source: trunk/eml/pressure_changers/compressor.mso @ 442

#*-------------------------------------------------------------------
* 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: Marcos L. Alencastro,  Estefane S. Horn
* $Id: compressor.mso 393 2007-10-17 23:50:09Z arge $
*--------------------------------------------------------------------*#

using "streams";

Model centrifugal_compressor
        ATTRIBUTES
        Pallete         = true;
        Icon            = "icon/CentrifugalCompressor"; 
        Brief           = "Model of a centrifugal compressor.";
        Info            =
"== Assumptions ==
* Steady State;
* Only Vapor;
* Adiabatic.
        
== Specify == 
* the inlet stream;
* the outlet pressure (Outlet.P);
* the Isentropic efficiency (Effs).
";
        
        PARAMETERS
outer PP                as Plugin               (Brief = "External Physical Properties", Type="PP");
outer NComp     as Integer              (Brief = "Number of chemical components", Lower = 1);
        R                       as positive     (Default = 8.31451, Brief = "Constant of Gases", Unit= 'kJ/kmol/K');
        Mw(NComp)       as molweight    (Brief = "Molar Weight");

        VARIABLES
        n                       as positive             (Brief = "Politropic Coefficient", Lower=0);
        k                       as positive     (Brief = "Isentropic Coefficient", Lower=1e-3); 
        Cp              as cp_mol               (Brief = "Heat Capacity");
        Cv                      as cv_mol               (Brief = "Heat Capacity");
        Pratio          as positive             (Brief = "Pressure Ratio", Symbol ="P_{ratio}");        
        Pdrop           as press_delta  (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P");
        Wp                      as energy_mol   (Brief = "Politropic Head");
        Ws                      as energy_mol   (Brief = "Isentropic Head");
        Tiso            as temperature  (Brief = "Isentropic Temperature"); 
        Effp            as positive     (Brief = "Politropic efficiency");
        Effs            as efficiency   (Brief = "Isentropic efficiency");
        FPower          as power                (Brief = "Fluid Power");
        Mwm                     as molweight    (Brief = "Mixture Molar Weight");
in      Inlet           as stream               (Brief = "Inlet stream", PosX=0, PosY=0.5086, Symbol="_{in}");
out     Outlet          as streamPH             (Brief = "Outlet stream", PosX=1, PosY=0.5022, Symbol="_{out}");

        SET
        Mw = PP.MolecularWeight();
        
        EQUATIONS
        
        "Calculate Mwm for Inlet Mixture"
        Mwm = sum(Mw*Inlet.z);

        "Pressure Ratio"
        Outlet.P = Inlet.P * Pratio;

        "Pressure Drop"
        Outlet.P  = Inlet.P - Pdrop;

        "Calculate Cp Using a External Physical Properties Routine"
        Cp = PP.VapourCp(Inlet.T,Inlet.P,Inlet.z);
        
        "Calculate Cv Using a External Physical Properties Routine"
        Cv = PP.VapourCv(Inlet.T,Inlet.P,Inlet.z);
        
        "Calculate Isentropic Coeficient"
        k * Cv = Cp;
        
        "Calculate Isentropic Head"
        Ws = (k/(k-1))*R*Inlet.T*((Outlet.P/Inlet.P)^((k-1)/k) - 1);
        
        "Calculate Isentropic Outlet Temperature"
#       Tiso = Inlet.T * (Outlet.P/Inlet.P)^((k-1)/k);
        PP.VapourEntropy(Tiso, Outlet.P, Outlet.z) = 
                PP.VapourEntropy(Inlet.T, Inlet.P, Inlet.z);

        "Calculate Real Outlet Temperature"
        Effs * (Outlet.T- Inlet.T) = (Tiso - Inlet.T);
        
        "Calculate Politropic Coefficient"
        n*(ln(Outlet.T/Inlet.T)) = (n-1)*(ln(Outlet.P/Inlet.P));
        
        "Calculate Politropic Efficiency"
        Effp * (n-1) * k = n * (k-1);
        
        "Calculate Politropic Head"
        Ws*Effp = Wp*Effs;

        "Calculate Fluid Power"
        FPower*Effs = Inlet.F*Ws;
        
        "Overall Molar Balance"
        Outlet.F = Inlet.F;

        "Component Molar Balance"
        Outlet.z = Inlet.z;
end