source: trunk/eml/reactors/pfr.mso @ 233

#*-------------------------------------------------------------------
* 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 Generic PFR with constant mass holdup
*--------------------------------------------------------------------
*
*       - Requires the information of:
*                * Reaction values
*                * Heat of reaction
*                * Pressure profile
*
*----------------------------------------------------------------------
* Author: Rafael de P. Soares and Paula B. Staudt
* $Id: pfr.mso 194 2007-03-07 19:38:30Z rafael $
*--------------------------------------------------------------------*#

using "streams";

Model pfr

ATTRIBUTES
        Pallete         = true;
        Brief           = "Brief";
        Info            =
        "write some information";

PARAMETERS

outer PP                                                        as Plugin               (Brief = "External Physical Properties", Type="PP");
outer   NComp                                           as Integer              (Brief="Number of components");
                NReac                                           as Integer              (Brief="Number of reactions");
                stoic(NComp, NReac)     as Real                         (Brief = "Stoichiometric Matrix");
                NDisc                                           as Integer              (Brief="Number of points of discretization", Default=10);
                Mw(NComp)                               as molweight    (Brief="Component Mol Weight");
                L                                                               as length               (Brief="Reactor Length");
                Across                                          as area                 (Brief="Cross section area");

SET
        
        Mw   = PP.MolecularWeight();

VARIABLES

in              Inlet   as stream       (Brief = "Inlet Stream");
out     Outlet  as stream       (Brief = "Outlet Stream");

        str(NDisc+1) as streamPH;
        vel(NDisc+1) as velocity;
        vol(NDisc+1) as vol_mol;
        rho(NDisc+1) as dens_mass;
        
        q(NDisc)                                as heat_rate;
        M(NComp, NDisc)         as mol                  (Brief = "Molar holdup");
        Mt(NDisc)                       as mol                  (Brief = "Molar holdup");
        C(NComp, NDisc)         as conc_mol     (Brief="Components concentration", Lower=-1e-6);
        E(NDisc)                                as energy               (Brief="Total Energy Holdup on element");
        r(NReac, NDisc)                 as reaction_mol;
        Hr(NReac, NDisc)        as heat_reaction;

EQUATIONS

"Inlet boundary"
        str(1).F = Inlet.F;
        str(1).T = Inlet.T;
        str(1).P = Inlet.P;
        str(1).z = Inlet.z;

"Outlet boundary"
        Outlet.F = str(NDisc+1).F;
        Outlet.T = str(NDisc+1).T;
        Outlet.P = str(NDisc+1).P;
        Outlet.z = str(NDisc+1).z;
        Outlet.h = str(NDisc+1).h;
        Outlet.v = str(NDisc+1).v;
        
        for z in [1:NDisc]
                for c in [1:NComp-1]
                        "Component Molar Balance"
                        diff(M(c,z)) = (str(z).F*str(z).z(c) - str(z+1).F*str(z+1).z(c))
                                + sum(stoic(c,:)*r(:, z)) * Across*L/NDisc;
                end

                "Energy Balance"
                diff(E(z)) = str(z).F*str(z).h - str(z+1).F*str(z+1).h +
                        sum(Hr(:,z)*r(:,z)) * Across*L/NDisc - q(z);

                "Energy Holdup"
                E(z) = Mt(z)*str(z+1).h - str(z+1).P*Across*L/NDisc;

                "mass flow is considered constant"
                str(z+1).F*vol(z+1) = str(z).F*vol(z); # FIXME: is this correct? No (constant velocity: only for equimolar)
                #rho(z+1)*vel(z+1) = rho(z)*vel(z);  # FIXME: this is correct! But does not converge.
        
                "Molar concentration"
                C(:,z) * Across*L/NDisc = M(:,z);
                
                "Sum of M"
                Mt(z) = sum(M(:,z));
                
                "Geometrical constraint"
                Across*L/NDisc = Mt(z) * vol(z);

                "Molar fraction"
                str(z+1).z * Mt(z) = M(:,z);
        end

        for z in [1:NDisc+1]
                "Specific Volume"
                vol(z) = PP.VapourVolume(str(z).T, str(z).P, str(z).z);
                
                "Specific Mass"
                rho(z) = PP.VapourDensity(str(z).T, str(z).P, str(z).z);

                "Velocity"
                vel(z)*Across = str(z).F*vol(z);
        end
end