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 522 2008-05-21 23:21:12Z arge $ |
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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 = 1; |
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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 | t1.VapourFlowModel = "Feehery_Fv"; #"Roffel_Fv" "Klingberg" "Wang_Fv" "Elgue" or "Reepmeyer"-> default |
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80 | t1.w = 0.5 * '1/m^4'; |
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81 | |
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82 | t1.LiquidFlowModel = "Wang_Fl"; # "Feehery_Fl" "Roffel_Fl" "Olsen" or "default" |
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83 | |
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84 | INITIAL |
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85 | t1.OutletL.T = 290 *'K'; |
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86 | t1.Level = 0.9 * t1.hw; |
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87 | t1.OutletL.z(1) = 0.5; |
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88 | |
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89 | OPTIONS |
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90 | TimeEnd = 100; |
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91 | end |
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92 | |
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93 | FlowSheet packedStage_Test_1 |
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94 | PARAMETERS |
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95 | PP as Plugin(Brief="Physical Properties", |
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96 | Type="PP", |
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97 | Components = [ "n-pentane", "benzene"], |
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98 | LiquidModel = "PR", |
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99 | VapourModel = "PR" |
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100 | ); |
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101 | NComp as Integer; |
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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 | t1 as packedStage; |
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108 | feed as source; |
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109 | inL as liquid_stream; |
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110 | inV as vapour_stream; |
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111 | |
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112 | CONNECTIONS |
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113 | feed.Outlet to t1.Inlet; |
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114 | inL to t1.InletL; |
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115 | inV to t1.InletV; |
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116 | |
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117 | SPECIFY |
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118 | feed.Outlet.F = 113.4 * 'kmol/h'; |
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119 | feed.Outlet.T = 291 * 'K'; |
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120 | feed.Outlet.P = 1.66 * 'atm'; |
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121 | feed.Outlet.z = [0.5, 0.5]; |
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122 | |
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123 | inL.P = 165 * 'kPa'; |
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124 | inL.T = 315 * 'K'; |
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125 | inL.F = 61.99 * 'kmol/h'; |
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126 | inL.z = [0.1641, 0.8359]; |
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127 | |
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128 | inV.F = 201.25 * 'kmol/h'; |
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129 | inV.P = 150 * 'kPa'; |
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130 | inV.T = 315 * 'K'; |
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131 | inV.z = [0.0584, 0.9416]; |
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132 | |
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133 | t1.OutletV.P = 145 * 'kPa'; |
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134 | |
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135 | SET |
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136 | #Metal Pall Ring - nominal packing size 50 mm - Billet and Schultes, 1999. |
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137 | t1.Q = 0 * 'kW'; |
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138 | t1.V = 0.8 * 'm^2' * 0.4 * 'm'; |
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139 | t1.d = 1.009 * 'm'; |
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140 | t1.Cpo = 0.763; |
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141 | t1.e = 0.951; |
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142 | t1.a = 112.6 * 'm^2/m^3'; |
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143 | t1.hs = 0.4 * 'm'; |
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144 | t1.Qsil = 10; |
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145 | |
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146 | INITIAL |
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147 | t1.OutletL.T = 315 *'K'; |
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148 | t1.ML = 0.25 * 'kmol'; |
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149 | t1.OutletL.z(1) = 0.1641; |
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150 | |
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151 | OPTIONS |
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152 | DAESolver(File="sundials"); |
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153 | TimeStep = 0.001; |
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154 | TimeEnd = 0.1; |
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155 | end |
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156 | |
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157 | FlowSheet packedStage_Test_2 |
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158 | PARAMETERS |
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159 | PP as Plugin(Brief="Physical Properties", |
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160 | Type="PP", |
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161 | Components = [ "isobutane", "n-pentane", "propylene", |
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162 | "benzene", "isobutene" ], |
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163 | LiquidModel = "PR", |
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164 | VapourModel = "PR" |
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165 | ); |
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166 | NComp as Integer; |
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167 | |
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168 | SET |
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169 | NComp = PP.NumberOfComponents; |
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170 | |
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171 | DEVICES |
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172 | t1 as packedStage; |
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173 | feed as source; |
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174 | inL as liquid_stream; |
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175 | inV as vapour_stream; |
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176 | |
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177 | CONNECTIONS |
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178 | feed.Outlet to t1.Inlet; |
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179 | inL to t1.InletL; |
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180 | inV to t1.InletV; |
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181 | |
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182 | SPECIFY |
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183 | feed.Outlet.F = 0 * 'kmol/h'; |
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184 | feed.Outlet.T = 300 * 'K'; |
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185 | feed.Outlet.P = 1.66 * 'atm'; |
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186 | feed.Outlet.z = [0.226, 0.425, 0.035, 0.025, 0.289]; |
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187 | |
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188 | inL.F = 71.21 * 'kmol/h'; |
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189 | inL.P = 2.22 * 'atm'; |
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190 | inL.T = 297.6 * 'K'; |
