| 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 model tray |
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| 17 | *-------------------------------------------------------------------- |
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| 18 | * |
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| 19 | * This sample file needs VRTherm DEMO (www.vrtech.com.br) to run. |
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| 20 | * |
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| 21 | *---------------------------------------------------------------------- |
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| 22 | * Author: Paula B. Staudt |
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| 23 | * $Id: sample_tray.mso 423 2007-11-29 20:03:51Z paula $ |
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| 24 | *--------------------------------------------------------------------*# |
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| 25 | using "stage_separators/tray"; |
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| 26 | |
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| 27 | FlowSheet tray_Test |
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| 28 | PARAMETERS |
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| 29 | PP as Plugin(Brief="Physical Properties", |
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| 30 | Type="PP", |
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| 31 | Components = [ "n-pentane", "benzene"], |
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| 32 | LiquidModel = "PR", |
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| 33 | VapourModel = "PR" |
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| 34 | ); |
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| 35 | NComp as Integer; |
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| 36 | |
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| 37 | SET |
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| 38 | NComp = PP.NumberOfComponents; |
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| 39 | |
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| 40 | DEVICES |
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| 41 | t1 as tray; |
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| 42 | feed as source; |
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| 43 | inL as liquid_stream; |
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| 44 | inV as vapour_stream; |
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| 45 | |
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| 46 | CONNECTIONS |
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| 47 | feed.Outlet to t1.Inlet; |
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| 48 | inL to t1.InletL; |
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| 49 | inV to t1.InletV; |
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| 50 | |
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| 51 | SPECIFY |
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| 52 | feed.Outlet.F = 113.4 * 'kmol/h'; |
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| 53 | feed.Outlet.T = 291 * 'K'; |
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| 54 | feed.Outlet.P = 1.66 * 'atm'; |
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| 55 | feed.Outlet.z = [0.5, 0.5]; |
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| 56 | |
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| 57 | inL.P = 165 * 'kPa'; |
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| 58 | inL.T = 310 * 'K'; |
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| 59 | inL.F = 61.99 * 'kmol/h'; |
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| 60 | inL.z = [0.1641, 0.8359]; |
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| 61 | |
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| 62 | inV.P = 150 * 'kPa'; |
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| 63 | inV.T = 321 * 'K'; |
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| 64 | inV.z = [0.0584, 0.9416]; |
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| 65 | |
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| 66 | t1.Emv = 1; |
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| 67 | t1.OutletV.F = 147.1 * 'kmol/h'; |
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| 68 | |
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| 69 | SET |
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| 70 | t1.V = 4 * 'ft^3'; |
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| 71 | t1.Ah = 0.394 * 'ft^2'; |
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| 72 | t1.lw = 20.94 * 'in'; |
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| 73 | t1.hw = 0.125 * 'ft'; |
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| 74 | t1.Q = 0 * 'kW'; |
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| 75 | t1.beta = 0.6; |
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| 76 | t1.alfa = 4; |
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| 77 | t1.Ap = 3.94 * 'ft^2'; |
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| 78 | |
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| 79 | INITIAL |
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| 80 | t1.OutletL.T = 290 *'K'; |
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| 81 | t1.Level = 0.9 * t1.hw; |
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| 82 | t1.OutletL.z(1) = 0.5; |
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| 83 | |
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| 84 | OPTIONS |
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| 85 | TimeEnd = 100; |
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| 86 | end |
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