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Volume
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Flow Conductance
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid3
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Vapor
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid1
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Liquid1
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid2
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid2
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
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Helium-4
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid3
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid3
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
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Helium-4
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NaN
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Aqueous
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Aqueous
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Solid
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Solid
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables
DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage
NRTL
In this Property Package, the NRTL (Non-Random Two-Liquid) model is used to calculate liquid-phase activity coefficients. Enthalpies are calculated by the Lee-Kesler model, while vapor-phase fugacities (optionally) and other thermodynamic properties (both phases) are calculated by the Peng-Robinson EOS.
NRTL (1)
false
false
false
Rackett_and_ExpData
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true
true
ExpData
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true
MoleAverage
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false
false
LeeKesler
true
false
false
false
true
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.MasterTableGraphic
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.MasterTableGraphic
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PP-47d83824-ea2a-4753-8abb-d524dcaac853
DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage
NRTL
In this Property Package, the NRTL (Non-Random Two-Liquid) model is used to calculate liquid-phase activity coefficients. Enthalpies are calculated by the Lee-Kesler model, while vapor-phase fugacities (optionally) and other thermodynamic properties (both phases) are calculated by the Peng-Robinson EOS.
NRTL (1)
false
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Rackett_and_ExpData
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true
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MoleAverage
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LeeKesler
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NestedLoops
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DWSIM.Thermodynamics.BaseClasses.ConstantProperties
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DefaultSet
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Default Reaction Set
DWSIM.DynamicsManager.Manager
DWSIM.SharedClasses.Flowsheet.Optimization.OptimizationCase
optcase0
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</NestedPanes>
</DockWindow>
<DockWindow ID="1" DockState="DockLeft" ZOrderIndex="3">
<NestedPanes Count="2">
<Pane ID="0" RefID="3" PrevPane="-1" Alignment="Bottom" Proportion="0.5" />
<Pane ID="1" RefID="2" PrevPane="3" Alignment="Bottom" Proportion="0.5" />
</NestedPanes>
</DockWindow>
<DockWindow ID="2" DockState="DockRight" ZOrderIndex="4">
<NestedPanes Count="0" />
</DockWindow>
<DockWindow ID="3" DockState="DockTop" ZOrderIndex="5">
<NestedPanes Count="0" />
</DockWindow>
<DockWindow ID="4" DockState="DockBottom" ZOrderIndex="2">
<NestedPanes Count="1">
<Pane ID="0" RefID="1" PrevPane="-1" Alignment="Right" Proportion="0.5" />
</NestedPanes>
</DockWindow>
</DockWindows>
<FloatWindows Count="0" />
</DockPanel>