| 1 | #*--------------------------------------------------------------------- |
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| 2 | * This file is property of the author and cannot be used, copyed |
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| 3 | * or modified without permission. |
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| 4 | * |
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| 5 | * Copyright (C) 2004 the author |
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| 6 | *---------------------------------------------------------------------- |
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| 7 | * Author: Paula B. Staudt |
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| 8 | * $Id: sample_cstr_PG.mso 6 2005-01-11 17:06:06Z paula $ |
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| 9 | *--------------------------------------------------------------------*# |
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| 10 | |
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| 11 | using "cstr"; |
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| 12 | |
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| 13 | FlowSheet cstr_PropyleneGlycol |
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| 14 | PARAMETERS |
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| 15 | PP as CalcObject(Brief="Physical Properties",File="VMG"); |
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| 16 | NoComps as Integer; |
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| 17 | R as Real(Default=8.3145, Unit="J/mol/K"); |
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| 18 | |
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| 19 | DEVICES |
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| 20 | s1 as stream_therm; |
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| 21 | Reac as cstr; |
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| 22 | |
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| 23 | SET |
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| 24 | PP.Models = "RK RK"; |
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| 25 | PP.Components = ["1,2-Propylene Oxide", "Methanol", |
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| 26 | "Water", "Sulfuric Acid", "1,2-Propylene Glycol" ]; |
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| 27 | NoComps = PP.NumberOfComponents; |
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| 28 | Reac.NoReacs = 1; |
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| 29 | Reac.stoic = [-1, 0, -1, 0, 1]; |
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| 30 | |
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| 31 | EQUATIONS |
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| 32 | # Reac.Hr = -36400 * "Btu/lbmol" - 7 * "Btu/lbmol/degR" * (Reac.Fout.T - 528 * "degR"); |
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| 33 | # Reac.r = 16.96e12 / "h" * exp(- 32400 * "Btu/lbmol"/R/Reac.Fout.T) |
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| 34 | # * Reac.C(1); |
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| 35 | Reac.Hr = 0 * "Btu/lbmol"; |
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| 36 | Reac.r = 0 * "mol/l/s"; |
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| 37 | |
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| 38 | SPECIFY |
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| 39 | s1.F = 52126 * "mol/h"; |
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| 40 | s1.P = 1 * "atm"; |
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| 41 | s1.T = 534.67* "degR"; |
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| 42 | s1.z = [0.0468, 0.0783, 0.874, 0.0009, 0]; |
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| 43 | s1.v = 0.0; |
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| 44 | |
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| 45 | Reac.Vr = 300 * "gal"; |
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| 46 | Reac.Outlet.F= Reac.Inlet.F; |
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| 47 | "Adiabatic" |
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| 48 | Reac.q = 0 * "J/s"; |
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| 49 | Reac.Outlet.P= 1 * "atm"; |
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| 50 | |
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| 51 | CONNECTIONS |
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| 52 | s1 to Reac.Inlet; |
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| 53 | |
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| 54 | INITIAL |
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| 55 | Reac.Outlet.T = Reac.Inlet.T; |
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| 56 | Reac.Outlet.z = Reac.Inlet.z; |
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| 57 | |
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| 58 | OPTIONS |
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| 59 | differentiation = "numeric"; |
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| 60 | outputLevel = "all"; |
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| 61 | end |
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