source: trunk/sample/mixers_splitters/sample_sepComp.mso @ 674

#*-------------------------------------------------------------------
* 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 sepComp_n and sepComp
*--------------------------------------------------------------------
* 
* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
* Author: Maurício Carvalho Maciel
* $Id: sample_sepComp.mso 632 2008-09-23 22:20:38Z bicca $
*--------------------------------------------------------------------*#

using "mixers_splitters/sepComp";

FlowSheet Sample_sepComp_n
        
PARAMETERS
        
        PP                      as Plugin       (Brief="Physical Properties",Type="PP",Components = [ "isobutane", "benzene"],
                                                                LiquidModel = "PR",
                                                                VapourModel = "PR");
        NComp   as Integer;
        
DEVICES
        Stream  as source;
        sep             as sepComp_n;
        
CONNECTIONS
        Stream.Outlet to sep.Inlet;
        
SET
        
        NComp = PP.NumberOfComponents;
        
        sep.mainComp = 1;
        sep.NOutlet = 3;
        
        Stream.ValidPhases = "Vapour-Liquid";
        Stream.CompositionBasis = "Molar";

SPECIFY
        Stream.F = 30 * 'kmol/h';
        Stream.P = 120 * 'kPa';
        Stream.T = 290 * 'K';
        Stream.Composition = [0.6, 0.4];
        
        sep.Outlet(1).z(1) = 0.7;
        sep.Outlet(2).z(1) = 0.1;
        sep.frac(1) = 0.4;
        sep.frac(2) = 0.2;
#       sep.recovery(1) = 0.533333;
#       sep.recovery(2) = 0.033333;

OPTIONS
        Dynamic = false;
        NLASolver(
                RelativeAccuracy = 1e-7
        );
end


FlowSheet Sample_sepComp
        PARAMETERS
        PP      as Plugin(Brief="Physical Properties",Type="PP",Components = [ "isobutane", "benzene"],
                                                        LiquidModel = "PR",
                                                        VapourModel = "PR");
        NComp as Integer;
        
        DEVICES
        Stream as source;
        sep as sepComp;
        
        CONNECTIONS
        Stream.Outlet to sep.Inlet;
        
        SET
        
        NComp = PP.NumberOfComponents;
        sep.mainComp = 1;
        
        Stream.ValidPhases = "Vapour-Liquid";
        Stream.CompositionBasis = "Molar";

        SPECIFY
        Stream.F = 30 * 'kmol/h';
        Stream.P = 120 * 'kPa';
        Stream.T = 290 * 'K';
        Stream.Composition = [0.6, 0.4];
        
        sep.Outlet1.z(1) = 0.7;
        sep.frac = 0.4;
#       sep.recovery = 0.533333;

        OPTIONS
        Dynamic = false;
        NLASolver(
                RelativeAccuracy = 1e-7
        );
        
end