[78] | 1 | #*------------------------------------------------------------------- |
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| 2 | * EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC. |
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| 3 | * |
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| 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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[1] | 14 | *---------------------------------------------------------------------- |
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| 15 | * Author: Gerson Balbueno Bicca |
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| 16 | * $Id: Mheatex.mso 544 2008-06-27 15:23:00Z bicca $ |
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| 17 | *--------------------------------------------------------------------*# |
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[45] | 18 | |
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[164] | 19 | using "HEX_Engine.mso"; |
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[1] | 20 | |
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| 21 | Model Mheatex |
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[135] | 22 | |
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| 23 | ATTRIBUTES |
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[307] | 24 | Icon = "icon/Mheatex"; |
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[139] | 25 | Pallete = true; |
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[284] | 26 | Brief = "Model of a Multistream heat exchangers"; |
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[359] | 27 | Info = |
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| 28 | "Heat Transfer between multiple hot and cold streams. |
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| 29 | |
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| 30 | == Specify == |
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[544] | 31 | The user must specify the following variables: |
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[359] | 32 | * The Inlet Hot streams: Any Number |
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| 33 | * The Inlet Cold streams: Any Number |
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| 34 | * The LMTD correction factor |
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[544] | 35 | * The outlet temperature and the outlet pressure for each stream on one side (hot or cold) of the heat exchanger |
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| 36 | * On the other side the user must leave at least one unespecified outlet stream. |
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[359] | 37 | |
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| 38 | == Setting The Mheatex Parameters == |
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[544] | 39 | * FlowDirection: counter or cocurrent flow |
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| 40 | * Number of hot streams (Nhot) |
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| 41 | * Number of cold streams (Ncold) |
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[359] | 42 | "; |
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| 43 | |
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[1] | 44 | PARAMETERS |
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| 45 | |
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[325] | 46 | outer PP as Plugin (Brief="Physical Properties", Type="PP"); |
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| 47 | outer NComp as Integer (Brief="Number of Components"); |
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| 48 | FlowDirection as Switcher (Brief="Flow Direction",Valid=["counter","cocurrent"],Default="cocurrent"); |
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[359] | 49 | Ncold as Integer (Brief="Number of Inlet Cold Streams",Lower=1, Symbol = "N_{cold}"); |
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| 50 | Nhot as Integer (Brief="Number of Inlet Hot Streams",Lower=1, Symbol = "N_{hot}"); |
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[45] | 51 | |
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[1] | 52 | VARIABLES |
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| 53 | |
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[544] | 54 | in InletHot(Nhot) as stream (Brief="Inlet Hot Streams", PosX=0, PosY=0.7156, Symbol="_{hot}^{in}"); |
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| 55 | out OutletHot(Nhot) as streamPH (Brief="Outlet Hot Streams", PosX=1, PosY=0.7156, Symbol="_{hot}^{out}"); |
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| 56 | in InletCold(Ncold) as stream (Brief="Inlet Cold Streams", PosX=1, PosY=0.2793, Symbol="_{cold}^{in}"); |
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| 57 | out OutletCold(Ncold) as streamPH (Brief="Outlet Cold Streams", PosX=0, PosY=0.2793, Symbol="_{cold}^{out}"); |
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[1] | 58 | |
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[359] | 59 | Method as LMTD_Basic (Brief="Log Mean Temperature Difference Method", Symbol = " "); |
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[325] | 60 | Q as power (Brief="Heat Transfer", Default=7000, Lower=1e-6, Upper=1e10); |
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| 61 | UA as Real (Brief="UA product",Unit='W/K',Lower=1e-8); |
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[131] | 62 | |
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[1] | 63 | EQUATIONS |
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| 64 | |
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| 65 | "Hot Flow" |
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[164] | 66 | OutletHot.F = InletHot.F; |
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[1] | 67 | |
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| 68 | "Cold Flow" |
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[164] | 69 | OutletCold.F = InletCold.F; |
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[1] | 70 | |
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| 71 | "Hot Composition" |
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[164] | 72 | OutletHot.z = InletHot.z; |
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[1] | 73 | |
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| 74 | "Cold Composition" |
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[164] | 75 | OutletCold.z = InletCold.z; |
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[1] | 76 | |
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| 77 | "Heat Duty Hot Stream" |
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[164] | 78 | Q = sum(InletHot.F*(InletHot.h- OutletHot.h)); |
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[1] | 79 | |
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| 80 | "Heat Duty Cold Stream" |
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[164] | 81 | Q = -sum(InletCold.F*(InletCold.h- OutletCold.h)); |
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[1] | 82 | |
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| 83 | "Heat Duty" |
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[168] | 84 | Q = UA*Method.LMTD*Method.Fc; |
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[1] | 85 | |
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[144] | 86 | switch FlowDirection |
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[1] | 87 | |
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[140] | 88 | case "cocurrent": |
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| 89 | |
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[131] | 90 | "Temperature Difference at Inlet" |
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[164] | 91 | Method.DT0 = max(InletHot.T) - min(InletCold.T); |
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[131] | 92 | |
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| 93 | "Temperature Difference at Outlet" |
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[164] | 94 | Method.DTL = min(OutletHot.T) - max(OutletCold.T); |
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[131] | 95 | |
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[140] | 96 | case "counter": |
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[1] | 97 | |
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[131] | 98 | "Temperature Difference at Inlet" |
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[164] | 99 | Method.DT0 = max(InletHot.T) - max(OutletCold.T); |
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[131] | 100 | |
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| 101 | "Temperature Difference at Outlet" |
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[164] | 102 | Method.DTL = min(OutletHot.T) - min(InletCold.T); |
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[131] | 103 | |
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[1] | 104 | end |
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| 105 | |
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| 106 | end |
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