- Timestamp:
- Feb 13, 2009, 5:33:49 PM (15 years ago)
- Location:
- branches/gui
- Files:
-
- 4 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/stage_separators/flash.mso
r584 r711 20 20 21 21 Model flash 22 ATTRIBUTES 22 23 ATTRIBUTES 23 24 Pallete = true; 24 25 Icon = "icon/Flash"; … … 33 34 34 35 == Initial Conditions == 35 * the flash initial temperature (OutletL.T);36 * the flash initial level (Level);37 * (NoComps - 1) OutletL (OR OutletV) compositions.36 * The flash initial temperature (Temperature_Initial); 37 * The flash initial level (Levelpercent_Initial); 38 *The Outlet Liquid Composition (Composition_Initial). 38 39 "; 39 40 40 PARAMETERS 41 outer PP as Plugin (Brief = "External Physical Properties", Type="PP"); 42 outer NComp as Integer (Brief = "Number of chemical components", Lower = 1); 43 V as volume (Brief="Total Volume of the flash"); 44 Mw(NComp) as molweight(Protected=true); 45 orientation as Switcher (Valid=["vertical","horizontal"],Default="vertical"); 46 diameter as length (Brief="Vessel diameter"); 47 48 SET 41 PARAMETERS 42 43 outer PP as Plugin (Brief = "External Physical Properties", Type="PP"); 44 outer NComp as Integer (Brief = "Number of chemical components", Lower = 1); 45 46 VesselVolume as volume (Brief="Total Volume of the flash"); 47 Mw(NComp) as molweight (Hidden=true); 48 Orientation as Switcher (Valid=["vertical","horizontal"],Default="vertical"); 49 Diameter as length (Brief="Vessel diameter"); 50 51 Levelpercent_Initial as positive (Brief="Initial liquid height in Percent", Default = 0.70); 52 Temperature_Initial as temperature (Brief="Initial Liquid Temperature", Default = 330); 53 Composition_Initial(NComp) as fraction (Brief="Initial Composition", Default = 0.10); 54 55 SET 56 49 57 Mw=PP.MolecularWeight(); 50 58 51 VARIABLES 52 in Inlet as stream(Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 53 out OutletL as liquid_stream(Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 54 out OutletV as vapour_stream(Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 55 in InletQ as power(Brief="Rate of heat supply", PosX=1, PosY=0.7559, Symbol="_{in}"); 56 57 M(NComp) as mol (Brief="Molar Holdup in the tray", Protected=true); 58 ML as mol (Brief="Molar liquid holdup", Protected=true); 59 MV as mol (Brief="Molar vapour holdup", Protected=true); 60 E as energy (Brief="Total Energy Holdup on tray", Protected=true); 61 vL as volume_mol (Brief="Liquid Molar Volume", Protected=true); 62 vV as volume_mol (Brief="Vapour Molar volume", Protected=true); 63 Level as length (Brief="liquid height"); 64 Across as area (Brief="Flash Cross section area", Protected=true); 65 vfrac as positive (Brief="Vapourization fraction", Symbol="\phi"); 66 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}"); 67 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P"); 68 69 out TI as control_signal(Brief="Temperature Indicator", PosX=1, PosY=0.2); 70 out PI as control_signal(Brief="Pressure Indicator", PosX=1, PosY=0.3); 71 out LI as control_signal(Brief="Level Indicator", PosX=1, PosY=0.4); 72 73 EQUATIONS 74 "Component Molar Balance" 75 diff(M)=Inlet.F*Inlet.z - OutletL.F*OutletL.z - OutletV.F*OutletV.z; 76 77 "Energy Balance" 78 diff(E) = Inlet.F*Inlet.h - OutletL.F*OutletL.h - OutletV.F*OutletV.h + InletQ; 79 80 "Molar Holdup" 81 M = ML*OutletL.z + MV*OutletV.z; 82 83 "Energy Holdup" 84 E = ML*OutletL.h + MV*OutletV.h - OutletL.P*V; 85 86 "Mol fraction normalisation" 87 sum(OutletL.z)=1.0; 88 89 "Mol fraction normalisation" 90 sum(OutletL.z)=sum(OutletV.z); 91 92 "Vaporization Fraction" 93 OutletV.F = Inlet.F * vfrac; 94 95 "Liquid Volume" 96 vL = PP.LiquidVolume(OutletL.T, OutletL.P, OutletL.z); 97 98 "Vapour Volume" 99 vV = PP.VapourVolume(OutletV.T, OutletV.P, OutletV.z); 100 101 "Chemical Equilibrium" 102 PP.LiquidFugacityCoefficient(OutletL.T, OutletL.P, OutletL.z)*OutletL.z = 103 PP.VapourFugacityCoefficient(OutletV.T, OutletV.P, OutletV.z)*OutletV.z; 104 105 "Thermal Equilibrium" 106 OutletV.T = OutletL.T; 107 108 "Mechanical Equilibrium" 109 OutletV.P = OutletL.P; 110 111 "Pressure Drop" 112 OutletL.P = Inlet.P - Pdrop; 113 114 "Pressure Ratio" 115 OutletL.P = Inlet.P * Pratio; 116 117 "Geometry Constraint" 118 V = ML * vL + MV * vV; 119 120 "Temperature indicator" 121 TI * 'K' = OutletL.T - 273.15*'K'; 122 "Pressure indicator" 123 PI * 'atm' = OutletL.P; 124 "Level indicator" 125 LI*V = Level*Across; 126 127 switch orientation 59 VARIABLES 60 61 in Inlet as stream (Brief="Feed Stream", PosX=0, PosY=0.5421, Symbol="_{in}"); 62 out OutletLiquid as liquid_stream (Brief="Liquid outlet stream", PosX=0.4790, PosY=1, Symbol="_{outL}"); 63 out OutletVapour as vapour_stream (Brief="Vapour outlet stream", PosX=0.4877, PosY=0, Symbol="_{outV}"); 64 in InletQ as power (Brief="Rate of heat supply", PosX=1, PosY=0.7559, Protected =true,Symbol="_{in}"); 65 66 TotalHoldup(NComp) as mol (Brief="Molar Holdup in the Vessel", Protected=true); 67 LiquidHoldup as mol (Brief="Molar liquid holdup", Protected=true); 68 VapourHoldup as mol (Brief="Molar vapour holdup", Protected=true); 69 70 E as energy (Brief="Total Energy Holdup in the Vessel", Protected=true); 71 vL as volume_mol (Brief="Liquid Molar Volume", Protected=true); 72 vV as volume_mol (Brief="Vapour Molar volume", Protected=true); 73 Level as length (Brief="liquid height", Protected=true); 74 Across as area (Brief="Flash Cross section area", Protected=true); 75 vfrac as positive (Brief="Vapourization fraction", Symbol="\phi", Protected=true); 76 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}", Protected=true); 77 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P", Protected=true); 78 79 out TI as control_signal (Brief="Temperature Indicator", PosX=1, PosY=0.2, Protected=true); 80 out PI as control_signal (Brief="Pressure Indicator", PosX=1, PosY=0.3, Protected=true); 81 out LI as control_signal (Brief="Level Indicator", PosX=1, PosY=0.4, Protected=true); 82 83 INITIAL 84 85 # initial level Percent 86 LI = Levelpercent_Initial; 87 88 # initial Outlet Liquid Temperature 89 OutletLiquid.T = Temperature_Initial; 90 91 # initial Outlet Liquid Composition Normalized 92 OutletLiquid.z(1:NComp - 1) = Composition_Initial(1:NComp - 1)/sum(Composition_Initial); 93 94 EQUATIONS 95 96 "Component Molar Balance" 97 diff(TotalHoldup)=Inlet.F*Inlet.z - OutletLiquid.F*OutletLiquid.z - OutletVapour.F*OutletVapour.z; 98 99 "Energy Balance" 100 diff(E) = Inlet.F*Inlet.h - OutletLiquid.F*OutletLiquid.h - OutletVapour.F*OutletVapour.h + InletQ; 101 102 "Molar Holdup" 103 TotalHoldup = LiquidHoldup*OutletLiquid.z + VapourHoldup*OutletVapour.z; 104 105 "Energy Holdup" 106 E = LiquidHoldup*OutletLiquid.h + VapourHoldup*OutletVapour.h - OutletLiquid.P*VesselVolume; 107 108 "Mol fraction normalisation" 109 sum(OutletLiquid.z)=1.0; 110 111 "Mol fraction normalisation" 112 sum(OutletLiquid.z)=sum(OutletVapour.z); 113 114 "Vaporization Fraction" 115 OutletVapour.F = Inlet.F * vfrac; 116 117 "Liquid Volume" 118 vL = PP.LiquidVolume(OutletLiquid.T, OutletLiquid.P, OutletLiquid.z); 119 120 "Vapour Volume" 121 vV = PP.VapourVolume(OutletVapour.T, OutletVapour.P, OutletVapour.z); 122 123 "Chemical Equilibrium" 124 PP.LiquidFugacityCoefficient(OutletLiquid.T, OutletLiquid.P, OutletLiquid.z)*OutletLiquid.z = 125 PP.VapourFugacityCoefficient(OutletVapour.T, OutletVapour.P, OutletVapour.z)*OutletVapour.z; 126 127 "Thermal Equilibrium" 128 OutletVapour.T = OutletLiquid.T; 129 130 "Mechanical Equilibrium" 131 OutletVapour.P = OutletLiquid.P; 132 133 "Pressure Drop" 134 OutletLiquid.P = Inlet.P - Pdrop; 135 136 "Pressure Ratio" 137 OutletLiquid.P = Inlet.P * Pratio; 138 139 "Geometry Constraint" 140 VesselVolume = LiquidHoldup * vL + VapourHoldup * vV; 141 142 "Temperature indicator Celsius Degree" 143 TI * 'K' = OutletLiquid.T - 273.15*'K'; 144 145 "Pressure indicator" 146 PI * 'atm' = OutletLiquid.P; 147 148 "Level indicator" 149 LI*VesselVolume= Level*Across; 150 151 switch Orientation 128 152 case "vertical": 129 153 "Cross Section Area" 130 Across = 0.5 * asin(1) * diameter^2;154 Across = 0.5 * asin(1) * Diameter^2; 131 155 132 156 "Liquid Level" 133 ML* vL = Across * Level;157 LiquidHoldup * vL = Across * Level; 134 158 135 159 case "horizontal": 136 160 "Cylindrical Side Area" 137 Across = 0.25* diameter^2 * (asin(1) - asin((diameter - 2*Level)/diameter)) +138 (Level - 0.5* diameter)*sqrt(Level*(diameter - Level));161 Across = 0.25*Diameter^2 * (asin(1) - asin((Diameter - 2*Level)/Diameter)) + 162 (Level - 0.5*Diameter)*sqrt(Level*(Diameter - Level)); 139 163 140 164 "Liquid Level" 141 0.5 * asin(1) * diameter^2 * ML* vL = Across * V; 142 end 165 0.5 * asin(1) * Diameter^2 * LiquidHoldup* vL = Across * VesselVolume; 166 end 167 143 168 end 144 169 -
branches/gui/sample/stage_separators/Sample_flash_PID.pfd
r684 r711 32 32 <View> 33 33 <Zoom_Level>1</Zoom_Level> 34 <Show_Grid> 1</Show_Grid>35 <Snap_to_Grid> 1</Snap_to_Grid>36 <Width>1 260</Width>37 <Height> 580</Height>34 <Show_Grid>0</Show_Grid> 35 <Snap_to_Grid>0</Snap_to_Grid> 36 <Width>1016</Width> 37 <Height>612</Height> 38 38 <X>0</X> 39 39 <Y>0</Y> … … 41 41 <View> 42 42 <Zoom_Level>1</Zoom_Level> 43 <Show_Grid> 1</Show_Grid>44 <Snap_to_Grid> 1</Snap_to_Grid>45 <Width>1 260</Width>43 <Show_Grid>0</Show_Grid> 44 <Snap_to_Grid>0</Snap_to_Grid> 45 <Width>1016</Width> 46 46 <Height>0</Height> 47 47 <X>0</X> … … 156 156 <Block_Properties> 