#*-------------------------------------------------------------------
* 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 80 2006-12-08 19:46:22Z paula $
*--------------------------------------------------------------------*#

using "mixers_splitters/sepComp";

FlowSheet Sample_sepComp_n
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp as Integer;
	
	DEVICES
	stream as stream_therm;
	sep as sepComp_n;
	
	CONNECTIONS
	stream to sep.Inlet;
	
	SET
	PP.Components = [ "isobutane", "benzene"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	sep.mainComp = 1;
	sep.NOutlet = 3;

	SPECIFY
	stream.F = 30 * "kmol/h";
	stream.P = 120 * "kPa";
	stream.T = 290 * "K";
	stream.z = [0.6, 0.4];
	stream.v = 0;
	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
	relativeAccuracy = 1e-7;
	
end


FlowSheet Sample_sepComp
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp as Integer;
	
	DEVICES
	stream as streamTP;
	sep as sepComp;
	
	CONNECTIONS
	stream to sep.Inlet;
	
	SET
	PP.Components = [ "isobutane", "benzene"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	sep.mainComp = 1;

	SPECIFY
	stream.F = 30 * "kmol/h";
	stream.P = 120 * "kPa";
	stream.T = 290 * "K";
	stream.z = [0.6, 0.4];
	sep.Outlet1.z(1) = 0.7;
	sep.frac = 0.4;
#	sep.recovery = 0.533333;

	OPTIONS
	relativeAccuracy = 1e-7;
	
end