Name | DESC</SortableItem>
- <SortableItem>Pressure Drop | ASC</SortableItem>
- <SortableItem>Pressure Drop | DESC</SortableItem>
- <SortableItem>Adiabatic Efficiency | ASC</SortableItem>
- <SortableItem>Adiabatic Efficiency | DESC</SortableItem>
- <SortableItem>Temperature Difference | ASC</SortableItem>
- <SortableItem>Temperature Difference | DESC</SortableItem>
- <SortableItem>Outlet Pressure | ASC</SortableItem>
- <SortableItem>Outlet Pressure | DESC</SortableItem>
- <SortableItem>Polytropic Efficiency | ASC</SortableItem>
- <SortableItem>Polytropic Efficiency | DESC</SortableItem>
- <SortableItem>Adiabatic Coefficient | ASC</SortableItem>
- <SortableItem>Adiabatic Coefficient | DESC</SortableItem>
- <SortableItem>Polytropic Coefficient | ASC</SortableItem>
- <SortableItem>Polytropic Coefficient | DESC</SortableItem>
- <SortableItem>Rotation Speed | ASC</SortableItem>
- <SortableItem>Rotation Speed | DESC</SortableItem>
- <SortableItem>Custom</SortableItem>
- </SortableItems>
- </GraphicObject>
- </GraphicObjects>
- <PropertyPackages>
- <PropertyPackage>
- <ID>PP-e6c896a7-bd6e-4d09-bfc9-d053037ad124</ID>
- <Type>DWSIM.Thermodynamics.PropertyPackages.PengRobinsonPropertyPackage</Type>
- <ComponentName>Peng-Robinson (PR)</ComponentName>
- <ComponentDescription>Property Package that uses the Peng-Robinson Cubic Equation of State. Recommended for use with hydrocarbons and non-condensables.</ComponentDescription>
- <Tag>Peng-Robinson (PR) (1)</Tag>
- <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>LeeKesler</EnthalpyEntropyCpCvCalculationMode>
- <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 />
- <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="True" />
- </FlashSettings>
- </PropertyPackage>
- </PropertyPackages>
- <Compounds>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
- <Acentric_Factor>0.256</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>7664-41-7</CAS_Number>
- <Chao_Seader_Acentricity>0.2517</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>24.9801</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0.0069802504654</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
- <CompCreatorStudyFile></CompCreatorStudyFile>
- <Critical_Compressibility>0.255</Critical_Compressibility>
- <Critical_Pressure>11353000</Critical_Pressure>
- <Critical_Temperature>405.4</Critical_Temperature>
- <Critical_Volume>0.07247</Critical_Volume>
- <CurrentDB>ChemSep</CurrentDB>
- <Dipole_Moment>4.9E-30</Dipole_Moment>
- <Electrolyte_Cp0>0</Electrolyte_Cp0>
- <Electrolyte_DelGF>0</Electrolyte_DelGF>
- <Electrolyte_DelHF>0</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>5.657</EnthalpyOfFusionAtTf>
- <Formula>NH3</Formula>
- <HVap_A>24542000</HVap_A>
- <HVap_B>-1.3178</HVap_B>
- <HVap_C>4.7194</HVap_C>
- <HVap_D>-5.4808</HVap_D>
- <HVap_E>2.4196</HVap_E>
- <HVap_TMAX>403.15</HVap_TMAX>
- <HVap_TMIN>195.41</HVap_TMIN>
- <HydrationNumber>0</HydrationNumber>
- <ID>1911</ID>
- <Ideal_Gas_Heat_Capacity_Const_A>33239</Ideal_Gas_Heat_Capacity_Const_A>
- <Ideal_Gas_Heat_Capacity_Const_B>-913.64</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>10.802</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>0.00021047</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>-4.1739E-08</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>16</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-2695.04395637949</IG_Enthalpy_of_Formation_25C>
