source: branches/new_gui/eml/mixers_splitters/sepComp.mso @ 959

#*-------------------------------------------------------------------
* 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
* $Id: sepComp.mso 744 2009-03-06 22:56:26Z bicca $
*--------------------------------------------------------------------*#

using "streams/streams";

Model sepComp_n
        ATTRIBUTES
        Pallete         = false;
        Icon            = "icon/splitter_n"; 
        Brief           = "Model of a separator of components (NOT Handled by the GUI)";
        Info            =
"== Assumptions ==
* thermodynamics equilibrium
* adiabatic

== Specify ==
* the inlet stream
* (NComp - 1) molar fractions to (Noutlet - 1) outlet streams
* (Noutlet - 1) frac (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

                        or

* (Noutlet - 1) recovery (Recovery of the component specified in the outlet stream i):

  recovery(i) = (Mole Flow of the component specified in the Outlet stream i/ 
                                Mole Flow of the component specified in the inlet stream)
                                                where i = 1, 2,...,Noutlet
";
        
PARAMETERS

outer PP                        as Plugin       (Brief = "External Physical Properties", Type="PP");
outer   NComp           as Integer      (Brief = "Number of chemical components", Lower = 1);
                NOutlet         as Integer      (Brief = "Number of Outlet Streams", Lower = 1);
                mainComp        as Integer      (Brief = "Component specified", Default = 1, Lower = 1);
        
VARIABLES

in              Inlet                   as stream (Brief = "Inlet stream", PosX=0, PosY=0.5, Symbol="_{in}");
out     Outlet(NOutlet) as stream (Brief = "Outlet streams", PosX=1, PosY=0.5059, Symbol="_{out}");

        frac(NOutlet)           as fraction (Brief = "Distribution of the Outlet streams", Symbol="\phi");
        recovery(NOutlet)       as fraction (Brief = "Recovery of the component specified", Symbol="\eta");

EQUATIONS
        
"Flow"
        sum(Outlet.F) = Inlet.F;
        
        
for i in [1:NOutlet-1] do

"Mol fraction normalisation"
        sum(Outlet(i).z) = 1;

end
        
        
for i in [1:NComp] do
        
"Composition"
        sum(Outlet.F*Outlet.z(i)) = Inlet.F*Inlet.z(i);
        
end     
        
        
for i in [1:NOutlet] do
        
"Flow"
        Outlet(i).F = Inlet.F*frac(i);
        
"Recovery"
        recovery(i)*Inlet.z(mainComp) = frac(i)*Outlet(i).z(mainComp);
        
"Pressure"
        Outlet(i).P = Inlet.P;
        
"Enthalpy"
        Outlet(i).h = (1-Outlet(i).v)*PP.LiquidEnthalpy(Outlet(i).T, Outlet(i).P, Outlet(i).z) + 
                                Outlet(i).v*PP.VapourEnthalpy(Outlet(i).T, Outlet(i).P, Outlet(i).z);
        
"Temperature"   
        Outlet(i).T = Inlet.T;

"Vapourization Fraction"
        Outlet(i).v = PP.VapourFraction(Outlet(i).T, Outlet(i).P, Outlet(i).z);
        
end

end

Model sepComp
        ATTRIBUTES
        Pallete         = true;
        Icon            = "icon/SepComp"; 
        Brief           = "Model of a separator of components";
        Info            =
"== Assumptions ==
* thermodynamics equilibrium
        
== Specify ==
* the inlet stream
* (NComp) Overhead_Splits or (NComp) Bottom_Splits 
* the Pressure and Temperature of the outlet streams
";

PARAMETERS

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

in              Inlet                                           as stream               (Brief = "Inlet stream", PosX=0, PosY=0.5001, Symbol="_{Inlet}");
out     Overhead_Outlet         as streamPH     (Brief = "Overhead_Outlet stream", PosX=0.5, PosY=0, Symbol="_{Overhead}");
out     Bottom_Outlet           as streamPH     (Brief = "Bottom_Outlet stream", PosX=0.5, PosY=1, Symbol="_{Bottom}");
in              InletQ                                  as power                (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}");

        Overhead_Splits(NComp)  as fraction     (Brief = "Fraction to Overhead_Outlet", Symbol="\phi_{overhead}");
        Bottom_Splits(NComp)            as fraction     (Brief = "Fraction to Bottom_Outlet", Symbol="\phi_{bottom}");
        
EQUATIONS

"Composition Overhead"
        Overhead_Outlet.F*Overhead_Outlet.z = Inlet.F * Inlet.z*Overhead_Splits;

"Bottom Composition Constraints"
        sum(Bottom_Outlet.z) = 1;

"Sum Of Splits"
        Overhead_Splits+Bottom_Splits = 1;

"Overhead Composition Constraints"
        sum(Overhead_Outlet.z) = 1;

 "Global Composition"
        Overhead_Outlet.F*Overhead_Outlet.z + Bottom_Outlet.F*Bottom_Outlet.z = Inlet.F*Inlet.z;

"Energy Balance"
        Inlet.F*Inlet.h = Overhead_Outlet.F*Overhead_Outlet.h + Bottom_Outlet.F*Bottom_Outlet.h - InletQ;

#"Overhead Pressure"
#       Overhead_Outlet.P = Inlet.P;

#"Bottom Pressure"
#       Bottom_Outlet.P = Inlet.P;

#"Overhead Temperature"
#       Overhead_Outlet.T = Inlet.T;

#"Bottom Temperature"
#       Bottom_Outlet.T = Inlet.T;

end