1 | #*------------------------------------------------------------------- |
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2 | * Models of Column Section with Tray Efficiency Prediction |
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3 | * Author: Josias J. Junges |
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4 | *-------------------------------------------------------------------*# |
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5 | |
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6 | using "tray_Eff"; |
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7 | using "reboiler"; |
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8 | using "condenser"; |
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9 | using "mixers_splitters/splitter"; |
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10 | using "tank"; |
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11 | using "pressure_changers/pump"; |
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12 | |
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13 | Model Section_Column_EffEmp |
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14 | ATTRIBUTES |
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15 | Pallete = true; |
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16 | Icon = "icon/SectionColumn"; |
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17 | Brief = "Model of a column section - Tray Efficiency Prediction"; |
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18 | Info = |
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19 | "== Model of a column section containing == |
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20 | * NTrays trays. |
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21 | |
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22 | == Specify == |
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23 | * the feed stream of each tray (Inlet); |
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24 | |
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25 | * the InletL stream of the top tray; |
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26 | * the InletV stream of the bottom tray. |
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27 | |
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28 | == Initial Conditions == |
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29 | * the trays temperature (OutletL.T); |
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30 | * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); |
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31 | * (NoComps - 1) OutletL (OR OutletV) compositions for each tray. |
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32 | "; |
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33 | |
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34 | PARAMETERS |
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35 | outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); |
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36 | outer NComp as Integer; |
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37 | NTrays as Integer(Brief="Number of trays", Default=2); |
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38 | topdown as Integer(Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1); |
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39 | top as Integer(Brief="Number of top tray"); |
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40 | bot as Integer(Brief="Number of bottom tray"); |
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41 | xas as Integer(Brief="Adjacent above stage vapour composition"); |
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42 | |
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43 | SET |
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44 | top = (NTrays-1)*(1-topdown)/2+1; |
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45 | bot = NTrays/top; |
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46 | |
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47 | VARIABLES |
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48 | trays(NTrays) as trayEffEmp; |
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49 | |
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50 | CONNECTIONS |
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51 | trays([top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV; |
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52 | trays([top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL; |
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53 | |
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54 | EQUATIONS |
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55 | |
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56 | if NComp > 2 then |
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57 | |
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58 | (trays(top).LoutLk-trays(top).LinLK)*trays(top).m=(trays(top).VoutLk-xas); |
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59 | |
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60 | for i in [(top+1):NTrays] |
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61 | (trays(i).LoutLk-trays(i).LinLK)*trays(i).m=(trays(i).VoutLk-trays(i-1).VoutLk); |
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62 | end |
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63 | |
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64 | else |
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65 | |
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66 | (trays(top).OutletL.z(1)-trays(top).InletL.z(1))*trays(top).m=(trays(top).OutletV.z(1)-xas); |
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67 | |
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68 | for i in [(top+1):NTrays] |
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69 | (trays(i).OutletL.z(1)-trays(i).InletL.z(1))*trays(i).m=(trays(i).OutletV.z(1)-trays(i-1).OutletV.z(1)); |
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70 | end |
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71 | end |
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72 | |
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73 | end |
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74 | |
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75 | Model Section_Column_EffFund |
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76 | ATTRIBUTES |
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77 | Pallete = true; |
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78 | Icon = "icon/SectionColumn"; |
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79 | Brief = "Model of a column section - Tray Efficiency Prediction"; |
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80 | Info = |
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81 | "== Model of a column section containing == |
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82 | * NTrays trays. |
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83 | |
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84 | == Specify == |
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85 | * the feed stream of each tray (Inlet); |
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86 | |
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87 | * the InletL stream of the top tray; |
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88 | * the InletV stream of the bottom tray. |
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89 | |
