source: branches/gui/eml/mixers_splitters/splitter.mso

#*-------------------------------------------------------------------
* 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.
*
*----------------------------------------------------------------------
* Author: Maurício Carvalho Maciel, Paula B. Staudt, Rafael P. Soares
* $Id: splitter.mso 910 2010-02-20 03:24:41Z arge $
*--------------------------------------------------------------------*#


using "streams";

Model splitter_n
        ATTRIBUTES
        Pallete         = false;
        Icon            = "icon/splitter_n"; 
        Brief           = "Model of a splitter (NOT Handled by the GUI)";
        Info            =
"== Assumptions ==
* thermodynamics equilibrium
* adiabatic
                        
== Specify ==
* the inlet stream
* (Noutlet - 1) fraction of split of the outlet streams:

        frac(i) = (Mole Flow of the outlet stream i / 
                                Mole Flow of the inlet stream)
                                where i = 1, 2,...,Noutlet
";
        
        PARAMETERS
        NOutlet as Integer (Brief = "Number of Outlet Streams", Lower = 1);
        
        VARIABLES
in      Inlet   as stream (Brief = "Inlet stream", PosX=0, PosY=0.5001, Symbol="_{in}");
out Outlet(NOutlet)  as stream (Brief = "Outlet streams", PosX=1, PosY=0.5, Symbol="_{out}");
        frac(NOutlet) as fraction (Brief = "Distribution of Outlets", Default=0.5, Symbol="\phi");

        EQUATIONS
        
        sum(frac) = 1;
        
        for i in [1:NOutlet] do
                
                "Flow"
                Outlet(i).F = Inlet.F*frac(i);
                
                "Composition"
                Outlet(i).z = Inlet.z;
        
                "Pressure"
                Outlet(i).P = Inlet.P;
        
                "Enthalpy"
                Outlet(i).h = Inlet.h;
        
                "Temperature"   
                Outlet(i).T = Inlet.T;
         
                "Vapourisation Fraction"
                Outlet(i).v = Inlet.v;
        end

end

Model splitter2
        ATTRIBUTES
        Pallete         = true;
        Icon            = "icon/splitter_column"; 
        Brief           = "Splitter with 2 outlet streams";
        Info            =
"== Assumptions ==
*Thermodynamics equilibrium
*Adiabatic
                        
== Specify ==
* The inlet stream
* One FlowRatios of split of the outlet streams:

        FlowRatios(i) = (Mole Flow of the outlet stream i / 
                                Mole Flow of the inlet stream)
                                where i = 1, 2
";

VARIABLES
in  Inlet   as stream (Brief = "Inlet stream", PosX=0.5, PosY=0, Symbol="_{in}");
out Outlet1 as stream (Brief = "Outlet stream 1", PosX=0.25, PosY=1, Symbol="_{out1}");
out Outlet2 as stream (Brief = "Outlet stream 2", PosX=0.75, PosY=1, Symbol="_{out2}");
        FlowRatios(2)   as fraction     (Brief = "Distribution of Outlets", Default=0.33, Symbol="\phi");

EQUATIONS

"Normalize Flow Ratios" 
        sum(FlowRatios) = 1;
        
"Flow"
        Outlet1.F = Inlet.F * FlowRatios(1);
        Outlet1.F + Outlet2.F = Inlet.F;

"Composition"
        Outlet1.z = Inlet.z;
        Outlet2.z = Inlet.z;

"Pressure"
        Outlet1.P = Inlet.P;
        Outlet2.P = Inlet.P;

"Enthalpy"
        Outlet1.h = Inlet.h;
        Outlet2.h = Inlet.h;

"Temperature"
        Outlet1.T = Inlet.T;
        Outlet2.T = Inlet.T;

"Vapourisation Fraction"
        Outlet1.v = Inlet.v;
        Outlet2.v = Inlet.v;

end

Model splitter3
        ATTRIBUTES
        Pallete         = true;
        Icon            = "icon/splitter"; 
        Brief           = "Model of a splitter with 3 outlet streams";
        Info            =
"== Assumptions ==
* Thermodynamics equilibrium
* Adiabatic
                        
== Specify ==
*The inlet stream
*Two FlowRatios of split of the outlet streams:

        FlowRatios(i) = (Mole Flow of the outlet stream i / 
                                Mole Flow of the inlet stream)
                                where i = 1, 2, 3
";
        
