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 flash and flashSteady |
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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: Paula B. Staudt |
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23 | * $Id: sample_flash.mso 633 2008-09-24 00:26:30Z bicca $ |
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24 | *--------------------------------------------------------------------*# |
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25 | using "stage_separators/flash"; |
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26 | |
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27 | # exemplo baseado nos dados do artigo do Gani 1985. |
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28 | FlowSheet flash_Test |
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29 | PARAMETERS |
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30 | PP as Plugin(Brief="Physical Properties", |
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31 | Type="PP", |
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32 | Components = ["1,3-butadiene", "isobutene", "n-pentane", |
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33 | "1-pentene", "1-hexene", "benzene"], |
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34 | LiquidModel = "PR", |
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35 | VapourModel = "PR" |
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36 | ); |
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37 | NComp as Integer; |
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38 | |
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39 | VARIABLES |
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40 | Q as energy_source (Brief="Heat supplied"); |
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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 | fl as flash; |
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47 | s1 as source; |
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48 | |
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49 | CONNECTIONS |
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50 | s1.Outlet to fl.Inlet; |
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51 | Q.OutletQ to fl.InletQ; |
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52 | |
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53 | EQUATIONS |
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54 | fl.OutletL.F = 400*sqrt(fl.Level/'m') * 'kmol/h'; |
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55 | |
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56 | SPECIFY |
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57 | s1.F = 496.3 * 'kmol/h'; |
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58 | s1.T = 338 * 'K'; |
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59 | s1.P = 507.1 * 'kPa'; |
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60 | s1.Composition = [0.2379,0.3082,0.09958,0.1373,0.08872,0.1283]; |
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61 | |
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62 | fl.OutletV.F = 68.5 * 'kmol/h'; |
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63 | Q.OutletQ.Q = 0 * 'kJ/h'; |
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64 | |
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65 | SET |
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66 | fl.V = 50 * 'm^3'; |
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67 | fl.diameter = 2 * 'm'; |
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68 | fl.orientation = "vertical"; |
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69 | # fl.orientation = "horizontal"; |
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70 | |
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71 | INITIAL |
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72 | fl.OutletL.T = 338 * 'K'; |
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73 | fl.Level = 0.4 * 'm'; |
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74 | |
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75 | fl.OutletL.z(1) = 0.1; |
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76 | fl.OutletL.z(2) = 0.1; |
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77 | fl.OutletL.z(3) = 0.1; |
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78 | fl.OutletL.z(4) = 0.1; |
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79 | fl.OutletL.z(5) = 0.1; |
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80 | |
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81 | OPTIONS |
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82 | Dynamic = true; |
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83 | TimeStep = 0.1; |
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84 | TimeEnd = 5; |
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85 | TimeUnit = 'h'; |
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86 | end |
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87 | |
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88 | # exemplo baseado nos dados do artigo do Gani 1985. |
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89 | FlowSheet flashSteady_Test |
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90 | PARAMETERS |
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91 | PP as Plugin(Brief="Physical Properties", |
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92 | Type="PP", |
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93 | Components = ["1,3-butadiene", "isobutene", "n-pentane", |
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94 | "1-pentene", "1-hexene", "benzene"], |
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95 | LiquidModel = "PR", |
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96 | VapourModel = "PR" |
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97 | ); |
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98 | NComp as Integer; |
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99 | |
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100 | VARIABLES |
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101 | Q as energy_source (Brief="Heat supplied"); |
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102 | |
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103 | SET |
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104 | NComp = PP.NumberOfComponents; |
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105 | |
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106 | DEVICES |
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107 | fl as flash_steady; |
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108 | s1 as source; |
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109 | |
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110 | CONNECTIONS |
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111 | s1.Outlet to fl.Inlet; |
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112 | Q.OutletQ to fl.InletQ; |
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113 | |
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114 | SPECIFY |
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115 | s1.F = 496.3 * 'kmol/h'; |
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116 | s1.T = 338 * 'K'; |
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117 | s1.P = 507.1 * 'kPa'; |
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118 | s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283]; |
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119 | |
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120 | fl.OutletL.P = 2.5 * 'atm'; |
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121 | |
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122 | #Q.OutletQ.Q = 0 * 'kJ/h'; |
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123 | fl.OutletL.T = 315.06 * 'K'; |
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124 | |
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125 | OPTIONS |
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126 | Dynamic = false; |
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127 | end |
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128 | |
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129 | |
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130 | Sensitivity Sense_Flash as flashSteady_Test |
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131 | |
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132 | VARY |
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133 | |
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134 | s1.F 'kmol/h'; |
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135 | |
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136 | RESPONSE |
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137 | |
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138 | fl.OutletV.F'kmol/h'; |
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139 | |
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140 | end |
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141 | |
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142 | # Case study to check the responses |
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143 | |
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144 | CaseStudy caseFlash as flashSteady_Test |
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145 | |
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146 | VARY |
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147 | |
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148 | s1.F = [496.3, 496.31]*'kmol/h'; |
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149 | |
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150 | RESPONSE |
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151 | |
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152 | |
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153 | fl.OutletV.F'kmol/h'; |
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154 | |
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155 | end |
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