- <IG_Entropy_of_Formation_25C>-5.80938085215286</IG_Entropy_of_Formation_25C>
- <IG_Gibbs_Energy_of_Formation_25C>-962.977055310114</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>4.0518</Liquid_Density_Const_A>
- <Liquid_Density_Const_B>0.27129</Liquid_Density_Const_B>
- <Liquid_Density_Const_C>405.4</Liquid_Density_Const_C>
- <Liquid_Density_Const_D>0.31349</Liquid_Density_Const_D>
- <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
- <Liquid_Density_Tmax>405.15</Liquid_Density_Tmax>
- <Liquid_Density_Tmin>195</Liquid_Density_Tmin>
- <Liquid_Heat_Capacity_Const_A>77659</Liquid_Heat_Capacity_Const_A>
- <Liquid_Heat_Capacity_Const_B>-45330</Liquid_Heat_Capacity_Const_B>
- <Liquid_Heat_Capacity_Const_C>445.74</Liquid_Heat_Capacity_Const_C>
- <Liquid_Heat_Capacity_Const_D>-1.4197</Liquid_Heat_Capacity_Const_D>
- <Liquid_Heat_Capacity_Const_E>0.0015508</Liquid_Heat_Capacity_Const_E>
- <Liquid_Heat_Capacity_Tmax>401.15</Liquid_Heat_Capacity_Tmax>
- <Liquid_Heat_Capacity_Tmin>195.45</Liquid_Heat_Capacity_Tmin>
- <Liquid_Thermal_Conductivity_Const_A>-0.95309</Liquid_Thermal_Conductivity_Const_A>
- <Liquid_Thermal_Conductivity_Const_B>14.684</Liquid_Thermal_Conductivity_Const_B>
- <Liquid_Thermal_Conductivity_Const_C>0.56768</Liquid_Thermal_Conductivity_Const_C>
- <Liquid_Thermal_Conductivity_Const_D>-0.00028968</Liquid_Thermal_Conductivity_Const_D>
- <Liquid_Thermal_Conductivity_Const_E>-1.9238E-06</Liquid_Thermal_Conductivity_Const_E>
- <Liquid_Thermal_Conductivity_Tmax>400.05</Liquid_Thermal_Conductivity_Tmax>
- <Liquid_Thermal_Conductivity_Tmin>195.41</Liquid_Thermal_Conductivity_Tmin>
- <Liquid_Viscosity_Const_A>-39.742</Liquid_Viscosity_Const_A>
- <Liquid_Viscosity_Const_B>1486.5</Liquid_Viscosity_Const_B>
- <Liquid_Viscosity_Const_C>4.7749</Liquid_Viscosity_Const_C>
- <Liquid_Viscosity_Const_D>-1.5796E-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>17.03052</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>Ammonia</Name>
- <NegativeIon></NegativeIon>
- <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
- <Normal_Boiling_Point>239.82</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>N</SMILES>
- <Solid_Density_Const_A>47.973</Solid_Density_Const_A>
- <Solid_Density_Const_B>-1.0295E-08</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>203.65</Solid_Density_Tmax>
- <Solid_Density_Tmin>194.15</Solid_Density_Tmin>
- <Solid_Heat_Capacity_Const_A>-5983.8</Solid_Heat_Capacity_Const_A>
- <Solid_Heat_Capacity_Const_B>380.66</Solid_Heat_Capacity_Const_B>
- <Solid_Heat_Capacity_Const_C>-0.59542</Solid_Heat_Capacity_Const_C>
- <Solid_Heat_Capacity_Const_D>-0.00029099</Solid_Heat_Capacity_Const_D>
- <Solid_Heat_Capacity_Const_E>4.9048E-06</Solid_Heat_Capacity_Const_E>
- <Solid_Heat_Capacity_Tmax>190</Solid_Heat_Capacity_Tmax>
- <Solid_Heat_Capacity_Tmin>20</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>-0.01195</Surface_Tension_Const_A>
- <Surface_Tension_Const_B>209.99</Surface_Tension_Const_B>
- <Surface_Tension_Const_C>-5.1813</Surface_Tension_Const_C>
- <Surface_Tension_Const_D>0.011762</Surface_Tension_Const_D>
- <Surface_Tension_Const_E>-2.7715E-05</Surface_Tension_Const_E>
- <Surface_Tension_Tmax>405.55</Surface_Tension_Tmax>