VARIABLES

in      Inlet                           as stream       (Brief = "Inlet stream", PosX=0, PosY=0.5001, Symbol="_{in}");
out  Outlet1    as stream       (Brief = "Outlet stream 1", PosX=1, PosY=0.25, Symbol="_{Out1}");
out  Outlet2    as stream       (Brief = "Outlet stream 2", PosX=1, PosY=0.5059, Symbol="_{Out2}");
out  Outlet3    as stream       (Brief = "Outlet stream 3", PosX=1, PosY=0.75, Symbol="_{Out3}");

        FlowRatios(3)   as fraction     (Brief = "Distribution of Outlets", Default=0.33, Symbol="\phi");

EQUATIONS
        
"Normalize Flow Ratios" 
        sum(FlowRatios) = 1;
        
"Outlet1 Flow"
        Outlet1.F = Inlet.F*FlowRatios(1);
        
"Outlet2 Flow"
        Outlet2.F = Inlet.F*FlowRatios(2);
        
"Outlet3 Flow"
        Outlet3.F = Inlet.F*FlowRatios(3);
        
"Outlet1 Composition"
        Outlet1.z = Inlet.z;

"Outlet2 Composition"
        Outlet2.z = Inlet.z;

"Outlet3 Composition"
        Outlet3.z = Inlet.z;

"Outlet1 Pressure"
        Outlet1.P = Inlet.P;

"Outlet2 Pressure"
        Outlet2.P = Inlet.P;

"Outlet3 Pressure"
        Outlet3.P = Inlet.P;

"Outlet1 Enthalpy"
        Outlet1.h = Inlet.h;

"Outlet2 Enthalpy"
        Outlet2.h = Inlet.h;

"Outlet3 Enthalpy"
        Outlet3.h = Inlet.h;
        
"Outlet1 Temperature"   
        Outlet1.T = Inlet.T;

"Outlet2 Temperature"   
        Outlet2.T = Inlet.T;

"Outlet3 Temperature"   
        Outlet3.T = Inlet.T;

"Outlet1 Vapourisation Fraction"
        Outlet1.v = Inlet.v;

"Outlet2 Vapourisation Fraction"
        Outlet2.v = Inlet.v;
        
"Outlet3 Vapourisation Fraction"
        Outlet3.v = Inlet.v;

end

Model splitter_column

ATTRIBUTES
        Pallete         = true;
        Icon            = "icon/splitter_column"; 
        Brief           = "Splitter with 2 outlet streams to be used with column section model";
        Info            =
"== Assumptions ==
*Thermodynamics equilibrium
*Adiabatic

== Specify ==
* The inlet stream
* One Split Flow of the outlet stream:
**SplitFlow_RefluxStream: split of the outlet Reflux stream
**SplitFlow_DistillateStream: split of the outlet Distillate stream

OR

* The inlet stream and the RefluxRatio
";

VARIABLES
        in  Inlet       as stream (Brief = "Inlet stream", PosX=0.5, PosY=0, Symbol="_{in}");
        out Reflux              as stream (Brief = "Reflux stream", PosX=0.25, PosY=1, Symbol="_{reflux}");
        out Distillate  as stream (Brief = "Distillate stream", PosX=0.75, PosY=1, Symbol="_{distillate}");

        SplitFlow_RefluxStream  as fraction     (Brief = "split of the outlet Reflux stream", Default=0.33);
        SplitFlow_DistillateStream      as fraction     (Brief = "split of the outlet Distillate stream", Default=0.33);
        RefluxRatio             as positive     (Brief = "Reflux Ratio", Default=10, Lower = 0.05);

EQUATIONS

"Reflux Ratio"  
        #Reflux.F*RefluxRatio = SplitFlow_RefluxStream*(Reflux.F*RefluxRatio + Reflux.F);
        SplitFlow_RefluxStream*(1 + RefluxRatio) = RefluxRatio;
        
"Normalize Flow Ratios" 
        SplitFlow_RefluxStream + SplitFlow_DistillateStream = 1;
        
"Flow"
        Reflux.F = Inlet.F * SplitFlow_RefluxStream;
        Inlet.F = Reflux.F + Distillate.F;

"Composition"
        Reflux.z = Inlet.z;
        Distillate.z = Inlet.z;

"Pressure"
        Reflux.P = Inlet.P;
        Distillate.P = Inlet.P;

"Enthalpy"
        Reflux.h = Inlet.h;
        Distillate.h = Inlet.h;

"Temperature"
        Reflux.T = Inlet.T;
        Distillate.T = Inlet.T;

"Vapourisation Fraction"
        Reflux.v = Inlet.v;
        Distillate.v = Inlet.v;

end