source: trunk/eml/streams.mso @ 917

#*-------------------------------------------------------------------
* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
*
* This LIBRARY is free software; you can distribute it and/or modify
* it under the therms of the ALSOC FREE LICENSE as available at
* http://www.enq.ufrgs.br/alsoc.
*
* EMSO Copyright (C) 2004 - 2007 ALSOC, original code
* from http://www.rps.eng.br Copyright (C) 2002-2004.
* All rights reserved.
*
* EMSO is distributed under the therms of the ALSOC LICENSE as
* available at http://www.enq.ufrgs.br/alsoc.
*
*--------------------------------------------------------------------
* Model of basic streams
*----------------------------------------------------------------------
* Author: Paula B. Staudt and Rafael de P. Soares
* $Id: streams.mso 753 2009-05-22 16:55:00Z arge $
*---------------------------------------------------------------------*#

using "types";

Model stream
        ATTRIBUTES
        Pallete = false;
        Brief = "General Material Stream";
        Info =
        "This is the basic building block for the EML models.
        Every model should have input and output streams derived
        from this model.";
        
        PARAMETERS
        outer NComp as Integer (Brief = "Number of chemical components", Lower = 1); 

        VARIABLES
        F as flow_mol                   (Brief = "Stream Molar Flow Rate");
        T as temperature                (Brief = "Stream Temperature");
        P as pressure                   (Brief = "Stream Pressure");
        h as enth_mol                   (Brief = "Stream Enthalpy");
        v as fraction                   (Brief = "Vapourization fraction");
        z(NComp) as fraction    (Brief = "Stream Molar Fraction");
end

Model liquid_stream as stream
        ATTRIBUTES
        Pallete = false;
        Brief = "Liquid Material Stream";
        Info =
        "Model for liquid material streams.
        This model should be used only when the phase of the stream
        is known ''a priori''.";

        PARAMETERS
        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
        
        EQUATIONS
        "Liquid Enthalpy"
        h = PP.LiquidEnthalpy(T, P, z);
        "Liquid stream"
        v = 0;
end

Model vapour_stream as stream
        ATTRIBUTES
        Pallete = false;
        Brief = "Vapour Material Stream";
        Info =
        "Model for vapour material streams.
        This model should be used only when the phase of the stream
        is known ''a priori''.";

        PARAMETERS
        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
        
        EQUATIONS
        "Vapour Enthalpy"
        h = PP.VapourEnthalpy(T, P, z);
        "Vapour stream"
        v = 1;
end

Model streamPH as stream
        ATTRIBUTES
        Brief = "Stream with built-in flash calculation";
        Info = "
        This model should be used when the vaporization fraction
        is unknown.
        
        The built-in flash calculation will determine the stream
        state as a function of the overall composition '''z''', the
        pressure '''P''' and the enthalpy '''h'''.
        
        Additionally, the liquid composition '''x''' and the vapor
        composition '''y''' are calculated.     
        ";
        Pallete = false;
        
        PARAMETERS
        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
        
        VARIABLES
        x(NComp) as fraction    (Brief = "Liquid Molar Fraction",Hidden=true);
        y(NComp) as fraction    (Brief = "Vapour Molar Fraction",Hidden=true);

        EQUATIONS
        "Flash Calculation"
        [v, x, y] = PP.FlashPH(P, h, z);
        
        "Enthalpy"
        h = (1-v)*PP.LiquidEnthalpy(T, P, x) + v*PP.VapourEnthalpy(T, P, y);
        
end

Model streamPHS as streamPH
        ATTRIBUTES
        Brief = "Stream with built-in flash calculation";
        Info = "
        This model should be used when the vaporization fraction
        is unknown.
        
        The built-in flash calculation will determine the stream
        state as a function of the overall composition '''z''', the
        pressure '''P''' and the enthalpy '''h'''.
        