- <Surface_Tension_Tmin>195.41</Surface_Tension_Tmin>
- <SurfaceTensionEquation>16</SurfaceTensionEquation>
- <TemperatureOfFusion>195.41</TemperatureOfFusion>
- <UNIQUAC_Q>0.98</UNIQUAC_Q>
- <UNIQUAC_R>0.9097</UNIQUAC_R>
- <Vapor_Pressure_Constant_A>62.8849</Vapor_Pressure_Constant_A>
- <Vapor_Pressure_Constant_B>-4136.862</Vapor_Pressure_Constant_B>
- <Vapor_Pressure_Constant_C>-6.320663</Vapor_Pressure_Constant_C>
- <Vapor_Pressure_Constant_D>9.203947E-06</Vapor_Pressure_Constant_D>
- <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
- <Vapor_Pressure_TMAX>406.05</Vapor_Pressure_TMAX>
- <Vapor_Pressure_TMIN>191.24</Vapor_Pressure_TMIN>
- <Vapor_Thermal_Conductivity_Const_A>1.6165E-05</Vapor_Thermal_Conductivity_Const_A>
- <Vapor_Thermal_Conductivity_Const_B>1.3146</Vapor_Thermal_Conductivity_Const_B>
- <Vapor_Thermal_Conductivity_Const_C>75.168</Vapor_Thermal_Conductivity_Const_C>
- <Vapor_Thermal_Conductivity_Const_D>-8202.1</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>200</Vapor_Thermal_Conductivity_Tmin>
- <Vapor_Viscosity_Const_A>4.59E-08</Vapor_Viscosity_Const_A>
- <Vapor_Viscosity_Const_B>0.96936</Vapor_Viscosity_Const_B>
- <Vapor_Viscosity_Const_C>48.366</Vapor_Viscosity_Const_C>
- <Vapor_Viscosity_Const_D>-2671.4</Vapor_Viscosity_Const_D>
- <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
- <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
- <Vapor_Viscosity_Tmin>194.6</Vapor_Viscosity_Tmin>
- <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
- <VaporPressureEquation>101</VaporPressureEquation>
- <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
- <VaporViscosityEquation>102</VaporViscosityEquation>
- <Z_Rackett>0</Z_Rackett>
- <FullerDiffusionVolume>20.7</FullerDiffusionVolume>
- <LennardJonesDiameter>3.15E-10</LennardJonesDiameter>
- <LennardJonesEnergy>358</LennardJonesEnergy>
- <Parachor>0.0108</Parachor>
- <Tag></Tag>
- <COSTALD_SRK_Acentric_Factor>0.26199</COSTALD_SRK_Acentric_Factor>
- <COSTALD_Characteristic_Volume>0.07011</COSTALD_Characteristic_Volume>
- <DynamicProperties />
- <UNIFACGroups />
- <MODFACGroups />
- <NISTMODFACGroups />
- <Elements>
- <Item Name="H" Value="3" />
- <Item Name="N" Value="1" />
- </Elements>
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
- <Acentric_Factor>0.126</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>7647-01-0</CAS_Number>
- <Chao_Seader_Acentricity>0.121</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>30.563</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0.0052555196148</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
- <CompCreatorStudyFile></CompCreatorStudyFile>
- <Critical_Compressibility>0.249</Critical_Compressibility>
- <Critical_Pressure>8310000</Critical_Pressure>
- <Critical_Temperature>324.69</Critical_Temperature>
- <Critical_Volume>0.081</Critical_Volume>
- <CurrentDB>ChemSep</CurrentDB>
- <Dipole_Moment>3.6E-30</Dipole_Moment>
- <Electrolyte_Cp0>0</Electrolyte_Cp0>
- <Electrolyte_DelGF>0</Electrolyte_DelGF>
- <Electrolyte_DelHF>0</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>2</EnthalpyOfFusionAtTf>
- <Formula>HCl</Formula>
- <HVap_A>19563000</HVap_A>
- <HVap_B>-0.79988</HVap_B>
- <HVap_C>3.8907</HVap_C>
- <HVap_D>-4.9768</HVap_D>
- <HVap_E>2.2266</HVap_E>
- <HVap_TMAX>324.65</HVap_TMAX>
- <HVap_TMIN>158.97</HVap_TMIN>
