#*-------------------------------------------------------------------
* 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: Núbia do Carmo Ferreira
* $Id: sample_reboiler.mso 247 2007-04-24 13:44:18Z rafael $
*--------------------------------------------------------------------*#
using "costs/reboiler_cost";

FlowSheet sample_reboiler_cost
	
	PARAMETERS
	PP	as Plugin(Brief="Physical Properties",
		Type="PP",
		Components = [ "isobutane", "benzene"],
		LiquidModel = "PR",
		VapourModel = "PR"
	);
	NComp	as Integer;

	SET
	NComp = PP.NumberOfComponents;
	
	DEVICES
	reb 	as reboiler_cost;
	feed 	as stream;
	bot		as source; # coming from bottom of a column
	Q 		as energy_source;

	CONNECTIONS
	feed to reb.Inlet;
	bot.Outlet to reb.InletL;
	Q.OutletQ to reb.InletQ;
	
	SPECIFY
	feed.F = 0 * 'kmol/h'; # no feed
	feed.T = 328 * 'K';
	feed.P = 180 * 'kPa';
	feed.z = [0.5, 0.5];
	feed.v = 0;
	feed.h = 0 * 'kJ/kmol';

	bot.P = 185 * 'kPa';
	bot.T = 327.7 * 'K';
	bot.F = 180 * 'kmol/h';
	bot.Composition = [0.006061, 0.9939];
	
	reb.OutletL.F = 68.4 * 'kmol/h';
	reb.OutletV.F = 111.6 * 'kmol/h';

	Q.OutletQ = 3.7743e6 * 'kJ/h';

	SET
	reb.V = 2 * 'm^3';
	reb.Across = 1 * 'm^2';
	
	# costs
	reb.Material = "Stainless steel 316";

	reb.Cost(1,:) = [8.202,0.01506,0.06811];
	reb.Cost(2,:) = [-0.9003,0.0906,0];
	reb.Cost(3,:) = [1.35,0,0];
	reb.Cost(4,:) = [-0.7844,0.0830,0];
	reb.Cost(5,:) = [0.8955,0.04981,0];
	reb.Cost(6,:) = [1.2002,0.07140,0];
	reb.Cost(7,:) = [1.4272,0.12088,0];
	reb.Cost(8,:) = [0.8608,0.23296,0];
	
	INITIAL
	reb.OutletL.T = 320 *'K';
	reb.Level = 1 * 'm';
	reb.OutletL.z(2) = 0.9;
	
	OPTIONS
	TimeEnd = 1000;
	TimeStep = 20;
end