        Additionally, the liquid composition '''x''', the vapor
        composition '''y''' and the stream entropy are calculated.      
        ";
        Pallete = false;
        
PARAMETERS
        outer PP as Plugin(Brief = "External Physical Properties", Type="PP");
        
VARIABLES
        s as entr_mol   (Brief = "Stream Entropy");

EQUATIONS

"Entropy"
        s = (1-v)*PP.LiquidEntropy(T, P, x) +   v*PP.VapourEntropy(T, P, y);
        
end

Model source
ATTRIBUTES
        Pallete = true;
        Icon = "icon/Source";
        Brief = "Material stream source";
        Info = "
        This model should be used for boundary streams.
        Usually these streams are known and come from another process
        units.

        The user should specify:
         * Total molar (mass or volumetric) flow
         * Temperature
         * Pressure
         * Molar or mass composition
        
        No matter the specification set, the model will calculate some
        additional properties:
         * Mass density
         * Mass flow
         * Mass compostions
         * Specific volume
         * Vapour fraction
         * Volumetric flow
         * Liquid and Vapour compositions
        ";

PARAMETERS
        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1); 
                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
                  CompositionBasis              as Switcher             (Brief = "Molar or Mass Composition", Valid = ["Molar", "Mass"], Default="Molar");
                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
                  T_std                                         as temperature (Brief = "Standard temperature", Hidden=true, Default = 298.15);
                  P_std                                         as pressure (Brief = "Standard pressure", Hidden=true, Default = 1);
SET

        M   = PP.MolecularWeight();

VARIABLES

        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
        
        Composition(NComp) as fraction                  (Brief = "Stream Composition");
        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
        Fw                                                      as flow_mass            (Brief = "Stream Mass Flow");
        Fvol                                    as flow_vol        (Brief = "Volumetric Flow");
        Fvol_std                                as flow_vol        (Brief = "Standard Volumetric Flow (1 atm, 20 C)");
        T                                                               as temperature  (Brief = "Stream Temperature");
        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
        P                                                               as pressure             (Brief = "Stream Pressure");
        
        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
        
        Mw                                              as molweight                    (Brief = "Average Mol Weight",Protected=true);
        vm                                              as volume_mol           (Brief = "Molar Volume",Protected=true);        
        vm_std                                  as volume_mol           (Brief = "Standard Molar Volume",Protected=true);       
        rho                                             as dens_mass                    (Brief = "Stream Mass Density",Protected=true);
        rhom                                            as dens_mol                     (Brief = "Stream Molar Density",Protected=true);
        
        zmass(NComp)            as fraction                             (Brief = "Mass Fraction",Protected=true);
        
        EQUATIONS

switch CompositionBasis

        case "Molar":
"Stream Molar Composition"
        Outlet.z = Composition/sum(Composition); 

"Stream Mass Composition"
        zmass = M*Outlet.z / Mw;

        case "Mass":
"Stream Mass Composition"
        zmass = Composition/sum(Composition);

"Stream Molar Composition"
        Outlet.z*sum(zmass/M) = zmass/M;

end

switch ValidPhases
        
        case "Liquid-Only":

"Vapour Fraction"
        Outlet.v = 0;

"Liquid Composition"
        x = Outlet.z;

"Vapour Composition"
        y = Outlet.z;

"Overall Enthalpy"
        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);

"Molar Volume"
        vm = PP.LiquidVolume(Outlet.T, Outlet.P, x);

"Standard Molar Volume"
        vm_std = PP.LiquidVolume(T_std, P_std, x);

        case "Vapour-Only":

"Vapor Fraction"
        Outlet.v = 1;

"Liquid Composition"
        x = Outlet.z;

"Vapour Composition"
        y = Outlet.z;

"Overall Enthalpy"
        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);

"Molar Volume"
        vm = PP.VapourVolume(Outlet.T, Outlet.P, y);

"Standard Molar Volume"
        vm_std = PP.VapourVolume(T_std, P_std, y);

        case "Vapour-Liquid":

"Flash Calculation"
        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);

"Overall Enthalpy"
        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);