- <HydrationNumber>0</HydrationNumber>
- <ID>1904</ID>
- <Ideal_Gas_Heat_Capacity_Const_A>29096.99</Ideal_Gas_Heat_Capacity_Const_A>
- <Ideal_Gas_Heat_Capacity_Const_B>-1271.123</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>6.610209</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>0.00378635</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>-1.3094E-06</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>16</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-2531.75041565028</IG_Enthalpy_of_Formation_25C>
- <IG_Entropy_of_Formation_25C>0.275048014113041</IG_Entropy_of_Formation_25C>
- <IG_Gibbs_Energy_of_Formation_25C>-2613.75598105809</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>2.3619</Liquid_Density_Const_A>
- <Liquid_Density_Const_B>0.23301</Liquid_Density_Const_B>
- <Liquid_Density_Const_C>324.69</Liquid_Density_Const_C>
- <Liquid_Density_Const_D>0.25076</Liquid_Density_Const_D>
- <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
- <Liquid_Density_Tmax>324.44</Liquid_Density_Tmax>
- <Liquid_Density_Tmin>158.97</Liquid_Density_Tmin>
- <Liquid_Heat_Capacity_Const_A>-53340</Liquid_Heat_Capacity_Const_A>
- <Liquid_Heat_Capacity_Const_B>265.92</Liquid_Heat_Capacity_Const_B>
- <Liquid_Heat_Capacity_Const_C>4.243</Liquid_Heat_Capacity_Const_C>
- <Liquid_Heat_Capacity_Const_D>0.058092</Liquid_Heat_Capacity_Const_D>
- <Liquid_Heat_Capacity_Const_E>-0.00013923</Liquid_Heat_Capacity_Const_E>
- <Liquid_Heat_Capacity_Tmax>188.13</Liquid_Heat_Capacity_Tmax>
- <Liquid_Heat_Capacity_Tmin>158.97</Liquid_Heat_Capacity_Tmin>
- <Liquid_Thermal_Conductivity_Const_A>-0.4993</Liquid_Thermal_Conductivity_Const_A>
- <Liquid_Thermal_Conductivity_Const_B>-113.3</Liquid_Thermal_Conductivity_Const_B>
- <Liquid_Thermal_Conductivity_Const_C>0.99185</Liquid_Thermal_Conductivity_Const_C>
- <Liquid_Thermal_Conductivity_Const_D>-0.0023549</Liquid_Thermal_Conductivity_Const_D>
- <Liquid_Thermal_Conductivity_Const_E>-3.3612E-06</Liquid_Thermal_Conductivity_Const_E>
- <Liquid_Thermal_Conductivity_Tmax>323.15</Liquid_Thermal_Conductivity_Tmax>
- <Liquid_Thermal_Conductivity_Tmin>273.15</Liquid_Thermal_Conductivity_Tmin>
- <Liquid_Viscosity_Const_A>-196.43</Liquid_Viscosity_Const_A>
- <Liquid_Viscosity_Const_B>5474.4</Liquid_Viscosity_Const_B>
- <Liquid_Viscosity_Const_C>31.068</Liquid_Viscosity_Const_C>
- <Liquid_Viscosity_Const_D>-9.4243E-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>36.46094</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>Hydrogen chloride</Name>
- <NegativeIon></NegativeIon>
- <NegativeIonStoichCoeff>0</NegativeIonStoichCoeff>
- <Normal_Boiling_Point>188.15</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>Cl</SMILES>
- <Solid_Density_Const_A>41.04</Solid_Density_Const_A>
- <Solid_Density_Const_B>-0.0070156</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>158.97</Solid_Density_Tmax>
- <Solid_Density_Tmin>103.15</Solid_Density_Tmin>
- <Solid_Heat_Capacity_Const_A>-10811</Solid_Heat_Capacity_Const_A>
- <Solid_Heat_Capacity_Const_B>1080.6</Solid_Heat_Capacity_Const_B>
- <Solid_Heat_Capacity_Const_C>-9.6311</Solid_Heat_Capacity_Const_C>
- <Solid_Heat_Capacity_Const_D>0.047728</Solid_Heat_Capacity_Const_D>
- <Solid_Heat_Capacity_Const_E>-9.1003E-05</Solid_Heat_Capacity_Const_E>
- <Solid_Heat_Capacity_Tmax>158</Solid_Heat_Capacity_Tmax>
