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 batch distillation with controllers |
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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: |
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23 | * $Id: sample_batch_dist_PID.mso 213 2007-03-15 19:40:55Z rafael $ |
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24 | *--------------------------------------------------------------------*# |
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25 | using "stage_separators/batch_dist"; |
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26 | using "controllers/PIDs"; |
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27 | |
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28 | FlowSheet TesteBatch_PID |
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29 | |
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30 | PARAMETERS |
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31 | PP as Plugin(Brief="Physical Properties", |
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32 | Type="PP", Components = [ "isobutane", "benzene" ], |
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33 | LiquidModel = "PR", VapourModel = "PR"); |
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34 | NComp as Integer; |
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35 | P_max as pressure(Brief="Maximum Pressure on distillator"); |
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36 | P_min as pressure(Brief="Minimum Pressure on distillator"); |
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37 | |
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38 | VARIABLES |
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39 | P_ad as fraction(Brief="Dimensionless pressure"); |
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40 | P_set as pressure(Brief="Minimum Pressure on distillator"); |
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41 | |
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42 | SET |
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43 | NComp = PP.NumberOfComponents; |
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44 | |
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45 | DEVICES |
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46 | batch as Diff_Dist; |
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47 | reflux as stream; |
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48 | feed as stream; |
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49 | pidP as PID_Ideal_AWBT; |
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50 | |
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51 | CONNECTIONS |
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52 | reflux to batch.InletL; |
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53 | feed to batch.Inlet; |
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54 | |
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55 | EQUATIONS |
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56 | if batch.Level > 1E-3 then |
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57 | batch.Q = 3.7743e6 * 'kJ/h'; |
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58 | else |
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59 | batch.Q = 0 * 'kJ/h'; |
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60 | end |
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61 | |
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62 | "Pressure Controller" |
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63 | pidP.Parameters.tau = 0*'s'; |
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64 | pidP.Parameters.tauSet = 0*'s'; |
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65 | pidP.Parameters.alpha = 0.3; |
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66 | pidP.Parameters.bias = 0; |
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67 | pidP.Parameters.gamma = 1; |
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68 | pidP.Parameters.beta = 1; |
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69 | pidP.Options.action = -1; |
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70 | pidP.Options.clip = 1; |
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71 | pidP.Options.autoMan = 0; |
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72 | pidP.Parameters.intTime = 0.1*'min'; |
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73 | pidP.Parameters.gain = 1; |
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74 | pidP.Parameters.derivTime = 0.02*'min'; |
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75 | pidP.Ports.setPoint = (P_set-P_min)/(P_max-P_min); |
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76 | pidP.Ports.input = P_ad; |
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77 | P_ad = (batch.P-P_min)/(P_max-P_min); |
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78 | batch.OutletV.F = 500 * 'kmol/h' * pidP.Ports.output; |
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79 | |
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80 | SPECIFY |
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81 | reflux.F = 0 * 'kmol/h'; |
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82 | reflux.T = 328 * 'K'; |
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83 | reflux.P = 180 * 'kPa'; |
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84 | reflux.z = [0.5, 0.5]; |
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85 | reflux.v = 0; |
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86 | reflux.h = 0 * 'kJ/kmol'; |
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87 | |
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88 | feed.F = 0 * 'kmol/h'; |
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89 | feed.T = 328 * 'K'; |
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90 | feed.P = 180 * 'kPa'; |
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91 | feed.z = [0.5, 0.5]; |
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92 | feed.v = 0; |
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93 | feed.h = 0 * 'kJ/kmol'; |
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94 | |
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95 | P_set = 300 * 'kPa'; |
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96 | |
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97 | SET |
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98 | batch.V = 3 * 'm^3'; |
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99 | batch.Across = 1 * 'm^2'; |
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100 | P_max = 500 * 'kPa'; |
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101 | P_min = 100 * 'kPa'; |
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102 | |
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103 | INITIAL |
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104 | batch.T = 298 *'K'; |
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105 | batch.Level = 2.5 * 'm'; |
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106 | batch.x(2) = 0.2; |
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107 | |
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108 | OPTIONS |
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109 | RelativeAccuracy = 1e-5; |
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110 | TimeEnd = 6; |
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111 | TimeStep = 0.01; |
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112 | TimeUnit = 'min'; |
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113 | end |
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