"Molar Volume"
        vm = (1-Outlet.v)*PP.LiquidVolume(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourVolume(Outlet.T, Outlet.P, y);

"Standard Molar Volume"
        vm_std = (1-Outlet.v)*PP.LiquidVolume(T_std, P_std, x) + Outlet.v*PP.VapourVolume(T_std, P_std, y);

end

"Molar Density"
        rhom * vm = 1;

"Average Molecular Weight"
        Mw = sum(M*Outlet.z);

"Mass or Molar Density"
        rhom * Mw = rho;

"Flow Mass"
        Fw      =  Mw*Outlet.F;

"Volumetric Flow"
        Fvol = Outlet.F*vm ;

"Standard Volumetric Flow"
        Fvol_std = Outlet.F*vm_std ;

"Temperature in °C"
        T_Cdeg = Outlet.T - 273.15 * 'K';

"Equate Flow"
        Outlet.F = F;

"Equate Pressures"
        Outlet.P = P;

"Equate Temperatures"
        Outlet.T = T;
        
end

Model simple_source

ATTRIBUTES
        Pallete = true;
        Icon = "icon/Source";
        Brief = "Simple Material stream source";
        Info = "
        This model should be used for boundary streams.
        Usually these streams are known and come from another process
        units.

        The user should specify:
         * Total molar flow
         * Temperature
         * Pressure
         * Molar composition
";

PARAMETERS
        outer PP                                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
        outer NComp                             as Integer                      (Brief = "Number of chemical components", Lower = 1); 
                  M(NComp)                              as molweight    (Brief = "Component Mol Weight");
                  ValidPhases                           as Switcher             (Brief = "Valid Phases for Flash Calculation", Valid = ["Vapour-Only", "Liquid-Only","Vapour-Liquid"], Default="Vapour-Liquid");
        

SET

        M   = PP.MolecularWeight();

VARIABLES

        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);
        
        MolarComposition(NComp) as fraction                     (Brief = "Stream Molar Composition");
        F                                                               as flow_mol             (Brief = "Stream Molar Flow Rate");
        T                                                               as temperature  (Brief = "Stream Temperature");
        T_Cdeg                                          as temperature  (Brief = "Temperature in °C", Lower=-200);
        P                                                               as pressure             (Brief = "Stream Pressure");
        
        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
        

EQUATIONS

"Stream Molar Composition"
        Outlet.z = MolarComposition/sum(MolarComposition); 


switch ValidPhases
        
        case "Liquid-Only":

"Vapour Fraction"
        Outlet.v = 0;

"Liquid Composition"
        x = Outlet.z;

"Vapour Composition"
        y = Outlet.z;

"Overall Enthalpy"
        Outlet.h = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);


        case "Vapour-Only":

"Vapor Fraction"
        Outlet.v = 1;

"Liquid Composition"
        x = Outlet.z;

"Vapour Composition"
        y = Outlet.z;

"Overall Enthalpy"
        Outlet.h = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);


        case "Vapour-Liquid":

"Flash Calculation"
        [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);

"Overall Enthalpy"
        Outlet.h = (1-Outlet.v)*PP.LiquidEnthalpy(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourEnthalpy(Outlet.T, Outlet.P, y);

end

"Temperature in °C"
        T_Cdeg = Outlet.T - 273.15 * 'K';

"Equate Flow"
        Outlet.F = F;

"Equate Pressures"
        Outlet.P = P;

"Equate Temperatures"
        Outlet.T = T;

end

Model sink
        ATTRIBUTES
        Pallete = true;
        Icon = "icon/Sink";
        Brief = "Material stream sink";
        Info = "
        This model should be used for boundary streams when additional
        information about the stream is desired.