- <Solid_Heat_Capacity_Tmin>100</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>-0.0056361</Surface_Tension_Const_A>
- <Surface_Tension_Const_B>317.9</Surface_Tension_Const_B>
- <Surface_Tension_Const_C>-7.6858</Surface_Tension_Const_C>
- <Surface_Tension_Const_D>0.026562</Surface_Tension_Const_D>
- <Surface_Tension_Const_E>-6.761E-05</Surface_Tension_Const_E>
- <Surface_Tension_Tmax>324.65</Surface_Tension_Tmax>
- <Surface_Tension_Tmin>158.97</Surface_Tension_Tmin>
- <SurfaceTensionEquation>16</SurfaceTensionEquation>
- <TemperatureOfFusion>158.97</TemperatureOfFusion>
- <UNIQUAC_Q>1.1</UNIQUAC_Q>
- <UNIQUAC_R>1.056032</UNIQUAC_R>
- <Vapor_Pressure_Constant_A>138.2562</Vapor_Pressure_Constant_A>
- <Vapor_Pressure_Constant_B>-4825.245</Vapor_Pressure_Constant_B>
- <Vapor_Pressure_Constant_C>-19.73669</Vapor_Pressure_Constant_C>
- <Vapor_Pressure_Constant_D>6.50759E-05</Vapor_Pressure_Constant_D>
- <Vapor_Pressure_Constant_E>2</Vapor_Pressure_Constant_E>
- <Vapor_Pressure_TMAX>324.65</Vapor_Pressure_TMAX>
- <Vapor_Pressure_TMIN>142.85</Vapor_Pressure_TMIN>
- <Vapor_Thermal_Conductivity_Const_A>0.0017816</Vapor_Thermal_Conductivity_Const_A>
- <Vapor_Thermal_Conductivity_Const_B>0.5013</Vapor_Thermal_Conductivity_Const_B>
- <Vapor_Thermal_Conductivity_Const_C>331.03</Vapor_Thermal_Conductivity_Const_C>
- <Vapor_Thermal_Conductivity_Const_D>3750.8</Vapor_Thermal_Conductivity_Const_D>
- <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
- <Vapor_Thermal_Conductivity_Tmax>700</Vapor_Thermal_Conductivity_Tmax>
- <Vapor_Thermal_Conductivity_Tmin>158.97</Vapor_Thermal_Conductivity_Tmin>
- <Vapor_Viscosity_Const_A>5.1969E-07</Vapor_Viscosity_Const_A>
- <Vapor_Viscosity_Const_B>0.66444</Vapor_Viscosity_Const_B>
- <Vapor_Viscosity_Const_C>177.83</Vapor_Viscosity_Const_C>
- <Vapor_Viscosity_Const_D>-3965.9</Vapor_Viscosity_Const_D>
- <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
- <Vapor_Viscosity_Tmax>1000</Vapor_Viscosity_Tmax>
- <Vapor_Viscosity_Tmin>200</Vapor_Viscosity_Tmin>
- <VaporizationEnthalpyEquation>106</VaporizationEnthalpyEquation>
- <VaporPressureEquation>101</VaporPressureEquation>
- <VaporThermalConductivityEquation>102</VaporThermalConductivityEquation>
- <VaporViscosityEquation>102</VaporViscosityEquation>
- <Z_Rackett>0</Z_Rackett>
- <FullerDiffusionVolume>23.31</FullerDiffusionVolume>
- <LennardJonesDiameter>3.36E-10</LennardJonesDiameter>
- <LennardJonesEnergy>328</LennardJonesEnergy>
- <Parachor>0.0125</Parachor>
- <Tag></Tag>
- <COSTALD_SRK_Acentric_Factor>0.1254</COSTALD_SRK_Acentric_Factor>
- <COSTALD_Characteristic_Volume>0.11545</COSTALD_Characteristic_Volume>
- <DynamicProperties />
- <UNIFACGroups />
- <MODFACGroups />
- <NISTMODFACGroups />
- <Elements>
- <Item Name="Cl" Value="1" />
- <Item Name="H" Value="1" />
- </Elements>
- </Compound>
- <Compound>
- <Type>DWSIM.Thermodynamics.BaseClasses.ConstantProperties</Type>
- <Acentric_Factor>0.65</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></CAS_Number>
- <Chao_Seader_Acentricity>0</Chao_Seader_Acentricity>
- <Chao_Seader_Liquid_Molar_Volume>0</Chao_Seader_Liquid_Molar_Volume>
- <Chao_Seader_Solubility_Parameter>0</Chao_Seader_Solubility_Parameter>
- <Charge>0</Charge>
- <ChemicalStructure></ChemicalStructure>
- <Comments></Comments>
