source: trunk/eml/reactors/stoic.mso @ 992

Last change on this file since 992 was 574, checked in by Rafael de Pelegrini Soares, 15 years ago

Updated the models to work with some language constraints
File size: 5.9 KB
Line 
1#*---------------------------------------------------------------------
2* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
3*
4* This LIBRARY is free software; you can distribute it and/or modify
5* it under the therms of the ALSOC FREE LICENSE as available at
6* http://www.enq.ufrgs.br/alsoc.
7*
8* EMSO Copyright (C) 2004 - 2007 ALSOC, original code
9* from http://www.rps.eng.br Copyright (C) 2002-2004.
10* All rights reserved.
11*
12* EMSO is distributed under the therms of the ALSOC LICENSE as
13* available at http://www.enq.ufrgs.br/alsoc.
14*
15*----------------------------------------------------------------------
16* Model of a stoichiometric reactor
17*----------------------------------------------------------------------
18*
19*   Description:
20*       Modeling of a reactor based on a stoichiometric approach.
21*
22*   Assumptions:
23*               * single- and two-phases involved
24*               * steady-state
25*
26*       Specify:
27*               * inlet stream
28*               * extent of reactions or
29*               * conversion of a key component
30*
31*----------------------------------------------------------------------
32* Author: Rodolfo Rodrigues
33* $Id$
34*--------------------------------------------------------------------*#
35
36using "tank_basic";
37
38
39#*---------------------------------------------------------------------
40*       only vapour-phase
41*--------------------------------------------------------------------*#
42Model stoic_vap as tank_vap
43        ATTRIBUTES
44        Brief   = "Basic model for a vapour-phase stoichiometric CSTR";
45        Info    = "
46== Assumptions ==
47* only vapour-phase
48* steady-state
49";
50       
51        PARAMETERS
52        NReac           as Integer (Brief="Number of reactions", Default=1);
53    stoic(NComp,NReac) as Real (Brief="Stoichiometric matrix", Symbol="\nu");
54
55        VARIABLES
56out Outlet              as vapour_stream(Brief="Outlet stream", PosX=1, PosY=1, Symbol="_{out}");
57
58        rate(NComp) as reaction_mol (Brief="Overall component rate of reaction");
59        conv(NComp) as Real (Brief="Fractional conversion of component", Symbol="X", Default=0);
60       
61        EQUATIONS
62        "Outlet stream"
63        Outlet.F*Outlet.z = Outletm.F*Outletm.z + rate*Tank.V;
64       
65        "Mechanical equilibrium"
66        Outlet.P = Outletm.P;
67       
68        "Energy balance"
69        Outlet.F*Outlet.h = Outletm.F*Outletm.h;
70       
71        "Steady-state"
72        Outlet.F = Outletm.F;
73       
74        for i in [1:NComp] do
75          if (Outletm.z(i) > 1e-16) then
76            "Molar conversion"
77            Outlet.F*Outlet.z(i) = Outletm.F*Outletm.z(i)*(1 - conv(i));
78          else if (Outlet.z(i) > 0) then
79                        "Molar conversion"
80                                conv(i) = 1;    # ?
81                        else
82                        "Molar conversion"
83                                conv(i) = 0;    # ?
