source: mso/sample/reactors/sample_cstr.mso @ 82

Last change on this file since 82 was 82, checked in by Paula Bettio Staudt, 16 years ago

Updated reactors sample files header

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[82]1#*-------------------------------------------------------------------
2* EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC.
[47]3*
[82]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* Sample file for model cstr
17*--------------------------------------------------------------------
18*
19* This sample file needs VRTherm (www.vrtech.com.br) to run.
20*
[47]21*----------------------------------------------------------------------
22* Author: Paula B. Staudt
[82]23* $Id: sample_cstr.mso 82 2006-12-08 20:11:44Z paula $
[47]24*--------------------------------------------------------------------*#
25
26using "reactors/cstr";
27
28FlowSheet cstr_PropyleneGlycol
29        PARAMETERS
30        PP   as CalcObject(Brief="Physical Properties",File="vrpp");
31        NComp as Integer;
32        R as Real(Default=8.3145, Unit="J/mol/K");
33
34        DEVICES
35        s1   as stream_therm;
36        Reac as cstr;
37
38        SET
39        PP.Components = ["1,2-propylene oxide", "methanol",
40                "water", "sulfuric acid", "1,2-propylene glycol" ];
41        PP.LiquidModel = "PR";
42        PP.VapourModel = "PR";
43
44        NComp = PP.NumberOfComponents;
45        Reac.NReac = 1;
46        Reac.stoic = [-1, 0, -1, 0, 1];
47       
48        EQUATIONS
49#       Reac.Hr = -36400 * "Btu/lbmol" - 7 * "Btu/lbmol/degR" * (Reac.Fout.T - 528 * "degR");
50#       Reac.r = 16.96e12 / "h" * exp(- 32400 * "Btu/lbmol"/R/Reac.Fout.T)
51#               * Reac.C(1);
52        Reac.Hr = 0 * "Btu/lbmol";
53        Reac.r  = 0 * "mol/l/s";
54
55        SPECIFY
56        s1.F = 52126 * "mol/h";
57        s1.P = 1     * "atm";
58        s1.T = 534.67* "degR";
59        s1.z = [0.0468, 0.0783, 0.874, 0.0009, 0];
60        s1.v = 0.0;
61
62        Reac.Vr    = 300   * "gal";
63        Reac.Outlet.F= Reac.Inlet.F;
64        "Adiabatic"
65        Reac.q     = 0     * "J/s";
66        Reac.Outlet.P= 1     * "atm";
67       
68        CONNECTIONS
69        s1  to  Reac.Inlet;
70       
71        INITIAL
72        Reac.Outlet.T = Reac.Inlet.T;
73        Reac.Outlet.z = Reac.Inlet.z;
74
75        OPTIONS
76        time = [0:0.1:5]*"h";
77end
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