- <CompCreatorStudyFile></CompCreatorStudyFile>
- <Critical_Compressibility>0.23</Critical_Compressibility>
- <Critical_Pressure>30000000</Critical_Pressure>
- <Critical_Temperature>2000</Critical_Temperature>
- <Critical_Volume>0.554</Critical_Volume>
- <CurrentDB>DWSIM</CurrentDB>
- <Dipole_Moment>0</Dipole_Moment>
- <Electrolyte_Cp0>0.0841</Electrolyte_Cp0>
- <Electrolyte_DelGF>-203.6</Electrolyte_DelGF>
- <Electrolyte_DelHF>-314</Electrolyte_DelHF>
- <EnthalpyOfFusionAtTf>0</EnthalpyOfFusionAtTf>
- <Formula>NH4Cl</Formula>
- <HVap_A>0</HVap_A>
- <HVap_B>0</HVap_B>
- <HVap_C>0</HVap_C>
- <HVap_D>0</HVap_D>
- <HVap_E>0</HVap_E>
- <HVap_TMAX>0</HVap_TMAX>
- <HVap_TMIN>0</HVap_TMIN>
- <HydrationNumber>0</HydrationNumber>
- <ID>200063</ID>
- <Ideal_Gas_Heat_Capacity_Const_A>0</Ideal_Gas_Heat_Capacity_Const_A>
- <Ideal_Gas_Heat_Capacity_Const_B>0</Ideal_Gas_Heat_Capacity_Const_B>
- <Ideal_Gas_Heat_Capacity_Const_C>0</Ideal_Gas_Heat_Capacity_Const_C>
- <Ideal_Gas_Heat_Capacity_Const_D>0</Ideal_Gas_Heat_Capacity_Const_D>
- <Ideal_Gas_Heat_Capacity_Const_E>0</Ideal_Gas_Heat_Capacity_Const_E>
- <IdealgasCpEquation>5</IdealgasCpEquation>
- <IG_Enthalpy_of_Formation_25C>-5870.25612263975</IG_Enthalpy_of_Formation_25C>
- <IG_Entropy_of_Formation_25C>0</IG_Entropy_of_Formation_25C>
- <IG_Gibbs_Energy_of_Formation_25C>-3806.31893811927</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>false</IsCOOLPROPSupported>
- <IsFPROPSSupported>false</IsFPROPSSupported>
- <IsHydratedSalt>false</IsHydratedSalt>
- <IsHYPO>0</IsHYPO>
- <IsIon>false</IsIon>
- <IsModified>false</IsModified>
- <IsPF>0</IsPF>
- <IsSalt>true</IsSalt>
- <Liquid_Density_Const_A>28.5286969527014</Liquid_Density_Const_A>
- <Liquid_Density_Const_B>0</Liquid_Density_Const_B>
- <Liquid_Density_Const_C>0</Liquid_Density_Const_C>
- <Liquid_Density_Const_D>0</Liquid_Density_Const_D>
- <Liquid_Density_Const_E>0</Liquid_Density_Const_E>
- <Liquid_Density_Tmax>0</Liquid_Density_Tmax>
- <Liquid_Density_Tmin>0</Liquid_Density_Tmin>
- <Liquid_Heat_Capacity_Const_A>168200</Liquid_Heat_Capacity_Const_A>
- <Liquid_Heat_Capacity_Const_B>0</Liquid_Heat_Capacity_Const_B>
- <Liquid_Heat_Capacity_Const_C>0</Liquid_Heat_Capacity_Const_C>
- <Liquid_Heat_Capacity_Const_D>0</Liquid_Heat_Capacity_Const_D>
- <Liquid_Heat_Capacity_Const_E>0</Liquid_Heat_Capacity_Const_E>
- <Liquid_Heat_Capacity_Tmax>0</Liquid_Heat_Capacity_Tmax>
- <Liquid_Heat_Capacity_Tmin>0</Liquid_Heat_Capacity_Tmin>
- <Liquid_Thermal_Conductivity_Const_A>0</Liquid_Thermal_Conductivity_Const_A>
- <Liquid_Thermal_Conductivity_Const_B>0</Liquid_Thermal_Conductivity_Const_B>
- <Liquid_Thermal_Conductivity_Const_C>0</Liquid_Thermal_Conductivity_Const_C>
- <Liquid_Thermal_Conductivity_Const_D>0</Liquid_Thermal_Conductivity_Const_D>
- <Liquid_Thermal_Conductivity_Const_E>0</Liquid_Thermal_Conductivity_Const_E>
- <Liquid_Thermal_Conductivity_Tmax>0</Liquid_Thermal_Conductivity_Tmax>
- <Liquid_Thermal_Conductivity_Tmin>0</Liquid_Thermal_Conductivity_Tmin>
- <Liquid_Viscosity_Const_A>0</Liquid_Viscosity_Const_A>
- <Liquid_Viscosity_Const_B>0</Liquid_Viscosity_Const_B>
- <Liquid_Viscosity_Const_C>0</Liquid_Viscosity_Const_C>
- <Liquid_Viscosity_Const_D>0</Liquid_Viscosity_Const_D>
- <Liquid_Viscosity_Const_E>0</Liquid_Viscosity_Const_E>
- <LiquidDensityEquation>1</LiquidDensityEquation>