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191 | inL.z = [0.226, 0.425, 0.035, 0.025, 0.289]; |
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192 | |
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193 | inV.F = 175.3 * 'kmol/h'; |
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194 | inV.P = 2.3062 * 'atm'; |
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195 | inV.T = 308.3 * 'K'; |
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196 | inV.z = [0.265, 0.233, 0.150, 0.014, 0.338]; |
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197 | |
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198 | t1.deltaP = 0.01 * 'atm'; |
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199 | |
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200 | SET |
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201 | #Metal Pall Ring - nominal packing size 50 mm - Billet and Schultes, 1999. |
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202 | t1.Q = 0 * 'kW'; |
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203 | t1.Cpo = 0.763; |
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204 | t1.e = 0.951; |
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205 | t1.a = 112.6 * 'm^2/m^3'; |
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206 | |
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207 | t1.V = 4 * 'ft^2' * 1 * 'ft'; |
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208 | t1.hs = 1 * 'ft'; |
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209 | t1.d = 2.26 * 'ft'; |
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210 | t1.Qsil = 10; |
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211 | |
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212 | INITIAL |
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213 | t1.OutletL.T = 290 *'K'; |
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214 | t1.ML = 0.02 * 'kmol'; |
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215 | t1.OutletL.z([1:4]) = [0.226, 0.425, 0.035, 0.025]; |
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216 | |
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217 | OPTIONS |
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218 | DAESolver(File="sundials"); |
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219 | TimeStep = 10; |
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220 | TimeEnd = 100; |
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221 | end |
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222 | |
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223 | FlowSheet trayRate_Test |
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224 | PARAMETERS |
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225 | PP as Plugin(Brief="Physical Properties", |
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226 | Type="PP", |
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227 | Components = [ "n-pentane", "benzene"], |
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228 | LiquidModel = "PR", |
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229 | VapourModel = "PR" |
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230 | ); |
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231 | NComp as Integer; |
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232 | |
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233 | SET |
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234 | NComp = PP.NumberOfComponents; |
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235 | |
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236 | DEVICES |
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237 | t1 as trayRate; |
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238 | feed as source; |
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239 | feedV as source; |
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240 | inL as liquid_stream; |
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241 | inV as vapour_stream; |
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242 | |
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243 | CONNECTIONS |
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244 | feed.Outlet to t1.Inlet; |
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245 | feedV.Outlet to t1.InletFV; |
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246 | inL to t1.InletL; |
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247 | inV to t1.InletV; |
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248 | |
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249 | SPECIFY |
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250 | feed.Outlet.F = 116 * 'kmol/h'; |
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251 | feed.Outlet.T = 280 * 'K'; |
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252 | feed.Outlet.P = 150 * 'kPa'; |
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253 | feed.Outlet.z = [0.5, 0.5]; |
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254 | |
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255 | feedV.Outlet.F = 0 * 'kmol/h'; |
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256 | feedV.Outlet.T = 280 * 'K'; |
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257 | feedV.Outlet.P = 150 * 'atm'; |
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258 | feedV.Outlet.z = [0.5, 0.5]; |
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259 | |
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260 | inL.P = 150 * 'kPa'; |
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261 | inL.T = 290 * 'K'; |
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262 | inL.F = 90 * 'kmol/h'; |
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263 | inL.z = [0.1641, 0.8359]; |
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264 | |
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265 | inV.P = 150 * 'kPa'; |
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266 | inV.T = 500 * 'K'; |
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267 | inV.z = [0.0584, 0.9416]; |
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268 | # inV.F = 62 * 'kmol/h'; |
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269 | |
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270 | t1.OutletV.F = 120 * 'kmol/h'; |
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271 | # t1.OutletL.F = 120 * 'kmol/h'; |
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272 | t1.interf.a = 40 * 'm^2'; |
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273 | t1.interf.htL = 10.01 * 'kW/m^2/K'; |
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274 | t1.interf.htV = 0.025 * 'kW/m^2/K'; |
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275 | t1.interf.kL = 0.00933 * 'm/s'; |
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276 | t1.interf.kV = 0.000236 * 'm/s'; |
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277 | |
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278 | SET |
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279 | t1.V = 4 * 'ft^3'; |
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280 | t1.Ah = 0.394 * 'ft^2'; |
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281 | t1.lw = 20.94 * 'in'; |
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282 | t1.hw = 0.125 * 'ft'; |
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283 | t1.beta = 0.6; |
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284 | t1.alfa = 4; |
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285 | t1.Ap = 3.94 * 'ft^2'; |
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286 | t1.Q = 0 * 'kW'; |
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287 | |
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288 | INITIAL |
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289 | t1.OutletL.T = 295 *'K'; |
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290 | t1.OutletV.T = 290 *'K'; |
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291 | t1.Level = 0.9 * t1.hw; |
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292 | t1.OutletL.z(1) = 0.5; |
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293 | t1.OutletV.z(1) = 0.6; |
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294 | t1.MV = 1.0*'mol' ; |
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295 | |
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296 | OPTIONS |
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297 | TimeStep = 0.1; |
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298 | TimeEnd = 10; |
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299 | TimeUnit = 's'; |
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300 | GuessFile = "trayRate_Test.rlt"; |
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301 | end |
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