source: mso/eml/pressure_changers/turbine.mso @ 78

#*-------------------------------------------------------------------
* 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 a Hidraulic Turbine
*--------------------------------------------------------------------
*
*       - Assumptions
*               * Steady State
*               * Only Liquid
*               * Adiabatic
*               * Isentropic
*
*----------------------------------------------------------------------
* Authors: Andrey Copat, Estefane S. Horn, Marcos L. Alencastro
* $Id: turbine.mso 77 2006-12-08 19:21:59Z paula $
*--------------------------------------------------------------------*#

using "streams";
using "pressure_changers/flux_machine_basic";

Model Hidraulic_Turbine as flux_machine_basic

        PARAMETERS
ext NComp       as Integer                      (Brief = "Number of chemical components", Lower = 1);
ext PP                  as CalcObject           (Brief = "External Physical Properties");
        Mw(NComp)       as molweight            (Brief = "Molar Weight");
        Eff     as positive                     (Default = 0.72, Brief = "Pump efficiency");
        Meff    as positive                     (Default = 1.0, Brief = "Brake efficiency");
        Beta    as positive                     (Default = 0, Brief = "Volumetric expansivity", Unit = "1/K");
        
        
        VARIABLES
        Head    as head                         (Brief = "Head Developed");
        FPower  as power                        (Brief = "Fluid Power");
        BPower  as power                        (Brief = "Brake Power");
        EPower  as power                        (Brief = "Eletrical Potency");
        Pdiff   as press_delta          (Brief = "Pressure Increase");
        Pratio  as positive                     (Brief = "Pressure Ratio");     
        Mwm     as molweight            (Brief = "Mixture Molar Weight");
        rho             as dens_mass            (Brief = "Specific Mass", Unit="kg/m^3");
        Cp              as cp_mol                       (Brief = "Heat Capacity");
        
        SET
        Mw = PP.MolecularWeight();      
        
        EQUATIONS
        #Mixtures Properties
        "Calculate Mwm for Inlet Mixture"
        Mwm = sum(Mw([1:NComp])*Inlet.z([1:NComp]));
        
        "Calculate rho using a External Physical Properties Routine"
        rho = PP.LiquidDensity(Inlet.T,Inlet.P,Inlet.z);
        
        "Calculate Outlet Vapour Fraction"
        Outlet.v = PP.VapourFraction(Outlet.T, Outlet.P, Outlet.z);
        
        "Calculate Cp Using a External Physical Properties Routine"
        Cp = PP.LiquidCp(Inlet.T,Inlet.P,Inlet.z);
        
        #Mass and Energy Balance and Turbine Equations
        "Calculate Outlet Stream Pressure"
        Outlet.P = Inlet.P + Pdiff;
        
        "Pratio Definition"
        Outlet.P = Inlet.P * Pratio;
        
        "Calculate Fluid Power"
        FPower = Pdiff * Inlet.F / (rho/Mwm);
        
        "Calculate Brake Power"
        BPower = FPower * Eff;
        
        "Calculate Eletric Power"
        EPower = BPower * Meff;
        
        "Calculate Outlet Temperature"
        (Outlet.T - Inlet.T)*Cp = (Outlet.h - Inlet.h) -  Pdiff /(rho/Mwm) * (1-Beta*Inlet.T);
        
        "Calculate Outlet Enthalpy"
        Outlet.h - Inlet.h =  Pdiff / (rho/Mwm);
        
        "Molar Balance"
        Outlet.F = Inlet.F;
        
        "Calculate Outlet Composition"
        Outlet.z = Inlet.z;

        "Calculate Head"
        Head = Pdiff/rho;

end