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"Minimum Dynamic Pressure for this Unit Operation."
Initialize using Inlet Stream
System.String
"Initializes the volume content with information from the inlet stream, if the content is null."
Reset Content
System.String
"Empties the volume content on the next run."
Flow Conductance
System.Int64
67
Volume
System.Int64
63
Minimum Pressure
System.Int64
46
Initialize using Inlet Stream
System.Int64
66
Reset Content
System.Int64
66
PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d
DWSIM.UnitOperations.Streams.EnergyStream
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true
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CorrentedeEnergia
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DWSIM.Thermodynamics.Streams.MaterialStream
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false
false
DefaultBasis
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CorrentedeMatria
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MAT-a1358b61-5abc-42a4-9471-1a07a6cc735e
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DWSIM.Thermodynamics.BaseClasses.Compound
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
OverallLiquid
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Vapor
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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0
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid1
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid1
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
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0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
1
1
0
0
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Methane
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0
0
NaN
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid2
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid2
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
0
0
0
0
0
0
0
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Methane
0
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0
0
0
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid3
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid3
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
0
0
0
0
0
0
0
0
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Methane
0
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0
0
0
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Aqueous
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Aqueous
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
1
1
0
0
1
0
0
0
0
Methane
0
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0
0
NaN
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Solid
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Solid
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
0
DWSIM.UnitOperations.UnitOperations.Compressor
PressureChangers
true
false
400.580342373476
OutletPressure
Adiabatic
false
99.999999999953
100
400000
120.580342373476
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500000
1.28619913758745
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0
0
0
0
1500
true
CompressorAdiabtico
COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3
Pressure
false
true
false
true
false
09/16/2021 11:30:10
false
Manipulated
false
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COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3
PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d
DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve
false
HEAD
3e273580-de52-4048-bdf4-d6be8116782b
Head
DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve
false
EFF
da74c9c0-8a2b-477a-aa77-ae7263a3ed25
Efficiency
DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve
false
POWER
43edcce7-8d4a-4056-8f9e-6ec621dec3cc
Power
DWSIM.Thermodynamics.Streams.MaterialStream
Streams
true
false
false
DefaultBasis
Mass
GlobalDef
true
CorrentedeMatria
MAT-8aae0cd5-5a00-4ced-86e6-1a47a4a675ac
MAT-8aae0cd5-5a00-4ced-86e6-1a47a4a675ac
0
false
Temperature_and_Pressure
Molar_Fractions
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true
Pressure
false
true
false
true
false
09/16/2021 11:30:10
false
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false
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MAT-8aae0cd5-5a00-4ced-86e6-1a47a4a675ac
PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
1
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Methane
0
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0
NaN
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Mixture
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Mixture
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
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NaN
NaN
0
0
0
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NaN
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0
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0
0
0
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
OverallLiquid
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
OverallLiquid
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0.00237950220439316
false
1
1
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0
1
0
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Methane
100000
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1
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0
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DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Vapor
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Vapor
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
1
1
0
0
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0
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Methane
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0
0
NaN
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid1
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid1
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
0
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0
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0
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Methane
0
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0
0
0
0
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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
0
0
0
0
0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
0
0
0
0
0
0
0
0
0
Methane
0
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0
0
0
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Liquid3
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Liquid3
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
0
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DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
0
0
0
0
0
0
0
0
0
Methane
0
-0.0378938418374108
0
0
0
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Aqueous
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Aqueous
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
0
7
DWSIM.Thermodynamics.BaseClasses.Compound
Methane
0
false
1
1
0
0
1
0
0
0
0
Methane
0
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0
0
NaN
0
0
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
Solid
System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound]
Solid
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
DWSIM.Thermodynamics.BaseClasses.PhaseProperties
0
0
0
0
0
0
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
Rackett_and_ExpData
true
true
ExpData
Letsou_Stiel
true
MoleAverage
Ideal
FromLiquidFugacity
false
false
LeeKesler
true
false
false
false
true
NestedLoops
[]
{}
17251524.dwbcs
F:\DWSIM\Flowsheet.dwxml
false
false
false
false
false
false
false
false
G8
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G6
DESKTOP-B608FMG\preet_lk79p9y
MySimulation_5
false
DWSIM.SharedClasses.SystemsOfUnits.SIUnits_Custom5
m/s2
Pa
-
m2
m/kg
m2/s
1/Pa
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bar
C.
