#*-------------------------------------------------------------------
* 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.
*
*--------------------------------------------------------------------
* Model of cstr reactor
*--------------------------------------------------------------------
* Author: Paula B. Staudt
* $Id: cstr.mso 403 2007-11-16 15:43:31Z arge $
*--------------------------------------------------------------------*#

using "streams";

Model cstr_basic

ATTRIBUTES
	ATTRIBUTES
	Pallete 	= false;
	Brief 		= "Basic model for a CSTR reactor";
	
PARAMETERS

outer	NComp 						as Integer	(Brief = "Number Of Components");
		NReac 						as Integer	(Brief = "Number Of Reactions");
		stoic(NComp, NReac) 	as Real 		(Brief = "Stoichiometric Matrix");

VARIABLES

in	Inlet  	as stream 	(Brief="Inlet Stream", PosX=0, PosY=0, Symbol="_{in}");
out	Outlet 	as streamPH	(Brief="Outlet Stream", PosX=1, PosY=1, Symbol="_{out}");

	q    			as heat_rate 	(Brief="Heat");
	Vr   			as volume 		(Brief="Reacting Volume");
	M    			as mol 			(Brief = "Molar total amount");
	C(NComp)  	as conc_mol	(Brief="Components concentration");

EQUATIONS

"Molar Concentration"
	Outlet.z * M = C * Vr;

"Molar fraction"
    sum(Outlet.z) = 1;
end

Model cstr_yield as cstr_basic

ATTRIBUTES
	ATTRIBUTES
	Pallete 	= true;
	Icon 		= "icon/cstr"; 
	Brief 		= "Model of a CSTR with given yield";
	
PARAMETERS
	
	yield(NReac) as fraction (Brief="Yield");
	
EQUATIONS

	Outlet.z*Outlet.F = Inlet.z*Inlet.F * sumt(stoic*(1-yield));

"Reactor Energy Balance"
	diff(M*Outlet.h) = Inlet.F*Inlet.h - Outlet.F*Outlet.h - q;

end


Model cstr as cstr_basic
	
ATTRIBUTES
	Pallete 	= true;
	Icon 		= "icon/cstr"; 
	Brief 		= "Model of a generic CSTR";
	Info 		= "
Requires the information of:
* Reaction values
* Heat of reaction
";

VARIABLES
	
	r(NReac) 	as reaction_mol 	(Brief="Molar Reaction Rate");
	Hr(NReac) 	as heat_reaction 	(Brief="Heat Reaction");
	
EQUATIONS

"Component Molar Balance"
	diff(Outlet.z*M) = (Inlet.F*Inlet.z - Outlet.F*Outlet.z) + sumt(stoic*r)*Vr;

"Reactor Energy Balance"
	diff(M*Outlet.h) = Inlet.F*Inlet.h - Outlet.F*Outlet.h +sum(Hr*sum(stoic*r))*Vr - q; #FIXME sum(sum())

end