84                        end
85          end
86        end
87end
88
89
90#*---------------------------------------------------------------------
91*       only liquid-phase
92*--------------------------------------------------------------------*#
93Model stoic_liq as tank_liq
94        ATTRIBUTES
95        Brief   = "Basic model for a liquid-phase stoichiometric CSTR";
96        Info    = "
97== Assumptions ==
98* only liquid-phase
99* steady-state
100";
101
102        PARAMETERS
103        NReac           as Integer (Brief="Number of reactions", Default=1);
104    stoic(NComp,NReac) as Real (Brief="Stoichiometric matrix", Symbol="\nu");
105       
106        VARIABLES
107out Outlet              as liquid_stream(Brief="Outlet stream", PosX=1, PosY=1, Symbol="_{out}");
108
109        rate(NComp) as reaction_mol (Brief="Overall component rate of reaction");
110        conv(NComp)     as Real (Brief="Fractional conversion of component", Symbol="X", Default=0);
111       
112        EQUATIONS
113        "Outlet stream"
114        Outlet.F*Outlet.z = Outletm.F*Outletm.z + rate*Tank.V;
115       
116        "Mechanical equilibrium"
117        Outlet.P = Outletm.P;
118       
119        "Energy balance"
120        Outlet.F*Outlet.h = Outletm.F*Outletm.h;
121       
122        "Steady-state"
123        Outlet.F = Outletm.F;
124
125        for i in [1:NComp] do
126          if (Outletm.z(i) > 1e-16) then
127            "Molar conversion"
128            Outlet.F*Outlet.z(i) = Outletm.F*Outletm.z(i)*(1 - conv(i));
129          else if (Outlet.z(i) > 0) then
130                        "Molar conversion"
131                                conv(i) = 1;    # ?
132                        else
133                        "Molar conversion"
134                                conv(i) = 0;    # ?
135                        end
136          end
137        end
138end
139
140
141#*---------------------------------------------------------------------
142*       1. extent of reactions are known
143*--------------------------------------------------------------------*#
144Model stoic_extent_vap as stoic_vap
145        ATTRIBUTES
146        Pallete = true;
147        Icon    = "icon/cstr";
148        Brief   = "Model of a generic vapour-phase stoichiometric CSTR based on extent of reaction";
149        Info    = "
150== Specify ==
151* inlet stream
152* extent of reactions
153";
154
155        VARIABLES
156        extent(NReac)   as flow_mol (Brief="Extent of reaction", Symbol="\xi");
157       
158        EQUATIONS
159        "Rate of reaction"
160        rate*Tank.V = sumt(stoic*extent);
161end
162
163Model stoic_extent_liq as stoic_liq
164        ATTRIBUTES
165        Pallete = true;
166        Icon    = "icon/cstr";
167        Brief   = "Model of a generic liquid-phase stoichiometric CSTR based on extent of reaction";
168        Info    = "
169== Specify ==
170* inlet stream
171* extent of reactions
172";
173
174        VARIABLES
175        extent(NReac)   as flow_mol (Brief="Extent of reaction", Symbol="\xi");
176       
177        EQUATIONS
178        "Rate of reaction"
179        rate*Tank.V = sumt(stoic*extent);
180end
181
182
183#*---------------------------------------------------------------------
184*       2. conversion of a key component is known
185*--------------------------------------------------------------------*#
186Model stoic_conv_vap as stoic_vap
187        ATTRIBUTES
188        Pallete = true;
189        Icon    = "icon/cstr";
190        Brief   = "Model of a generic vapour-phase stoichiometric CSTR based on conversion of a key component";
191        Info    = "
192== Specify ==
193* inlet stream
194* conversion of a key component
195";
196
197        PARAMETERS
198        KComp as Integer(Brief="Key component", Lower=1, Default=1);
199
200        VARIABLES
201        kconv as Real   (Brief="Molar conversion of key component", Symbol="X_k");
202
203        EQUATIONS
204        "Reaction rate"
205        rate*Tank.V = sumt(stoic)/abs(sumt(stoic(KComp,:)))*Outletm.F*Outletm.z(KComp)*kconv;
206end
207
208Model stoic_conv_liq as stoic_liq
209        ATTRIBUTES
210        Pallete = true;
211        Icon    = "icon/cstr";
212        Brief   = "Model of a generic liquid-phase stoichiometric CSTR based on conversion of a key component";
213        Info    = "
214== Specify ==
215* inlet stream
216* conversion of a key component
217";
218
219        PARAMETERS
220        KComp as Integer(Brief="Key component", Lower=1, Default=1);
221
222        VARIABLES
223        kconv as Real   (Brief="Molar conversion of key component", Symbol="X_k");
224
225        EQUATIONS
226        "Reaction rate"
227        rate*Tank.V = sumt(stoic)/abs(sumt(stoic(KComp,:)))*Outletm.F*Outletm.z(KComp)*kconv;
228end
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