#*-------------------------------------------------------------------
* 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 flash and flashSteady
*--------------------------------------------------------------------
* 
* This sample file needs VRTherm (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
* Author: Paula B. Staudt
* $Id: sample_flash.mso 633 2008-09-24 00:26:30Z bicca $
*--------------------------------------------------------------------*#
using "stage_separators/flash";

# exemplo baseado nos dados do artigo do Gani 1985.
FlowSheet flash_Test
	PARAMETERS
	PP as Plugin(Brief="Physical Properties",
		Type="PP",
		Components = ["1,3-butadiene", "isobutene", "n-pentane",
			"1-pentene", "1-hexene", "benzene"],
		LiquidModel = "PR",
		VapourModel = "PR"
	);
	NComp as Integer;

	VARIABLES
	Q	as energy_source (Brief="Heat supplied");
	
	SET
	NComp = PP.NumberOfComponents;
	
	DEVICES
	fl as flash;
	s1 as source;
	
	CONNECTIONS
	s1.Outlet to fl.Inlet;
	Q.OutletQ to fl.InletQ;
	
	EQUATIONS
	fl.OutletLiquid.F = 400*sqrt(fl.Geometry.Level/'m') * 'kmol/h';
	
	SPECIFY
	s1.F = 496.3 * 'kmol/h';
	s1.T = 338 * 'K';
	s1.P = 507.1 * 'kPa';
	s1.Composition = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283];

	fl.OutletVapour.F = 68.5 * 'kmol/h';
	Q.OutletQ = 0 * 'kJ/h';
	
	SET
	fl.Geometry.Lenght = 10 * 'm';
	fl.Geometry.Diameter = 2 * 'm';
	fl.Geometry.Orientation = "vertical";
#	fl.Geometry.Orientation = "horizontal";

	INITIAL
	fl.OutletLiquid.T = 338 * 'K';
	fl.Geometry.Level = 0.4 * 'm';
	fl.OutletLiquid.z([1:5]) = 0.1;
	
	OPTIONS
	Dynamic = true;
	TimeStep = 0.1;
	TimeEnd = 5;
	TimeUnit = 'h';
end

# exemplo baseado nos dados do artigo do Gani 1985.
FlowSheet flashSteady_Test
	PARAMETERS
	PP as Plugin(Brief="Physical Properties",
		Type="PP",
		Components = ["1,3-butadiene", "isobutene", "n-pentane",
			"1-pentene", "1-hexene", "benzene"],
		LiquidModel = "PR",
		VapourModel = "PR"
	);
	NComp as Integer;

	VARIABLES
	Q	as energy_source (Brief="Heat supplied");
	
	SET
	NComp = PP.NumberOfComponents;
	
	DEVICES
	fl as flash_steady;
	s1 as source;
	
	CONNECTIONS
	s1.Outlet to fl.Inlet;
	Q.OutletQ to fl.InletQ;
	
	SPECIFY
	s1.F = 496.3 * 'kmol/h';
	s1.T = 338 * 'K';
	s1.P = 507.1 * 'kPa';
	s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283];
	
	fl.OutletLiquid.P = 2.5 * 'atm';

	#Q.OutletQ = 0 * 'kJ/h';
	fl.OutletLiquid.T = 315.06 * 'K';
	
	OPTIONS
	Dynamic = false;	
end


CaseStudy caseFlash as flashSteady_Test

	VARY

	s1.F = [496.3, 496.31]*'kmol/h';

	RESPONSE


	fl.OutletVapour.F'kmol/h';

end

CaseStudy caseFlash2 as flashSteady_Test

	VARY

	s1.Composition(1) = [ 0.2379, 0.3 ,  0.35];
	s1.F = [496.3, 496.31]*'kmol/h';

RESPONSE

	fl.OutletVapour.z(1);
	fl.OutletVapour.F'kmol/h';

end