source: trunk/sample/stage_separators/sample_reboiler.mso @ 335

#*-------------------------------------------------------------------
* 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 reboilers model
*--------------------------------------------------------------------
* 
* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
* Author: Paula B. Staudt
* $Id: sample_reboiler.mso 313 2007-07-14 16:45:55Z arge $
*--------------------------------------------------------------------*#
using "stage_separators/reboiler";

FlowSheet reboiler_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
        r1 as reboiler;
        feed as stream;
        s1 as source;

        CONNECTIONS
        feed to r1.Inlet;
        s1.Outlet to r1.InletL;
        Q.OutletQ to r1.InletQ;
        
        SPECIFY
        feed.F = 0 * 'kmol/h';
        feed.T = 328 * 'K';
        feed.P = 180 * 'kPa';
        feed.z = [0.5, 0.5];
        feed.v = 0;
        feed.h = 0 * 'kJ/kmol';

        s1.Outlet.P = 185 * 'kPa';
        s1.Outlet.T = 327.7 * 'K';
        s1.Outlet.F = 180 * 'kmol/h';
        s1.Outlet.z = [0.006061, 0.9939];
        
        r1.OutletL.F = 68.4 * 'kmol/h';
        r1.OutletV.F = 111.6 * 'kmol/h';

        Q.OutletQ.Q = 3.7743e6 * 'kJ/h';

        SET
        r1.V = 2 * 'm^3';
        r1.Across = 1 * 'm^2';
        
        INITIAL
        r1.OutletL.T = 320 *'K';
        r1.Level = 1 * 'm';
        r1.OutletL.z(2) = 0.9;
        
        OPTIONS
        TimeEnd = 1000;
        TimeStep = 20;
end


FlowSheet reboilerSteady_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
        r1 as reboilerSteady;
        s1 as source;

        CONNECTIONS
        s1.Outlet to r1.InletL;
        Q.OutletQ to r1.InletQ;
        
        SPECIFY
        s1.Outlet.P = 185 * 'kPa';
        s1.Outlet.T = 327.7 * 'K';
        s1.Outlet.F = 180 * 'kmol/h';
        s1.Outlet.z = [0.006061, 0.9939];
        
#       Q.OutletQ.Q = 3.7743e6 * 'kJ/h';
        r1.OutletV.T = 350 * 'K';

        SET
        r1.DP = 10 * 'kPa';
        
        OPTIONS
        Dynamic = false;
end