#*-------------------------------------------------------------------
* 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 valve (simplified) and valve_linear
*--------------------------------------------------------------------
* 
* This sample file needs VRTherm DEMO (www.vrtech.com.br) to run.
*
*----------------------------------------------------------------------
* Author: Paula B. Staudt, Estefane Horn
* $Id: sample_valve.mso 109 2007-01-11 22:03:27Z arge $
*--------------------------------------------------------------------*#

using "pressure_changers/valve";

FlowSheet valve_Test_V
# with vapour conditions
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp	as Integer;

	SET
	PP.Components = [ "isobutane", "benzene"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	
	DEVICES
	v1 as valve;
	s1 as stream_therm;
	
	CONNECTIONS
	s1 to v1.Inlet;

	SPECIFY
	s1.P = 150 * "kPa";
	s1.T = 281.75 * "K";
	s1.z = [0.664, 0.336];
	s1.v = 0.0;

	v1.x = 0.866;
	v1.Outlet.P = 148 * "kPa";

	SET
	v1.k = 20 * "gal/min/psi^0.5";
	
	OPTIONS
	relativeAccuracy = 1e-6;
	mode = "steady";
end

FlowSheet valve_Test_L
#with liquid conditions
	PARAMETERS
	PP	as CalcObject(Brief="Physical Properties",File="vrpp");
	NComp	as Integer;

	SET
	PP.Components = [ "isobutane", "benzene"];
	PP.LiquidModel = "PR";
	PP.VapourModel = "PR";
	NComp = PP.NumberOfComponents;
	
	DEVICES
	v1 as valve;
	s1 as stream_therm;
	
	CONNECTIONS
	s1 to v1.Inlet;

	SPECIFY
	s1.P = 185 * "kPa";
	s1.T = 328.12 * "K";
	s1.z = [0.001848, 0.9982];
	s1.v = 0.0;

	v1.x = 0.3363;
	v1.Outlet.P = 183 * "kPa";

	SET
	v1.k = 20 * "gal/min/psi^0.5";
	
	OPTIONS
	relativeAccuracy = 1e-6;
	mode = "steady";
end

FlowSheet valve_linear_Test
	
	DEVICES
	S1 as streamTP;
	V1 as valve_linear;

	CONNECTIONS
	S1 to V1.Inlet;
	
	PARAMETERS 
	PP 		as CalcObject	(Brief="External Physical Properties", File="vrpp");
	NComp   as Integer 		(Default= 1);
	
	SET
	PP.Components = ["water"];	
	PP.LiquidModel = "IdealLiquid";
	PP.VapourModel = "Ideal";
	PP.Derivatives = 0;
	NComp = PP.NumberOfComponents;
	
	SPECIFY
	S1.P = 2169.78			* "kPa";
	S1.T = 394.26 			* "K" ;
	S1.z = [1];
	V1.Qv = 113.56			* "m^3/h";
	V1.x = 0.5;
	V1.cv = 10				* "m^3/h/kPa^0.5";
	
	OPTIONS
	relativeAccuracy = 1e-6;
	mode = "steady";
end