        Some of the additional informations calculated by this models are:
         * Mass density
         * Mass flow
         * Mass compostions
         * Specific volume
         * Vapour fraction
         * Volumetric flow
         * Liquid and Vapour compositions
        ";

        PARAMETERS
        outer PP                        as Plugin               (Brief = "External Physical Properties", Type="PP");
        outer NComp             as Integer              (Brief = "Number of chemical components", Lower = 1); 
                  M(NComp)      as molweight    (Brief = "Component Mol Weight");
                  rhoModel              as Switcher             (Brief = "Density model", Valid = ["volume", "correlation"], Default="volume");
                  T_std                 as temperature  (Brief = "Standard temperature", Hidden=true, Default = 298.15);
                  P_std                 as pressure             (Brief = "Standard pressure", Hidden=true, Default = 1);

        SET

        M   = PP.MolecularWeight();
        
        VARIABLES
        in Inlet                as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Symbol="_{in}");
        v                               as fraction             (Brief = "Vapourization fraction");
        x(NComp)                as fraction             (Brief = "Liquid Molar Fraction",Hidden=true);
        y(NComp)                as fraction             (Brief = "Vapour Molar Fraction",Hidden=true);
        zmass(NComp)    as fraction             (Brief = "Mass Fraction");
        Mw                              as molweight    (Brief = "Average Mol Weight");
        vm                              as volume_mol   (Brief = "Molar Volume");       
        vm_std                  as volume_mol   (Brief = "Standard Molar Volume",Protected=true);       
        rho                             as dens_mass    (Brief = "Stream Mass Density");
        rhom                    as dens_mol             (Brief = "Stream Molar Density");
        Fw                              as flow_mass    (Brief = "Stream Mass Flow");
        Fvol            as flow_vol     (Brief = "Volumetric Flow");
        Fvol_std        as flow_vol     (Brief = "Standard Volumetric Flow (1 atm, 20 C)");
        s                               as entr_mol             (Brief = "Stream Entropy");
        T_Cdeg                  as temperature  (Brief = "Temperature in °C", Lower=-200);

        EQUATIONS
        "Flash Calculation"
        [v, x, y] = PP.FlashPH(Inlet.P, Inlet.h, Inlet.z);
        
        "Average Molecular Weight"
        Mw = sum(M*Inlet.z);

        switch rhoModel
                case "volume":
        "Molar Density"
                rhom * vm = 1;
                
                case "correlation":
        "Mass Density"
                rho * ((1-v)/PP.LiquidDensity(Inlet.T,Inlet.P,x) + v/PP.VapourDensity(Inlet.T,Inlet.P,y)) = 1;
        end
        
        "Mass or Molar Density"
        rhom * Mw = rho;

        "Flow Mass"
        Fw      =  Mw*Inlet.F;

        "Molar Volume"
        vm = (1-v)*PP.LiquidVolume(Inlet.T, Inlet.P, x) + v*PP.VapourVolume(Inlet.T, Inlet.P, y);

        "Standard Molar Volume"
        vm_std = (1-v)*PP.LiquidVolume(T_std, P_std, x) + v*PP.VapourVolume(T_std, P_std, y);

        "Volumetric Flow"
        Fvol = Inlet.F*vm ;

        "Standard Volumetric Flow"
        Fvol_std = Inlet.F*vm_std ;

        "Mass Fraction"
        zmass = M*Inlet.z / Mw;
        
        "Overall Entropy"
        s = (1-v)*PP.LiquidEntropy(Inlet.T, Inlet.P, x) +
                v*PP.VapourEntropy(Inlet.T, Inlet.P, y);
        
        "Temperature in °C"
        T_Cdeg = Inlet.T - 273.15 * 'K';

end

Model simple_sink
        ATTRIBUTES
        Pallete = true;
        Icon = "icon/Sink";
        Brief = "Simple material stream sink";
        Info = "
        This model should be used for boundary streams when no additional
        information about the stream is desired.
        ";
        
        VARIABLES
        in Inlet                as stream       (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Symbol="_{in}");
end

Model energy_stream
        ATTRIBUTES
        Pallete = false;
        Brief = "General Energy Stream";
        Info =
        "This is the basic building block for the EML models.
        Every model should have input and output energy streams
        derived from this model.";