kg/m3
mm
m
kJ/kg
kJ/[kg.K]
kJ/kg
kJ/[kg.K]
N
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Pa
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kJ/[kg.K]
kW
kJ/[kg.K]
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-
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-
kg
kg/m3
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m-1
kmol/m3
kJ/kmol
kJ/[kmol.K]
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kmol/h
-
kg/kmol
C5
C
C
bar
kmol/[m3.h]
kmol/[kg.s]
m3/kg
m/s
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C
W/[m.K]
W/[m.K]
W/[m.K]
mm
bar
m/s
Pa.s
Pa.s
Pa.s
m3
m3/h
m2/s
[kg/s]/[Pa^0.5]
true
false
ShowWarning
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0.01
0.01
false
RightBottom
true
DimGray
Consolas
8
4
Molar_Fractions
true
true
AsAdded
false
true
None
false
DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic
false
1
true
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false
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false
false
false
MaterialStream
0
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false
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false
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false
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false
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true
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false
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Adiabatic Compressor
false
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0
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false
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false
COMP-9a8683ba-83c0-4fab-9ea6-31f0b79ad4b3
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MaterialStream
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false
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false
MAT-a1358b61-5abc-42a4-9471-1a07a6cc735e
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic
false
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Energy Stream
false
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true
EnergyStream
0
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false
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false
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E-01
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false
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CoolerGraphic
false
1
true
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Material Stream Cooler
false
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Cooler
0
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false
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false
RESF-4437c986-5958-4780-8cd8-c3549f6e1576
COOL-01
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic
false
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true
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false
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MaterialStream
0
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false
20
false
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false
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic
false
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true
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EnergyStream
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false
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false
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E-02
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false
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CompressorGraphic
false
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true
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false
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic
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false
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DWSIM.Drawing.SkiaSharp.GraphicObjects.Tables.MasterTableGraphic
Master Property Table
Object S-10 S-09 S-08 S-07 S-06 S-05 S-04 S-03 S-02 S-01
Temperature -161.698 -161.698 -161.698 -63.15 116.082 6.85 129.159 6.85 127.43 6.85 C
Pressure 1 1 1 100 100 25 25 5 5 1 bar
Mass Flow 0.393659 0.606341 1 1 1 1 1 1 1 1 kg/h
Molar Flow 0.0245385 0.037796 0.0623346 0.0623346 0.0623346 0.0623346 0.0623346 0.0623346 0.0623346 0.0623346 kmol/h
Molar Fraction (Vapor) 0 1 0.606341 0 1 1 1 1 1 1
Molar Fraction (Mixture) / Methane 1 1 1 1 1 1 1 1 1 1
Mass Fraction (Mixture) / Methane 1 1 1 1 1 1 1 1 1 1
1
5
#ff000000
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#ff000000
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Name | DESC
- S-10
- S-09
- S-08
- S-07
- S-06
- S-05
- S-04
- S-03
- S-02
- S-01
MaterialStream
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GO_MasterTable
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MASTERTABLE-0b2f7bb1-1838-4191-903d-0c85e903fabc
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Name | ASC
Name | DESC
Temperature | ASC
Temperature | DESC
Pressure | ASC
Pressure | DESC
Mass Flow | ASC
Mass Flow | DESC
Molar Flow | ASC
Molar Flow | DESC
Molar Fraction (Vapor) | ASC
Molar Fraction (Vapor) | DESC
Molar Fraction (Mixture) / Methane | ASC
Molar Fraction (Mixture) / Methane | DESC
Mass Fraction (Mixture) / Methane | ASC
Mass Fraction (Mixture) / Methane | DESC
Custom
PP-c0cfbb95-8720-47d8-9445-fedf3f6b069d
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
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Rackett_and_ExpData
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true
true
ExpData
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true
MoleAverage
Ideal
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false
false
LeeKesler
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NestedLoops
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DWSIM.Thermodynamics.BaseClasses.ConstantProperties
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74-82-8
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0.9414
CH4
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DefaultSet
Default Set
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DWSIM.DynamicsManager.Manager
DWSIM.SharedClasses.Flowsheet.Optimization.OptimizationCase
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