source: trunk/sample/stage_separators/sample_condenser.mso @ 690

#*-------------------------------------------------------------------
* 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.
*
*--------------------------------------------------------------------
* Sample file for model condenser and condenserSteady
*--------------------------------------------------------------------
* 
* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
* Author: Paula B. Staudt
* $Id: sample_condenser.mso 650 2008-10-01 01:00:48Z arge $
*--------------------------------------------------------------------*#
using "stage_separators/condenser";
using "mixers_splitters/splitter";

# condenser with splitter dividing liquid outlet
FlowSheet condenser_Test
        PARAMETERS
        PP      as Plugin(Brief="Physical Properties",
                Type="PP",
                Components = [ "isobutane", "benzene"],
                LiquidModel = "PR",
                VapourModel = "PR"
        );
        NComp   as Integer;

        VARIABLES
        Q       as energy_source (Brief="Heat supplied");
        
        SET
        NComp = PP.NumberOfComponents;
        
        DEVICES
        c1 as condenser;
        sp as splitter;
        s1 as source;
        
        CONNECTIONS
        s1.Outlet to c1.InletV;
        c1.OutletL to sp.Inlet;
        Q.OutletQ to c1.InletQ;
        
        SPECIFY
        s1.P = 152 * 'kPa';
        s1.T = 298.6 * 'K';
        s1.F = 153 * 'kmol/h';
        s1.Composition = [0.664, 0.336];
        
        sp.frac = 0.444445;
        c1.OutletV.F = 0 * 'kmol/h';
        c1.OutletL.F = 153 * 'kmol/h';

        Q.OutletQ.Q = -3.71e6 * 'kJ/h';

        SET
        c1.V = 2 * 'm^3';
        c1.Across = 1 * 'm^2';

        INITIAL
        c1.OutletL.T = 280 *'K';
        c1.Level = 1 * 'm';
        c1.OutletL.z(1) = 0.65;
        
        OPTIONS
        TimeEnd = 1000;
        TimeStep = 20;
        DAESolver(File="dassl");
end

FlowSheet condenserSteady_Test
        PARAMETERS
        PP      as Plugin(Brief="Physical Properties",
                Type="PP",
                Components = [ "isobutane", "benzene"],
                LiquidModel = "PR",
                VapourModel = "PR"
        );
        NComp   as Integer;

        VARIABLES
        Q       as energy_source (Brief="Heat supplied");
        
        SET
        NComp = PP.NumberOfComponents;
        
        DEVICES
        c1 as condenserSteady;
        s1 as source;
        
        CONNECTIONS
        s1.Outlet to c1.InletV;
        Q.OutletQ to c1.InletQ;
        
        SPECIFY
        s1.P = 152 * 'kPa';
        s1.T = 298.6 * 'K';
        s1.F = 153 * 'kmol/h';
        s1.Composition = [0.664, 0.336];

        Q.OutletQ.Q = 3.71e6 * 'kJ/h';
        c1.DP = 100 * 'kPa';

        OPTIONS
        Dynamic = false;
end