        VARIABLES
        Q as heat_rate(Brief="Energy rate");
end

Model work_stream
        ATTRIBUTES
        Pallete = false;
        Brief = "General Work Stream";
        VARIABLES
        Work            as power(Brief = "work");
end

Model work_source
        ATTRIBUTES
        Pallete = true;
        Icon = "icon/work_source";
        Brief = "Work stream source";

        VARIABLES
        out OutletWork          as work_stream (Brief = "Outlet work stream", PosX=1, PosY=0.46, Symbol="_{out}");

end

Model work_sink
        ATTRIBUTES
        Pallete = true;
        Icon = "icon/work_sink";
        Brief = "Work stream sink";

        VARIABLES
        in InletWork            as work_stream (Brief = "Inlet work stream", PosX=0, PosY=0.46, Symbol="_{in}");

end

Model energy_source
        ATTRIBUTES
        Pallete = true;
        Icon = "icon/energy_source";
        Brief = "Enegry stream source";

        VARIABLES
        out OutletQ             as energy_stream (Brief = "Outlet energy stream", PosX=1, PosY=0.46, Symbol="_{out}");
end

Model energy_sink
        ATTRIBUTES
        Pallete = true;
        Icon = "icon/energy_sink";
        Brief = "Enegry stream sink";

        VARIABLES
        in InletQ               as energy_stream (Brief = "Inlet energy stream", PosX=0, PosY=0.46, Symbol="_{in}");
end

Model sourceNoFlow

ATTRIBUTES
        Pallete = true;
        Icon = "icon/SourceNoFlow";
        Brief = "Simple Material stream source with no flow.";
        Info = "
        This model should be used for boundary streams.
        Usually these streams are known and come from another process
        units.";

PARAMETERS
        outer PP                                as Plugin                       (Brief = "External Physical Properties", Type="PP");
        outer NComp             as Integer                      (Brief = "Number of chemical components", Lower = 1); 

VARIABLES

        out Outlet                      as stream                       (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}",Protected=true);

EQUATIONS

"Stream Molar Composition"
        Outlet.z = 1/NComp;

"Stream Molar Enthalpy"
        Outlet.h = 0 * 'J/mol';

"Stream Temperature"
        Outlet.T = 300 * 'K'; 

"Stream Molar Flow"
        Outlet.F = 0 * 'kmol/h';

"Stream Pressure"
        Outlet.P = 1 * 'atm';

"Stream Vapour Fraction"
        Outlet.v = 0;

end

Model info_stream
        
ATTRIBUTES
        Pallete = true;
        Icon = "icon/Info_Stream";
        Brief = "Material stream information";
        Info = "
        This model should be used for middle streams when additional
        information about the stream is desired.

        Some of the additional informations calculated by this models are:
         * Mass density
         * Mass flow
         * Mass compostions
         * Specific volume
         * Vapour fraction
         * Volumetric flow
         * Liquid and Vapour compositions
         * Viscosity
         * Heat Capacity
         * Thermal Conductivity
         * Temperature in Celsius Degrees
        ";

PARAMETERS
        outer PP                        as Plugin                       (Brief = "External Physical Properties", Type="PP");
        outer NComp     as Integer                      (Brief = "Number of chemical components", Lower = 1); 
                  M(NComp)      as molweight    (Brief = "Component Mol Weight");
        
SET

        M   = PP.MolecularWeight();
        
VARIABLES

        in      Inlet           as stream               (Brief = "Inlet Stream", PosX=0, PosY=0.5308, Protected=true , Symbol="_{in}");
        out     Outlet          as stream               (Brief = "Outlet Stream", PosX=1, PosY=0.5308, Protected=true , Symbol="_{out}");
        
        v                                                       as fraction                     (Brief = "Vapourization fraction",Hidden=true);
        x(NComp)                        as fraction                     (Brief = "Liquid Molar Fraction",Hidden=true);
        y(NComp)                        as fraction                     (Brief = "Vapour Molar Fraction",Hidden=true);
        