157 157 <Model_File_Path>stage_separators/flash</Model_File_Path> 158 <Instance_Id>OutletL </Instance_Id>159 <Model_Name>OutletL </Model_Name>158 <Instance_Id>OutletLiquid</Instance_Id> 159 <Model_Name>OutletLiquid</Model_Name> 160 160 <T_Connection>2</T_Connection> 161 161 <Base_Models> 162 162 <Block_Properties> 163 163 <Model_File_Path>streams</Model_File_Path> 164 <Instance_Id>OutletL </Instance_Id>164 <Instance_Id>OutletLiquid</Instance_Id> 165 165 <Model_Name>liquid_stream</Model_Name> 166 166 <T_Connection>2</T_Connection> … … 168 168 <Block_Properties> 169 169 <Model_File_Path>streams</Model_File_Path> 170 <Instance_Id>OutletL </Instance_Id>170 <Instance_Id>OutletLiquid</Instance_Id> 171 171 <Model_Name>stream</Model_Name> 172 172 <T_Connection>2</T_Connection> 173 <Parameters>174 <Desc>NComp</Desc>175 <Index>0</Index>176 <Values>3</Values>177 <Status>0</Status>178 </Parameters>179 <Variables>180 <Desc>F</Desc>181 <Index>0</Index>182 <Values>315.508</Values>183 <Status>0</Status>184 <Unit>kmol/h</Unit>185 </Variables>186 <Variables>187 <Desc>T</Desc>188 <Index>0</Index>189 <Values>333.224</Values>190 <Status>2</Status>191 <Unit>K</Unit>192 </Variables>193 <Variables>194 <Desc>P</Desc>195 <Index>0</Index>196 <Values>0.6</Values>197 <Status>0</Status>198 <Unit>atm</Unit>199 </Variables>200 <Variables>201 <Desc>h</Desc>202 <Index>0</Index>203 <Values>-26874.5</Values>204 <Status>0</Status>205 <Unit>kJ/kmol</Unit>206 </Variables>207 <Variables>208 <Desc>v</Desc>209 <Index>0</Index>210 <Values>0</Values>211 <Status>0</Status>212 </Variables>213 <Variables>214 <Desc>z</Desc>215 <Index>0</Index>216 <Values>0.0860913</Values>217 <Status>2</Status>218 <Index>1</Index>219 <Values>0.321186</Values>220 <Status>2</Status>221 <Index>2</Index>222 <Values>0.592723</Values>223 <Status>0</Status>224 </Variables>225 173 </Block_Properties> 226 174 </Base_Models> … … 238 186 <Block_Properties> 239 187 <Model_File_Path>stage_separators/flash</Model_File_Path> 240 <Instance_Id>OutletV </Instance_Id>241 <Model_Name>OutletV </Model_Name>188 <Instance_Id>OutletVapour</Instance_Id> 189 <Model_Name>OutletVapour</Model_Name> 242 190 <T_Connection>2</T_Connection> 243 191 <Base_Models> 244 192 <Block_Properties> 245 193 <Model_File_Path>streams</Model_File_Path> 246 <Instance_Id>OutletV </Instance_Id>194 <Instance_Id>OutletVapour</Instance_Id> 247 195 <Model_Name>vapour_stream</Model_Name> 248 196 <T_Connection>2</T_Connection> … … 250 198 <Block_Properties> 251 199 <Model_File_Path>streams</Model_File_Path> 252 <Instance_Id>OutletV </Instance_Id>200 <Instance_Id>OutletVapour</Instance_Id> 253 201 <Model_Name>stream</Model_Name> 254 202 <T_Connection>2</T_Connection> 255 <Parameters>256 <Desc>NComp</Desc>257 <Index>0</Index>258 <Values>3</Values>259 <Status>0</Status>260 </Parameters>261 <Variables>262 <Desc>F</Desc>263 <Index>0</Index>264 <Values>184.492</Values>265 <Status>0</Status>266 <Unit>kmol/h</Unit>267 </Variables>268 <Variables>269 <Desc>T</Desc>270 <Index>0</Index>271 <Values>333.224</Values>272 <Status>0</Status>273 <Unit>K</Unit>274 </Variables>275 <Variables>276 <Desc>P</Desc>277 <Index>0</Index>278 <Values>0.6</Values>279 <Status>0</Status>280 <Unit>atm</Unit>281 </Variables>282 <Variables>283 <Desc>h</Desc>284 <Index>0</Index>285 <Values>3428.57</Values>286 <Status>0</Status>287 <Unit>kJ/kmol</Unit>288 </Variables>289 <Variables>290 <Desc>v</Desc>291 <Index>0</Index>292 <Values>1</Values>293 <Status>0</Status>294 </Variables>295 <Variables>296 <Desc>z</Desc>297 <Index>0</Index>298 <Values>0.665815</Values>299 <Status>0</Status>300 <Index>1</Index>301 <Values>0.263769</Values>302 <Status>0</Status>303 <Index>2</Index>304 <Values>0.0704164</Values>305 <Status>0</Status>306 </Variables>307 203 </Block_Properties> 308 204 </Base_Models> … … 330 226 </Parameters> 331 227 <Parameters> 332 <Desc>V</Desc> 333 <Index>0</Index> 334 <Values>2</Values> 335 <Status>4</Status> 336 <Unit>m^3</Unit> 337 </Parameters> 338 <Parameters> 339 <Desc>Mw</Desc> 340 <Index>0</Index> 341 <Values>58.123</Values> 342 <Status>0</Status> 343 <Unit>kg/kmol</Unit> 344 <Index>1</Index> 345 <Values>78.1134</Values> 346 <Status>0</Status> 347 <Unit>kg/kmol</Unit> 348 <Index>2</Index> 349 <Values>114.23</Values> 350 <Status>0</Status> 351 <Unit>kg/kmol</Unit> 352 </Parameters> 353 <Parameters> 354 <Desc>orientation</Desc> 228 <Desc>Orientation</Desc> 355 229 <Index>0</Index> 356 230 <Values>vertical</Values> 357 <Status>4</Status> 358 </Parameters> 359 <Parameters> 360 <Desc>diameter</Desc> 361 <Index>0</Index> 362 <Values>0.5</Values> 363 <Status>4</Status> 364 <Unit>m</Unit> 231 <Status>0</Status> 365 232 </Parameters> 366 233 <Variables> … … 370 237 <Status>0</Status> 371 238 <Unit>kW</Unit> 372 </Variables>373 <Variables>374 <Desc>M</Desc>375 <Index>0</Index>376 <Values>0.543784</Values>377 <Status>0</Status>378 <Unit>kmol</Unit>379 <Index>1</Index>380 <Values>1.97928</Values>381 <Status>0</Status>382 <Unit>kmol</Unit>383 <Index>2</Index>384 <Values>3.64333</Values>385 <Status>0</Status>386 <Unit>kmol</Unit>387 </Variables>388 <Variables>389 <Desc>ML</Desc>390 <Index>0</Index>391 <Values>6.14412</Values>392 <Status>0</Status>393 <Unit>kmol</Unit>394 </Variables>395 <Variables>396 <Desc>MV</Desc>397 <Index>0</Index>398 <Values>0.022271</Values>399 <Status>0</Status>400 <Unit>kmol</Unit>401 239 </Variables> 402 240 <Variables> … … 814 652 <Block_Properties> 815 653 <Model_File_Path>pressure_changers/valve</Model_File_Path> 816 <Instance_Id>valve_ flow_1</Instance_Id>654 <Instance_Id>valve_liquid</Instance_Id> 817 655 <Model_Name>valve_flow</Model_Name> 818 656 <T_Connection>0</T_Connection> … … 998 836 <Block_Properties> 999 837 <Model_File_Path>pressure_changers/valve</Model_File_Path> 1000 <Instance_Id>valve_ flow_1_1</Instance_Id>838 <Instance_Id>valve_Vapour</Instance_Id> 1001 839 <Model_Name>valve_flow</Model_Name> 1002 840 <T_Connection>0</T_Connection> … … 1182 1020 <Block_Properties> 1183 1021 <Model_File_Path>controllers/PIDs</Model_File_Path> 1184 <Instance_Id>PID_ 1</Instance_Id>1022 <Instance_Id>PID_LC</Instance_Id> 1185 1023 <Model_Name>PID</Model_Name> 1186 1024 <T_Connection>0</T_Connection> … … 1322 1160 <Block_Properties> 1323 1161 <Model_File_Path>controllers/PIDs</Model_File_Path> 