#*---------------------------------------------------------------------
* 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 of an yield reactor
*----------------------------------------------------------------------
*
* This sample file needs VRTherm (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
*
* There are three parallel reactions involved:
*	(1) C4H6(1,3-butadiene) + H2 --> C4H8(1-butene)
*	(2) C4H6(1,3-butadiene) + H2 --> C4H8(cis-2-butene)
*	(3) C4H6(1,3-butadiene) + H2 --> C4H8(trans-2-butene)
*
*----------------------------------------------------------------------
* Author: Rodolfo Rodrigues
* $Id$
*--------------------------------------------------------------------*#

using "reactors/yield";


FlowSheet sample_yield
	PARAMETERS
	PP	as Plugin(Brief="Physical properties",
		Type="PP",
		Components = ["1,3-butadiene","hydrogen","1-butene", 
						"cis-2-butene","trans-2-butene"],
		LiquidModel = "PR",
		VapourModel = "PR"
	);
	NComp	as Integer;
	
	DEVICES
	Fin 		as source;
	R 			as yield_vap;

	CONNECTIONS
	Fin.Outlet 	to R.Inlet;
	
	SET
	NComp = PP.NumberOfComponents;
	R.NReac = 3;
	R.KComp = 2;
	
	SPECIFY
	Fin.Outlet.F = 1000*'kmol/h';
	Fin.Outlet.z = [0.25, 0.69, 0.03, 0.02, 0.01];
	Fin.Outlet.P = 10*'kgf/cm^2';
	Fin.Outlet.T = 500*'K';
	
	R.Outlet.F = 300*'kmol/h'*sqrt(R.Tank.Level/'m');
	R.Outlet.P = 10*'kgf/cm^2';
	R.Outlet.T = Fin.Outlet.T;
	R.Q = 0*'W';	
	
	R.yield = [0.6, 1, 0.4, 0.5, 0.05];
	R.Tank.Across = 50000*'cm^2';
	R.Tank.L = 10000*'cm';

	INITIAL
	R.Outletm.T = 500*'K';
	R.M = [75, 50, 10, 5, 2]*'kmol';
	
	OPTIONS
#	Dynamic = false;
	TimeStep = 50;
	TimeEnd = 600;
end