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90 | == Initial Conditions == |
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91 | * the trays temperature (OutletL.T); |
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92 | * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); |
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93 | * (NoComps - 1) OutletL (OR OutletV) compositions for each tray. |
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94 | "; |
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95 | |
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96 | PARAMETERS |
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97 | outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); |
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98 | outer NComp as Integer; |
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99 | NTrays as Integer(Brief="Number of trays", Default=2); |
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100 | topdown as Integer(Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1); |
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101 | top as Integer(Brief="Number of top tray"); |
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102 | bot as Integer(Brief="Number of bottom tray"); |
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103 | xas as Real(Brief="Adjacent above stage vapour composition"); |
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104 | |
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105 | SET |
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106 | top = (NTrays-1)*(1-topdown)/2+1; |
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107 | bot = NTrays/top; |
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108 | |
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109 | VARIABLES |
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110 | trays(NTrays) as trayEffFund; |
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111 | |
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112 | CONNECTIONS |
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113 | trays([top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV; |
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114 | trays([top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL; |
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115 | |
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116 | EQUATIONS |
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117 | |
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118 | if NComp > 2 then |
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119 | |
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120 | (trays(top).LoutLk-trays(top).LinLK)*trays(top).m=(trays(top).VoutLk-xas); |
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121 | |
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122 | for i in [(top+1):NTrays] |
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123 | (trays(i).LoutLk-trays(i).LinLK)*trays(i).m=(trays(i).VoutLk-trays(i-1).VoutLk); |
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124 | end |
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125 | |
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126 | else |
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127 | |
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128 | (trays(top).OutletL.z(1)-trays(top).InletL.z(1))*trays(top).m=(trays(top).OutletV.z(1)-xas); |
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129 | |
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130 | for i in [(top+1):NTrays] |
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131 | (trays(i).OutletL.z(1)-trays(i).InletL.z(1))*trays(i).m=(trays(i).OutletV.z(1)-trays(i-1).OutletV.z(1)); |
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132 | end |
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133 | end |
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134 | end |
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135 | |
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136 | #*---------------------------------------------------------------------- |
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137 | * Models of Column with Tray Efficiency Prediction |
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138 | * Author: Josias J. Junges |
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139 | *---------------------------------------------------------------------*# |
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140 | Model Distillation_kettle_cond_EffEmp |
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141 | ATTRIBUTES |
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142 | Pallete = true; |
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143 | Icon = "icon/DistillationKettleCond"; |
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144 | Brief = "Model of a distillation column with dynamic condenser and dynamic reboiler-Tray Efficiency Prediction"; |
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145 | Info = |
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146 | "== Specify == |
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147 | * the feed stream of each tray (Inlet); |
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148 | |
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149 | * the pump pressure difference; |
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150 | * the heat supllied in reboiler and condenser; |
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151 | * the condenser vapor outlet flow (OutletV.F); |
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152 | * the reboiler liquid outlet flow (OutletL.F); |
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153 | * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. |
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154 | |
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155 | == Initial Conditions == |
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156 | * the trays temperature (OutletL.T); |
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157 | * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); |
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158 | * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; |
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159 | |
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160 | * the condenser temperature (OutletL.T); |
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161 | * the condenser liquid level (Level); |
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162 | * (NoComps - 1) OutletL (OR OutletV) compositions; |
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163 | |
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164 | * the reboiler temperature (OutletL.T); |
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165 | * the reboiler liquid level (Level); |
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166 | * (NoComps - 1) OutletL (OR OutletV) compositions. |
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167 | "; |
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168 | |
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169 | PARAMETERS |
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170 | outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); |
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171 | outer NComp as Integer; |
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172 | NTrays as Integer(Brief="Number of trays", Default=2); |
