| [431] | 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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| 14 | * |
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| 15 | *-------------------------------------------------------------------- |
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| 16 | * Sample file for Double Pipe Heat Exchanger - Incremental approach |
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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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| 21 | *---------------------------------------------------------------------- |
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| 22 | * Author: Gerson B. Bicca |
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| 23 | * $Id: Sample_DoublePipeIncr.mso $ |
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| 24 | *--------------------------------------------------------------------*# |
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| 25 | |
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| 26 | using "heat_exchangers/DoublePipeIncr"; |
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| 27 | |
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| 28 | FlowSheet DoublePipe_Incremental |
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| 29 | |
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| 30 | PARAMETERS |
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| 31 | PP as Plugin (Type ="PP", LiquidModel = "PR", VapourModel = "PR", |
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| 32 | Components = ["aniline","benzene"]); |
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| 33 | NComp as Integer; |
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| 34 | |
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| 35 | DEVICES |
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| 36 | |
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| 37 | exchanger as DoublePipeIncr; |
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| 38 | InletHot as simple_source; |
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| 39 | InletCold as simple_source; |
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| 40 | OutletHot as simple_sink; |
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| 41 | OutletCold as simple_sink; |
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| 42 | |
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| 43 | |
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| 44 | CONNECTIONS |
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| 45 | |
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| 46 | InletCold.Outlet to exchanger.InletInner; |
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| 47 | InletHot.Outlet to exchanger.InletOuter; |
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| 48 | exchanger.OutletOuter to OutletHot.Inlet; |
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| 49 | exchanger.OutletInner to OutletCold.Inlet; |
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| 50 | |
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| 51 | SET |
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| 52 | |
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| [482] | 53 | NComp = PP.NumberOfComponents; |
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| 54 | exchanger.N = 100; |
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| [431] | 55 | |
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| [482] | 56 | #exchanger.CalculationApproach = "Simplified"; |
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| 57 | exchanger.CalculationApproach = "Full"; |
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| 58 | exchanger.Qestimated = 33*'kW'; |
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| 59 | |
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| 60 | |
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| [431] | 61 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 62 | # Options |
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| 63 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 64 | |
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| 65 | exchanger.FlowDirection = "counter"; |
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| 66 | exchanger.InnerTurbulentCorrelation = "SiederTate"; |
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| 67 | exchanger.InnerLaminarCorrelation = "Schlunder"; |
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| 68 | |
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| 69 | exchanger.OuterTurbulentCorrelation = "SiederTate"; |
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| 70 | exchanger.OuterLaminarCorrelation = "Schlunder"; |
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| 71 | |
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| 72 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 73 | # Double Pipe Geometrical Parameters and Alocation |
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| 74 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 75 | |
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| 76 | exchanger.DoInner = 42.16*'mm'; |
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| [438] | 77 | exchanger.DiInner = 35.05*'mm'; |
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| [431] | 78 | exchanger.DiOuter = 52.50*'mm'; |
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| [438] | 79 | exchanger.Kwall = 0.057 *'kW/m/K'; |
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| 80 | exchanger.Lpipe = 9*'m'; |
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| [431] | 81 | |
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| [438] | 82 | exchanger.Donozzle_Inner = 36.63*'mm'; |
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| 83 | exchanger.Dinozzle_Inner = 36.63*'mm'; |
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| 84 | |
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| 85 | exchanger.Donozzle_Outer = 42.72*'mm'; |
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| 86 | exchanger.Dinozzle_Outer = 42.72*'mm'; |
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| [431] | 87 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 88 | # Fouling |
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| 89 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 90 | exchanger.Rfi = 0.00018*'m^2*K/W'; |
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| 91 | exchanger.Rfo = 0*'m^2*K/W'; |
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| 92 | |
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| 93 | SPECIFY |
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| 94 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 95 | # Hot Stream |
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| 96 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 97 | #InletHot.Fw = 4396 * 'kg/h'; |
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| 98 | InletHot.Outlet.F = 47.2038 * 'kmol/h'; |
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| 99 | InletHot.Outlet.T = 338.71 * 'K'; |
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| 100 | InletHot.Outlet.P = 413.685 * 'kPa'; |
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| 101 | InletHot.Outlet.z = [1,0]; |
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| 102 | |
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| 103 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 104 | # Cold Stream |
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| 105 | #++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++ |
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| 106 | #InletCold.Fw = 4536 * 'kg/h'; |
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| 107 | InletCold.Outlet.F = 58.0694 * 'kmol/h'; |
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| 108 | InletCold.Outlet.T = 288.71 * 'K'; |
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| 109 | InletCold.Outlet.P = 413.685 * 'kPa'; |
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| 110 | InletCold.Outlet.z = [0,1]; |
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| 111 | |
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| 112 | OPTIONS |
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| 113 | |
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| 114 | Dynamic = false; |
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| 115 | GuessFile = "GuessDPincremental"; |
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| 116 | |
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| 117 | end |
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| 118 | |
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