- <LiquidHeatCapacityEquation>1</LiquidHeatCapacityEquation>
- <LiquidThermalConductivityEquation></LiquidThermalConductivityEquation>
- <LiquidViscosityEquation></LiquidViscosityEquation>
- <Molar_Weight>53.49</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>Ammonium Chloride</Name>
- <NegativeIon>Cl-</NegativeIon>
- <NegativeIonStoichCoeff>1</NegativeIonStoichCoeff>
- <Normal_Boiling_Point>0</Normal_Boiling_Point>
- <OriginalDB>Electrolytes</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>NH4+</PositiveIon>
- <PositiveIonStoichCoeff>1</PositiveIonStoichCoeff>
- <PR_Volume_Translation_Coefficient>0</PR_Volume_Translation_Coefficient>
- <SMILES></SMILES>
- <Solid_Density_Const_A>0</Solid_Density_Const_A>
- <Solid_Density_Const_B>0</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>0</Solid_Density_Tmax>
- <Solid_Density_Tmin>0</Solid_Density_Tmin>
- <Solid_Heat_Capacity_Const_A>0</Solid_Heat_Capacity_Const_A>
- <Solid_Heat_Capacity_Const_B>0</Solid_Heat_Capacity_Const_B>
- <Solid_Heat_Capacity_Const_C>0</Solid_Heat_Capacity_Const_C>
- <Solid_Heat_Capacity_Const_D>0</Solid_Heat_Capacity_Const_D>
- <Solid_Heat_Capacity_Const_E>0</Solid_Heat_Capacity_Const_E>
- <Solid_Heat_Capacity_Tmax>0</Solid_Heat_Capacity_Tmax>
- <Solid_Heat_Capacity_Tmin>0</Solid_Heat_Capacity_Tmin>
- <SolidDensityAtTs>1526</SolidDensityAtTs>
- <SolidDensityEquation></SolidDensityEquation>
- <SolidHeatCapacityEquation></SolidHeatCapacityEquation>
- <SolidTs>293.15</SolidTs>
- <SRK_Volume_Translation_Coefficient>0</SRK_Volume_Translation_Coefficient>
- <StandardStateMolarVolume>0</StandardStateMolarVolume>
- <StoichSum>2</StoichSum>
- <Surface_Tension_Const_A>0</Surface_Tension_Const_A>
- <Surface_Tension_Const_B>0</Surface_Tension_Const_B>
- <Surface_Tension_Const_C>0</Surface_Tension_Const_C>
- <Surface_Tension_Const_D>0</Surface_Tension_Const_D>
- <Surface_Tension_Const_E>0</Surface_Tension_Const_E>
- <Surface_Tension_Tmax>0</Surface_Tension_Tmax>
- <Surface_Tension_Tmin>0</Surface_Tension_Tmin>
- <SurfaceTensionEquation></SurfaceTensionEquation>
- <TemperatureOfFusion>0</TemperatureOfFusion>
- <UNIQUAC_Q>0</UNIQUAC_Q>
- <UNIQUAC_R>0</UNIQUAC_R>
- <Vapor_Pressure_Constant_A>0</Vapor_Pressure_Constant_A>
- <Vapor_Pressure_Constant_B>0</Vapor_Pressure_Constant_B>
- <Vapor_Pressure_Constant_C>0</Vapor_Pressure_Constant_C>
- <Vapor_Pressure_Constant_D>0</Vapor_Pressure_Constant_D>
- <Vapor_Pressure_Constant_E>0</Vapor_Pressure_Constant_E>
- <Vapor_Pressure_TMAX>0</Vapor_Pressure_TMAX>
- <Vapor_Pressure_TMIN>0</Vapor_Pressure_TMIN>
- <Vapor_Thermal_Conductivity_Const_A>0</Vapor_Thermal_Conductivity_Const_A>
- <Vapor_Thermal_Conductivity_Const_B>0</Vapor_Thermal_Conductivity_Const_B>
- <Vapor_Thermal_Conductivity_Const_C>0</Vapor_Thermal_Conductivity_Const_C>
- <Vapor_Thermal_Conductivity_Const_D>0</Vapor_Thermal_Conductivity_Const_D>
- <Vapor_Thermal_Conductivity_Const_E>0</Vapor_Thermal_Conductivity_Const_E>
- <Vapor_Thermal_Conductivity_Tmax>0</Vapor_Thermal_Conductivity_Tmax>
- <Vapor_Thermal_Conductivity_Tmin>0</Vapor_Thermal_Conductivity_Tmin>
- <Vapor_Viscosity_Const_A>0</Vapor_Viscosity_Const_A>
- <Vapor_Viscosity_Const_B>0</Vapor_Viscosity_Const_B>
- <Vapor_Viscosity_Const_C>0</Vapor_Viscosity_Const_C>
- <Vapor_Viscosity_Const_D>0</Vapor_Viscosity_Const_D>