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173 | topdown as Integer(Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1); |
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174 | top as Integer(Brief="Number of top tray"); |
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175 | bot as Integer(Brief="Number of bottom tray"); |
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176 | VapourFlow as Switcher(Valid = ["on", "off"], Default = "on"); |
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177 | outer iLK as Integer (Brief="Pseudo-binary ligth key index"); |
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178 | outer iHK as Integer (Brief="Pseudo-binary heavy key index"); |
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179 | |
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180 | SET |
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181 | top = (NTrays-1)*(1-topdown)/2+1; |
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182 | bot = NTrays/top; |
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183 | |
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184 | VARIABLES |
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185 | trays(NTrays) as trayEffEmp; |
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186 | cond as condenser; |
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187 | reb as reboiler; |
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188 | sptop as splitter; |
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189 | pump1 as pump; |
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190 | alfaTopo as Real; |
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191 | condVoutLk as positive (Brief="Pseudo-binary approach"); |
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192 | |
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193 | EQUATIONS |
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194 | switch VapourFlow |
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195 | case "on": |
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196 | cond.InletV.F*trays(top).vV = alfaTopo * trays(top).Ah * sqrt(2*(trays(top).OutletV.P - |
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197 | cond.OutletL.P + 1e-8 * 'atm') / (trays(top).alfa*trays(top).rhoV)); |
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198 | when cond.InletV.F < 1e-6 * 'kmol/h' switchto "off"; |
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199 | |
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200 | case "off": |
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201 | cond.InletV.F = 0 * 'mol/s'; |
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202 | when trays(top).OutletV.P > cond.OutletL.P + 1e-1 * 'atm' switchto "on"; |
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203 | end |
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204 | |
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205 | "Condenser pseudo-binary approach" |
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206 | condVoutLk=cond.OutletV.z(iLK)/(cond.OutletV.z(iLK)+cond.OutletV.z(iHK)); |
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207 | |
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208 | CONNECTIONS |
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209 | #vapor |
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210 | reb.OutletV to trays(bot).InletV; |
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211 | trays([top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV; |
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212 | trays(top).OutletV to cond.InletV; |
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213 | |
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214 | #liquid |
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215 | cond.OutletL to sptop.Inlet; |
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216 | sptop.Outlet2 to pump1.Inlet; |
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217 | pump1.Outlet to trays(top).InletL; |
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218 | trays([top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL; |
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219 | trays(bot).OutletL to reb.InletL; |
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220 | |
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221 | EQUATIONS |
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222 | |
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223 | if NComp > 2 then |
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224 | |
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225 | (trays(top).LoutLk-trays(top).LinLK)*trays(top).m=(trays(top).VoutLk-condVoutLk); |
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226 | |
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227 | for i in [(top+1):NTrays] |
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228 | (trays(i).LoutLk-trays(i).LinLK)*trays(i).m=(trays(i).VoutLk-trays(i-1).VoutLk); |
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229 | end |
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230 | |
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231 | else |
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232 | |
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233 | (trays(top).OutletL.z(1)-trays(top).InletL.z(1))*trays(top).m=(trays(top).OutletV.z(1)-cond.OutletV.z(1)); |
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234 | |
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235 | for i in [(top+1):NTrays] |
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236 | (trays(i).OutletL.z(1)-trays(i).InletL.z(1))*trays(i).m=(trays(i).OutletV.z(1)-trays(i-1).OutletV.z(1)); |
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237 | end |
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238 | end |
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239 | end |
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240 | |
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241 | Model Distillation_kettle_cond_EffFund |
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242 | ATTRIBUTES |
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243 | Pallete = true; |
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244 | Icon = "icon/DistillationKettleCond"; |
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245 | Brief = "Model of a distillation column with dynamic condenser and dynamic reboiler-Tray Efficiency Prediction"; |
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246 | Info = |
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247 | "== Specify == |
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248 | * the feed stream of each tray (Inlet); |
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249 | |
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250 | * the pump pressure difference; |
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251 | * the heat supllied in reboiler and condenser; |
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252 | * the condenser vapor outlet flow (OutletV.F); |
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253 | * the reboiler liquid outlet flow (OutletL.F); |
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254 | * both splitter outlet flows OR one of the splitter outlet flows and the splitter frac. |
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255 | |
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256 | == Initial Conditions == |
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257 | * the trays temperature (OutletL.T); |
