| [82] | 1 | #*------------------------------------------------------------------- |
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| 2 | * EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC. |
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| [47] | 3 | * |
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| [82] | 4 | * This LIBRARY is free software; you can distribute it and/or modify |
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| 5 | * it under the therms of the ALSOC FREE LICENSE as available at |
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| 6 | * http://www.enq.ufrgs.br/alsoc. |
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| 7 | * |
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| 8 | * EMSO Copyright (C) 2004 - 2007 ALSOC, original code |
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| 9 | * from http://www.rps.eng.br Copyright (C) 2002-2004. |
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| 10 | * All rights reserved. |
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| 11 | * |
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| 12 | * EMSO is distributed under the therms of the ALSOC LICENSE as |
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| 13 | * available at http://www.enq.ufrgs.br/alsoc. |
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| 14 | * |
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| 15 | *-------------------------------------------------------------------- |
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| 16 | * Sample file for model cstr |
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| 17 | *-------------------------------------------------------------------- |
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| 18 | * |
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| 19 | * This sample file needs VRTherm (www.vrtech.com.br) to run. |
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| 20 | * |
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| [47] | 21 | *---------------------------------------------------------------------- |
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| 22 | * Author: Paula B. Staudt |
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| [82] | 23 | * $Id: sample_cstr.mso 82 2006-12-08 20:11:44Z paula $ |
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| [47] | 24 | *--------------------------------------------------------------------*# |
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| 25 | |
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| 26 | using "reactors/cstr"; |
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| 27 | |
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| 28 | FlowSheet cstr_PropyleneGlycol |
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| 29 | PARAMETERS |
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| 30 | PP as CalcObject(Brief="Physical Properties",File="vrpp"); |
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| 31 | NComp as Integer; |
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| 32 | R as Real(Default=8.3145, Unit="J/mol/K"); |
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| 33 | |
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| 34 | DEVICES |
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| 35 | s1 as stream_therm; |
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| 36 | Reac as cstr; |
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| 37 | |
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| 38 | SET |
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| 39 | PP.Components = ["1,2-propylene oxide", "methanol", |
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| 40 | "water", "sulfuric acid", "1,2-propylene glycol" ]; |
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| 41 | PP.LiquidModel = "PR"; |
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| 42 | PP.VapourModel = "PR"; |
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| 43 | |
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| 44 | NComp = PP.NumberOfComponents; |
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| 45 | Reac.NReac = 1; |
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| 46 | Reac.stoic = [-1, 0, -1, 0, 1]; |
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| 47 | |
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| 48 | EQUATIONS |
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| 49 | # Reac.Hr = -36400 * "Btu/lbmol" - 7 * "Btu/lbmol/degR" * (Reac.Fout.T - 528 * "degR"); |
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| 50 | # Reac.r = 16.96e12 / "h" * exp(- 32400 * "Btu/lbmol"/R/Reac.Fout.T) |
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| 51 | # * Reac.C(1); |
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| 52 | Reac.Hr = 0 * "Btu/lbmol"; |
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| 53 | Reac.r = 0 * "mol/l/s"; |
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| 54 | |
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| 55 | SPECIFY |
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| 56 | s1.F = 52126 * "mol/h"; |
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| 57 | s1.P = 1 * "atm"; |
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| 58 | s1.T = 534.67* "degR"; |
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| 59 | s1.z = [0.0468, 0.0783, 0.874, 0.0009, 0]; |
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| 60 | s1.v = 0.0; |
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| 61 | |
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| 62 | Reac.Vr = 300 * "gal"; |
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| 63 | Reac.Outlet.F= Reac.Inlet.F; |
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| 64 | "Adiabatic" |
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| 65 | Reac.q = 0 * "J/s"; |
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| 66 | Reac.Outlet.P= 1 * "atm"; |
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| 67 | |
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| 68 | CONNECTIONS |
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| 69 | s1 to Reac.Inlet; |
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| 70 | |
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| 71 | INITIAL |
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| 72 | Reac.Outlet.T = Reac.Inlet.T; |
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| 73 | Reac.Outlet.z = Reac.Inlet.z; |
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| 74 | |
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| 75 | OPTIONS |
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| 76 | time = [0:0.1:5]*"h"; |
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| 77 | end |
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