- <Vapor_Viscosity_Const_E>0</Vapor_Viscosity_Const_E>
- <Vapor_Viscosity_Tmax>0</Vapor_Viscosity_Tmax>
- <Vapor_Viscosity_Tmin>0</Vapor_Viscosity_Tmin>
- <VaporizationEnthalpyEquation></VaporizationEnthalpyEquation>
- <VaporPressureEquation>101</VaporPressureEquation>
- <VaporThermalConductivityEquation></VaporThermalConductivityEquation>
- <VaporViscosityEquation></VaporViscosityEquation>
- <Z_Rackett>0.23</Z_Rackett>
- <FullerDiffusionVolume>0</FullerDiffusionVolume>
- <LennardJonesDiameter>0</LennardJonesDiameter>
- <LennardJonesEnergy>0</LennardJonesEnergy>
- <Parachor>0</Parachor>
- <Tag></Tag>
- <COSTALD_SRK_Acentric_Factor>0</COSTALD_SRK_Acentric_Factor>
- <COSTALD_Characteristic_Volume>0</COSTALD_Characteristic_Volume>
- <DynamicProperties />
- <UNIFACGroups />
- <MODFACGroups />
- <NISTMODFACGroups />
- <Elements>
- <Item Name="Cl" Value="1" />
- <Item Name="H" Value="4" />
- <Item Name="N" Value="1" />
- </Elements>
- </Compound>
- </Compounds>
- <ReactionSets>
- <ReactionSet>
- <ID>DefaultSet</ID>
- <Name>Default Set</Name>
- <Description>Default Reaction Set</Description>
- <Reactions>
- <Reaction Key="67a5f595-d8fd-4edb-8c26-640a19818dbf" ReactionID="67a5f595-d8fd-4edb-8c26-640a19818dbf" Rank="0" IsActive="true" />
- </Reactions>
- </ReactionSet>
- </ReactionSets>
- <Reactions>
- <Reaction>
- <Type>DWSIM.Thermodynamics.BaseClasses.Reaction</Type>
- <BaseReactant>Ammonia</BaseReactant>
- <Description></Description>
- <Equation>NH3 + HCl --> NH4Cl </Equation>
- <ID>67a5f595-d8fd-4edb-8c26-640a19818dbf</ID>
- <Name></Name>
- <ReactionBasis>Fugacity</ReactionBasis>
- <ReactionHeat>-175792</ReactionHeat>
- <ReactionHeatCO>0</ReactionHeatCO>
- <ReactionPhase>Vapor</ReactionPhase>
- <ReactionType>Conversion</ReactionType>
- <StoichBalance>0</StoichBalance>
- <A_Forward>0</A_Forward>
- <A_Reverse>0</A_Reverse>
- <Approach>0</Approach>
- <ConcUnit></ConcUnit>
- <ConstantKeqValue>0</ConstantKeqValue>
- <E_Forward>0</E_Forward>
- <E_Reverse>0</E_Reverse>
- <Expression>80</Expression>
- <KExprType>Gibbs</KExprType>
- <Kvalue>0</Kvalue>
- <Rate>0</Rate>
- <RateEquationDenominator></RateEquationDenominator>
- <RateEquationNumerator></RateEquationNumerator>
- <ReactionGibbsEnergy>0</ReactionGibbsEnergy>
- <Tmax>2000</Tmax>
- <Tmin>0</Tmin>
- <VelUnit></VelUnit>
- <ReactionKinFwdType>Arrhenius</ReactionKinFwdType>
- <ReactionKinRevType>Arrhenius</ReactionKinRevType>
- <ReactionKinFwdExpression></ReactionKinFwdExpression>
- <ReactionKinRevExpression></ReactionKinRevExpression>
- <E_Forward_Unit>J/mol</E_Forward_Unit>
- <E_Reverse_Unit>J/mol</E_Reverse_Unit>
- <ReactionKinetics>Expression</ReactionKinetics>
- <ScriptTitle></ScriptTitle>
- <EquilibriumReactionBasisUnits>Pa</EquilibriumReactionBasisUnits>
- <Compounds>
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a/Triple_Effect_Evaporation_Of_Saline_Solution_By_Ms_Yutika_Naik/README.txt b/Triple_Effect_Evaporation_Of_Saline_Solution_By_Ms_Yutika_Naik/README.txt new file mode 100644 index 0000000..f808ab1 --- /dev/null +++ b/Triple_Effect_Evaporation_Of_Saline_Solution_By_Ms_Yutika_Naik/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Triple effect evaporation of saline solution +Proposar Name: Ms Yutika Naik +University: Sardar Vallabhbhai National Institute Of Technology, Surat + + +DWSIM Flowsheet Project By FOSSEE, IIT Bombay |