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258 | * the trays liquid level (Level) OR the trays liquid flow (OutletL.F); |
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259 | * (NoComps - 1) OutletL (OR OutletV) compositions for each tray; |
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260 | |
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261 | * the condenser temperature (OutletL.T); |
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262 | * the condenser liquid level (Level); |
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263 | * (NoComps - 1) OutletL (OR OutletV) compositions; |
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264 | |
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265 | * the reboiler temperature (OutletL.T); |
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266 | * the reboiler liquid level (Level); |
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267 | * (NoComps - 1) OutletL (OR OutletV) compositions. |
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268 | "; |
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269 | |
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270 | PARAMETERS |
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271 | outer PP as Plugin(Brief = "External Physical Properties", Type="PP"); |
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272 | outer NComp as Integer; |
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273 | NTrays as Integer(Brief="Number of trays", Default=2); |
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274 | topdown as Integer(Brief="Trays counting (1=top-down, -1=bottom-up)", Default=1); |
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275 | top as Integer(Brief="Number of top tray"); |
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276 | bot as Integer(Brief="Number of bottom tray"); |
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277 | VapourFlow as Switcher(Valid = ["on", "off"], Default = "on"); |
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278 | outer iLK as Integer (Brief="Pseudo-binary ligth key index"); |
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279 | outer iHK as Integer (Brief="Pseudo-binary heavy key index"); |
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280 | |
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281 | SET |
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282 | top = (NTrays-1)*(1-topdown)/2+1; |
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283 | bot = NTrays/top; |
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284 | |
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285 | VARIABLES |
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286 | trays(NTrays) as trayEffFund; |
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287 | cond as condenser; |
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288 | reb as reboiler; |
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289 | sptop as splitter; |
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290 | pump1 as pump; |
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291 | alfaTopo as Real; |
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292 | condVoutLk as positive (Brief="Pseudo-binary approach"); |
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293 | |
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294 | EQUATIONS |
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295 | switch VapourFlow |
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296 | case "on": |
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297 | cond.InletV.F*trays(top).vV = alfaTopo * trays(top).Ah * sqrt(2*(trays(top).OutletV.P - |
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298 | cond.OutletL.P + 1e-8 * 'atm') / (trays(top).alfa*trays(top).rhoV)); |
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299 | when cond.InletV.F < 1e-6 * 'kmol/h' switchto "off"; |
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300 | |
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301 | case "off": |
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302 | cond.InletV.F = 0 * 'mol/s'; |
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303 | when trays(top).OutletV.P > cond.OutletL.P + 1e-1 * 'atm' switchto "on"; |
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304 | end |
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305 | |
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306 | "Condenser pseudo-binary approach" |
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307 | condVoutLk=cond.OutletV.z(iLK)/(cond.OutletV.z(iLK)+cond.OutletV.z(iHK)); |
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308 | |
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309 | CONNECTIONS |
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310 | #vapor |
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311 | reb.OutletV to trays(bot).InletV; |
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312 | trays([top+topdown:topdown:bot]).OutletV to trays([top:topdown:bot-topdown]).InletV; |
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313 | trays(top).OutletV to cond.InletV; |
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314 | |
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315 | #liquid |
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316 | cond.OutletL to sptop.Inlet; |
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317 | sptop.Outlet2 to pump1.Inlet; |
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318 | pump1.Outlet to trays(top).InletL; |
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319 | trays([top:topdown:bot-topdown]).OutletL to trays([top+topdown:topdown:bot]).InletL; |
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320 | trays(bot).OutletL to reb.InletL; |
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321 | |
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322 | EQUATIONS |
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323 | |
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324 | if NComp > 2 then |
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325 | |
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326 | (trays(top).LoutLk-trays(top).LinLK)*trays(top).m=(trays(top).VoutLk-condVoutLk); |
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327 | |
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328 | for i in [(top+1):NTrays] |
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329 | (trays(i).LoutLk-trays(i).LinLK)*trays(i).m=(trays(i).VoutLk-trays(i-1).VoutLk); |
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330 | end |
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331 | |
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332 | else |
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333 | |
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334 | (trays(top).OutletL.z(1)-trays(top).InletL.z(1))*trays(top).m=(trays(top).OutletV.z(1)-cond.OutletV.z(1)); |
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335 | |
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336 | for i in [(top+1):NTrays] |
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337 | (trays(i).OutletL.z(1)-trays(i).InletL.z(1))*trays(i).m=(trays(i).OutletV.z(1)-trays(i-1).OutletV.z(1)); |
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338 | end |
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339 | end |
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340 | end |
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