#*-------------------------------------------------------------------
* 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 213 2007-03-15 19:40:55Z rafael $
*--------------------------------------------------------------------*#
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 heat_rate (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 to r1.Q;
	
	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 = 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
	RelativeAccuracy = 1e-5;
	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 heat_rate (Brief="Heat supplied");

	SET
	NComp = PP.NumberOfComponents;
	
	DEVICES
	r1 as reboilerSteady;
	s1 as source;

	CONNECTIONS
	s1.Outlet to r1.InletL;
	Q to r1.Q;
	
	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 = 3.7743e6 * 'kJ/h';
	r1.OutletV.T = 350 * 'K';

	SET
	r1.DP = 10 * 'kPa';
	
	OPTIONS
	RelativeAccuracy = 1e-5;
	Dynamic = false;
end