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 86 2006-12-08 20:58:15Z 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 CalcObject(Brief="Physical Properties",File="vrpp"); |
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30 | NComp as Integer; |
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31 | |
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32 | SET |
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33 | PP.Components = [ "n-pentane", "benzene"]; |
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34 | PP.LiquidModel = "PR"; |
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35 | PP.VapourModel = "PR"; |
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36 | NComp = PP.NumberOfComponents; |
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37 | |
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38 | DEVICES |
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39 | t1 as tray; |
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40 | feed as stream_therm; |
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41 | inL as stream_therm; |
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42 | inV as stream_therm; |
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43 | |
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44 | CONNECTIONS |
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45 | feed to t1.Inlet; |
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46 | inL to t1.InletL; |
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47 | inV to t1.InletV; |
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48 | |
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49 | SPECIFY |
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50 | feed.F = 113.4 * "kmol/h"; |
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51 | feed.T = 291 * "K"; |
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52 | feed.P = 1.66 * "atm"; |
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53 | feed.z = [0.5, 0.5]; |
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54 | feed.v = 0; |
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55 | |
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56 | inL.P = 165 * "kPa"; |
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57 | inL.T = 310 * "K"; |
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58 | inL.F = 61.99 * "kmol/h"; |
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59 | inL.z = [0.1641, 0.8359]; |
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60 | inL.v = 0.0; |
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61 | |
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62 | inV.F = 147.1 * "kmol/h"; |
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63 | inV.v = 1.0; |
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64 | inV.P = 150 * "kPa"; |
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65 | inV.T = 321 * "K"; |
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66 | inV.z = [0.0584, 0.9416]; |
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67 | |
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68 | t1.Emv = 1; |
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69 | t1.OutletV.F = 147.1 * "kmol/h"; |
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70 | |
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71 | SET |
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72 | t1.V = 4 * "ft^3"; |
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73 | t1.Ah = 0.394 * "ft^2"; |
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74 | t1.lw = 20.94 * "in"; |
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75 | t1.hw = 0.125 * "ft"; |
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76 | t1.Q = 0 * "kW"; |
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77 | t1.beta = 0.6; |
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78 | t1.alfa = 4; |
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79 | t1.Ap = 3.94 * "ft^2"; |
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80 | |
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81 | INITIAL |
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82 | t1.OutletL.T = 290 *"K"; |
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83 | t1.Level = 0.9 * t1.hw; |
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84 | t1.OutletL.z(1) = 0.5; |
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85 | |
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86 | OPTIONS |
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87 | relativeAccuracy = 1e-6; |
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88 | time = [0:1:100]; |
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89 | end |
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