1324 <Instance_Id>PID_ 1</Instance_Id>1162 <Instance_Id>PID_PC</Instance_Id> 1325 1163 <Model_Name>PID</Model_Name> 1326 1164 <T_Connection>0</T_Connection> … … 1462 1300 <Block_Properties> 1463 1301 <Model_File_Path>streams</Model_File_Path> 1464 <Instance_Id> VaporProduct</Instance_Id>1302 <Instance_Id>LiquidProduct</Instance_Id> 1465 1303 <Model_Name>sink</Model_Name> 1466 1304 <T_Connection>0</T_Connection> … … 1620 1458 <Status>0</Status> 1621 1459 <Unit>K</Unit> 1460 </Variables> 1461 </Block_Properties> 1462 </Block> 1463 <Block> 1464 <Type>flash</Type> 1465 <Id_String>F101_1</Id_String> 1466 <Image_File_Name>/home/bicca/apps/biblioteca/branches/gui/eml/stage_separators/icon/Flash.png</Image_File_Name> 1467 <X>314</X> 1468 <Y>142</Y> 1469 <Z>0</Z> 1470 <Width>140</Width> 1471 <Height>225</Height> 1472 <Block_Properties> 1473 <Model_File_Path>stage_separators/flash</Model_File_Path> 1474 <Instance_Id>F101</Instance_Id> 1475 <Model_Name>flash</Model_Name> 1476 <T_Connection>0</T_Connection> 1477 <Sub_Models> 1478 <Block_Properties> 1479 <Model_File_Path>stage_separators/flash</Model_File_Path> 1480 <Instance_Id>Inlet</Instance_Id> 1481 <Model_Name>Inlet</Model_Name> 1482 <T_Connection>1</T_Connection> 1483 <Base_Models> 1484 <Block_Properties> 1485 <Model_File_Path>streams</Model_File_Path> 1486 <Instance_Id>Inlet</Instance_Id> 1487 <Model_Name>stream</Model_Name> 1488 <T_Connection>1</T_Connection> 1489 <Parameters> 1490 <Desc>NComp</Desc> 1491 <Index>0</Index> 1492 <Values>3</Values> 1493 <Status>0</Status> 1494 </Parameters> 1495 <Variables> 1496 <Desc>F</Desc> 1497 <Index>0</Index> 1498 <Values>500</Values> 1499 <Status>0</Status> 1500 <Unit>kmol/h</Unit> 1501 </Variables> 1502 <Variables> 1503 <Desc>T</Desc> 1504 <Index>0</Index> 1505 <Values>338</Values> 1506 <Status>0</Status> 1507 <Unit>K</Unit> 1508 </Variables> 1509 <Variables> 1510 <Desc>P</Desc> 1511 <Index>0</Index> 1512 <Values>5</Values> 1513 <Status>0</Status> 1514 <Unit>atm</Unit> 1515 </Variables> 1516 <Variables> 1517 <Desc>h</Desc> 1518 <Index>0</Index> 1519 <Values>-23082.6</Values> 1520 <Status>0</Status> 1521 <Unit>kJ/kmol</Unit> 1522 </Variables> 1523 <Variables> 1524 <Desc>v</Desc> 1525 <Index>0</Index> 1526 <Values>0</Values> 1527 <Status>0</Status> 1528 </Variables> 1529 <Variables> 1530 <Desc>z</Desc> 1531 <Index>0</Index> 1532 <Values>0.3</Values> 1533 <Status>0</Status> 1534 <Index>1</Index> 1535 <Values>0.3</Values> 1536 <Status>0</Status> 1537 <Index>2</Index> 1538 <Values>0.4</Values> 1539 <Status>0</Status> 1540 </Variables> 1541 </Block_Properties> 1542 </Base_Models> 1543 </Block_Properties> 1544 </Sub_Models> 1545 <Sub_Models> 1546 <Block_Properties> 1547 <Model_File_Path>stage_separators/flash</Model_File_Path> 1548 <Instance_Id>OutletLiquid</Instance_Id> 1549 <Model_Name>OutletLiquid</Model_Name> 1550 <T_Connection>2</T_Connection> 1551 <Base_Models> 1552 <Block_Properties> 1553 <Model_File_Path>streams</Model_File_Path> 1554 <Instance_Id>OutletLiquid</Instance_Id> 1555 <Model_Name>liquid_stream</Model_Name> 1556 <T_Connection>2</T_Connection> 1557 <Base_Models> 1558 <Block_Properties> 1559 <Model_File_Path>streams</Model_File_Path> 1560 <Instance_Id>OutletLiquid</Instance_Id> 1561 <Model_Name>stream</Model_Name> 1562 <T_Connection>2</T_Connection> 1563 <Parameters> 1564 <Desc>NComp</Desc> 1565 <Index>0</Index> 1566 <Values>3</Values> 1567 <Status>0</Status> 1568 </Parameters> 1569 <Variables> 1570 <Desc>F</Desc> 1571 <Index>0</Index> 1572 <Values>96.3975</Values> 1573 <Status>0</Status> 1574 <Unit>kmol/h</Unit> 1575 </Variables> 1576 <Variables> 1577 <Desc>T</Desc> 1578 <Index>0</Index> 1579 <Values>316.758</Values> 1580 <Status>0</Status> 1581 <Unit>K</Unit> 1582 </Variables> 1583 <Variables> 1584 <Desc>P</Desc> 1585 <Index>0</Index> 1586 <Values>0.247012</Values> 1587 <Status>0</Status> 1588 <Unit>atm</Unit> 1589 </Variables> 1590 <Variables> 1591 <Desc>h</Desc> 1592 <Index>0</Index> 1593 <Values>-30704.6</Values> 1594 <Status>0</Status> 1595 <Unit>kJ/kmol</Unit> 1596 </Variables> 1597 <Variables> 1598 <Desc>v</Desc> 1599 <Index>0</Index> 1600 <Values>0</Values> 1601 <Status>0</Status> 1602 </Variables> 1603 <Variables> 1604 <Desc>z</Desc> 1605 <Index>0</Index> 1606 <Values>0.0468708</Values> 1607 <Status>0</Status> 1608 <Index>1</Index> 1609 <Values>0.343192</Values> 1610 <Status>0</Status> 1611 <Index>2</Index> 1612 <Values>0.609937</Values> 1613 <Status>0</Status> 1614 </Variables> 1615 </Block_Properties> 1616 </Base_Models> 1617 <Parameters> 1618 <Desc>PP</Desc> 1619 <Index>0</Index> 1620 <Values>PP</Values> 1621 <Status>0</Status> 1622 </Parameters> 1623 </Block_Properties> 1624 </Base_Models> 1625 </Block_Properties> 1626 </Sub_Models> 1627 <Sub_Models> 1628 <Block_Properties> 1629 <Model_File_Path>stage_separators/flash</Model_File_Path> 1630 <Instance_Id>OutletVapour</Instance_Id> 1631 <Model_Name>OutletVapour</Model_Name> 1632 <T_Connection>2</T_Connection> 1633 <Base_Models> 1634 <Block_Properties> 1635 <Model_File_Path>streams</Model_File_Path> 1636 <Instance_Id>OutletVapour</Instance_Id> 1637 <Model_Name>vapour_stream</Model_Name> 1638 <T_Connection>2</T_Connection> 1639 <Base_Models> 1640 <Block_Properties> 1641 <Model_File_Path>streams</Model_File_Path> 1642 <Instance_Id>OutletVapour</Instance_Id> 1643 <Model_Name>stream</Model_Name> 1644 <T_Connection>2</T_Connection> 1645 <Parameters> 1646 <Desc>NComp</Desc> 1647 <Index>0</Index> 1648 <Values>3</Values> 1649 <Status>0</Status> 1650 </Parameters> 1651 <Variables> 1652 <Desc>F</Desc> 1653 <Index>0</Index> 1654 <Values>193.067</Values> 1655 <Status>0</Status> 1656 <Unit>kmol/h</Unit> 1657 </Variables> 1658 <Variables> 1659 <Desc>T</Desc> 1660 <Index>0</Index> 1661 <Values>316.758</Values> 1662 <Status>0</Status> 1663 <Unit>K</Unit> 1664 </Variables> 1665 <Variables> 1666 <Desc>P</Desc> 1667 <Index>0</Index> 1668 <Values>0.247012</Values> 1669 <Status>0</Status> 1670 <Unit>atm</Unit> 1671 </Variables> 1672 <Variables> 1673 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branches/gui/sample/stage_separators/Sample_flash_PIDincr.pfd
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branches/gui/sample/stage_separators/sample_flash.pfd
