#*-------------------------------------------------------------------
* 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 247 2007-04-24 13:44:18Z rafael $
*--------------------------------------------------------------------*#

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;

SPECIFY
	Stream.Outlet.F = 30 * 'kmol/h';
	Stream.Outlet.P = 120 * 'kPa';
	Stream.Outlet.T = 290 * 'K';
	Stream.Outlet.z = [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;

	SPECIFY
	Stream.Outlet .F = 30 * 'kmol/h';
	Stream.Outlet .P = 120 * 'kPa';
	Stream.Outlet .T = 290 * 'K';
	Stream.Outlet .z = [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