        F(NComp)        as flow_mol             (Brief = "Component Molar Flow",Protected=true);
        FwTotal         as flow_mass            (Brief = "Total Mass Flow",Protected=true);
        Fw(NComp)               as flow_mass            (Brief = "Component Mass Flow",Protected=true);
        FvolTotal           as flow_vol         (Brief = "Total Volumetric Flow",Protected=true);
        T_Cdeg                          as temperature          (Brief = "Temperature in °C", Lower=-200,Protected=true);

        Mu      as viscosity            (Brief="Stream Viscosity",Lower=0.0001, Symbol = "\mu",Protected=true);
        Cp              as cp_mol                       (Brief="Stream Molar Heat Capacity", Upper=1e10,Protected=true);        
        K               as conductivity         (Brief="Stream Thermal Conductivity", Default=1.0, Lower=1e-5, Upper=500,Protected=true);
        Mw                                              as molweight            (Brief = "Average Mol Weight",Protected=true);
        vm              as volume_mol   (Brief = "Molar Volume",Protected=true);        
        rho             as dens_mass            (Brief = "Stream Mass Density",Protected=true);
        rhom    as dens_mol             (Brief = "Stream Molar Density",Protected=true);
        s               as entr_mol             (Brief = "Stream Entropy",Protected=true);
        zmass(NComp) as fraction                        (Brief = "Mass Fraction",Protected=true);
        
EQUATIONS

"Flash Calculation"
        [v, x, y] = PP.FlashPH(Inlet.P, Inlet.h, Inlet.z);
        
"Average Molecular Weight"
        Mw = sum(M*Inlet.z);

"Mass Density"
        rho * ((1-v)/PP.LiquidDensity(Inlet.T,Inlet.P,x) + v/PP.VapourDensity(Inlet.T,Inlet.P,y)) = 1;
        
"Mass or Molar Density"
        rhom * Mw = rho;

"Total Flow Mass"
        FwTotal =  Mw*Inlet.F;

"Component Flow Mass"
        Fw      =  FwTotal*zmass;

"Molar Volume"
        vm = (1-v)*PP.LiquidVolume(Inlet.T, Inlet.P, x) + v*PP.VapourVolume(Inlet.T,Inlet.P,y);
        
"Total Volumetric Flow"
        FvolTotal = Inlet.F*vm ;
        
"Mass Fraction"
        zmass = M*Inlet.z / Mw;

"Stream Heat Capacity"
        Cp      =       (1-v)*PP.LiquidCp(Inlet.T, Inlet.P, x) + v*PP.VapourCp(Inlet.T,Inlet.P,y);

"Stream Viscosity"
        Mu      =       (1-v)*PP.LiquidViscosity(Inlet.T, Inlet.P, x) + v*PP.VapourViscosity(Inlet.T,Inlet.P,y);

"Stream ThermalConductivity"
        K       =       (1-v)*PP.LiquidThermalConductivity(Inlet.T, Inlet.P, x) + v*PP.VapourThermalConductivity(Inlet.T,Inlet.P,y);

"Stream Overall Entropy"
        s = (1-v)*PP.LiquidEntropy(Inlet.T, Inlet.P, x) + v*PP.VapourEntropy(Inlet.T, Inlet.P, y);
        
"Temperature in °C"
        T_Cdeg = Inlet.T - 273.15 * 'K';

"Outlet Flow"
        Outlet.F = Inlet.F;

"Component Molar Flow"
        F = Inlet.F*Inlet.z;

"Outlet Temperature"
        Outlet.T = Inlet.T;

"Outlet Pressure"
        Outlet.P = Inlet.P;

"Outlet Vapour Fraction"
        Outlet.v = Inlet.v;

"Outlet Enthalpy"
        Outlet.h = Inlet.h;

"Outlet Composition"
        Outlet.z= Inlet.z;
end