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1349 <Status>0</Status> 1334 1350 <Unit>m^3/h</Unit> … … 1337 1353 <Desc>T_Cdeg</Desc> 1338 1354 <Index>0</Index> 1339 <Values> 57.361</Values>1355 <Values>90.1364</Values> 1340 1356 <Status>0</Status> 1341 1357 <Unit>K</Unit> … … 1579 1595 <Block_Properties> 1580 1596 <Model_File_Path>controllers/PIDs</Model_File_Path> 1581 <Instance_Id>PID_PC _1</Instance_Id>1597 <Instance_Id>PID_PC</Instance_Id> 1582 1598 <Model_Name>PID</Model_Name> 1583 1599 <T_Connection>0</T_Connection> … … 1673 1689 <Desc>MaxInput</Desc> 1674 1690 <Index>0</Index> 1675 <Values> 2.36</Values>1691 <Values>6</Values> 1676 1692 <Status>4</Status> 1677 1693 </Parameters> … … 1691 1707 <Desc>Input</Desc> 1692 1708 <Index>0</Index> 1693 <Values> 0.6</Values>1709 <Values>3.22753</Values> 1694 1710 <Status>0</Status> 1695 1711 </Variables> … … 1697 1713 <Desc>Output</Desc> 1698 1714 <Index>0</Index> 1699 <Values> 0.184492</Values>1715 <Values>1</Values> 1700 1716 <Status>0</Status> 1701 1717 </Variables> … … 1719 1735 <Block_Properties> 1720 1736 <Model_File_Path>controllers/PIDs</Model_File_Path> 1721 <Instance_Id>PID_LC _1</Instance_Id>1737 <Instance_Id>PID_LC</Instance_Id> 1722 1738 <Model_Name>PID</Model_Name> 1723 1739 <T_Connection>0</T_Connection> … … 1831 1847 <Desc>Input</Desc> 1832 1848 <Index>0</Index> 1833 <Values>0. 5</Values>1849 <Values>0.736935</Values> 1834 1850 <Status>0</Status> 1835 1851 </Variables> … … 1837 1853 <Desc>Output</Desc> 1838 1854 <Index>0</Index> 1839 <Values>0. 315508</Values>1855 <Values>0.522804</Values> 1840 1856 <Status>0</Status> 1841 1857 </Variables> … … 1843 1859 <Desc>SetPoint</Desc> 1844 1860 <Index>0</Index> 1845 <Values>0. 5</Values>1861 <Values>0.7</Values> 1846 1862 <Status>1</Status> 1847 1863 </Variables> … … 1858 1874 <Block_Target>F101</Block_Target> 1859 1875 <Port_Target>InletQ</Port_Target> 1860 </Line>1861 <Line>1862 <Line_Name>1</Line_Name>1863 <X1>310.06</X1>1864 <Y1>272</Y1>1865 <X2>426</X2>1866 <Y2>405.67</Y2>1867 <Block_Source>F101</Block_Source>1868 <Port_Source>OutletL</Port_Source>1869 <Block_Target>LCV</Block_Target>1870 <Port_Target>Inlet</Port_Target>1871 </Line>1872 <Line>1873 <Line_Name>3</Line_Name>1874 <X1>311.278</X1>1875 <Y1>47</Y1>1876 <X2>449</X2>1877 <Y2>56.8315</Y2>1878 <Block_Source>F101</Block_Source>1879 <Port_Source>OutletV</Port_Source>1880 <Block_Target>PCV</Block_Target>1881 <Port_Target>Inlet</Port_Target>1882 1876 </Line> 1883 1877 <Line> … … 1980 1974 <Port_Target>FlowFraction</Port_Target> 1981 1975 </Line> 1976 <Line> 1977 <Line_Name>1</Line_Name> 1978 <X1>310.06</X1> 1979 <Y1>272</Y1> 1980 <X2>429</X2> 1981 <Y2>405</Y2> 1982 <Block_Source>F101</Block_Source> 1983 <Port_Source>OutletLiquid</Port_Source> 1984 <Block_Target>LCV</Block_Target> 1985 <Port_Target>Inlet</Port_Target> 1986 </Line> 1987 <Line> 1988 <Line_Name>3</Line_Name> 1989 <X1>311.278</X1> 1990 <Y1>47</Y1> 1991 <X2>448</X2> 1992 <Y2>55</Y2> 1993 <Block_Source>F101</Block_Source> 1994 <Port_Source>OutletVapour</Port_Source> 1995 <Block_Target>PCV</Block_Target> 1996 <Port_Target>Inlet</Port_Target> 1997 </Line> 1982 1998 </Diagram>
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