Changeset 809
- Timestamp:
- Aug 4, 2009, 12:12:36 PM (14 years ago)
- Location:
- branches/gui
- Files:
-
- 1 added
- 3 edited
-
eml/controllers/heat_flow.mso (modified) (1 diff)
-
eml/stage_separators/column.mso (modified) (3 diffs)
-
sample/stage_separators/Column_ThermSubcoling.pfd (modified) (119 diffs)
-
sample/stage_separators/Column_ThermSubcoling.rlt (added)
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/controllers/heat_flow.mso
r743 r809 21 21 22 22 Model heat_flow 23 ATTRIBUTES24 Pallete = true;25 Icon = "icon/heat_flow";26 Brief = "Model of a very simple valve for setting the energy flow with a controller.";27 23 24 ATTRIBUTES 25 Pallete = true; 26 Icon = "icon/heat_flow"; 27 Brief = "Model of a very simple valve for setting the energy flow with a controller."; 28 Info = 29 "== ASSUMPTIONS == 30 * nothing happens in this valve 31 32 == SET == 33 * MinHeatFlow: the Minimum Heat Flow Allowable in the valve; 34 * MaxHeatFlow: the Maximum Heat Flow Allowable in the valve; 35 36 == SPECIFY == 37 * the HeatFlowFraction (the model requires an inlet signal, also you can use a controller for setting the HeatFlowFraction) 38 "; 28 39 29 40 PARAMETERS 30 41 31 MinHeatFlow as power(Brief="Minimum of Heat Flow",Default=-1000);32 MaxHeatFlow as power 42 MinHeatFlow as power (Brief="Minimum of Heat Flow",Default=-1000); 43 MaxHeatFlow as power (Brief="Maximum of Heat Flow",Default=1000); 33 44 34 45 VARIABLES 35 46 36 out HeatFlow as power (Brief="Heat Flow", PosX=0, PosY=0.60);37 in HeatFlowFraction as fraction (Brief="Flow Signal", PosX=0.50, PosY=0);47 out HeatFlow as power (Brief="Heat Flow", PosX=0, PosY=0.60,Protected=true); 48 in HeatFlowFraction as fraction (Brief="Flow Signal", PosX=0.50, PosY=0,Protected=true); 38 49 39 50 EQUATIONS 40 51 "Heat Flow" 41 52 HeatFlow = MinHeatFlow + HeatFlowFraction*(MaxHeatFlow-MinHeatFlow); -
branches/gui/eml/stage_separators/column.mso
r808 r809 817 817 CONTROL as ControlSection (Brief = "Control"); 818 818 819 out TCI as control_signal (Brief="Temperature Indicator", Protected = true, PosX=1, PosY=0. 63);819 out TCI as control_signal (Brief="Temperature Indicator", Protected = true, PosX=1, PosY=0.55); 820 820 out PCI as control_signal (Brief="Pressure Indicator", Protected = true, PosX=0, PosY=0.23); 821 821 … … 1169 1169 1170 1170 out TI_reb as control_signal (Brief="Temperature Indicator of Reboiler ",Protected = true, PosX=1, PosY=0.92); 1171 out PI_reb as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=1, PosY=0.8 5);1171 out PI_reb as control_signal (Brief="Pressure Indicator of Reboiler", Protected = true, PosX=1, PosY=0.875); 1172 1172 1173 1173 out TI_cond as control_signal (Brief="Temperature Indicator of Condenser ", Protected = true, PosX=0.52, PosY=0); 1174 1174 out PI_cond as control_signal (Brief="Pressure Indicator of Condenser", Protected = true, PosX=0.42, PosY=0); 1175 1175 1176 out TI_drum as control_signal (Brief="Temperature Indicator of Reflux Drum ", Protected = true, PosX=1, PosY=0. 18);1177 out PI_drum as control_signal (Brief="Pressure Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.1 7);1176 out TI_drum as control_signal (Brief="Temperature Indicator of Reflux Drum ", Protected = true, PosX=1, PosY=0.20); 1177 out PI_drum as control_signal (Brief="Pressure Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.155); 1178 1178 out LI_drum as control_signal (Brief="Level Indicator of Reflux Drum", Protected = true, PosX=1, PosY=0.24); 1179 1179 1180 out LI_sump as control_signal (Brief="Level Indicator of Column Sump", Protected = true, PosX=1, PosY=0.7 0);1181 out TI_sump as control_signal (Brief="Temperature Indicator of Column Sump ",Protected = true, PosX=1, PosY=0.7 5);1182 1183 out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.32);1184 out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Bottom Splitter", PosX=0.05, PosY=1);1185 1186 in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true);1187 in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true);1180 out LI_sump as control_signal (Brief="Level Indicator of Column Sump", Protected = true, PosX=1, PosY=0.765); 1181 out TI_sump as control_signal (Brief="Temperature Indicator of Column Sump ",Protected = true, PosX=1, PosY=0.71); 1182 1183 out LiquidDistillate as liquid_stream (Brief="Liquid outlet stream From Top Splitter", PosX=1, PosY=0.33); 1184 out BottomProduct as liquid_stream (Brief="Liquid outlet stream From Bottom Splitter", PosX=0.06, PosY=1); 1185 1186 in ConnectorSplitterBottom as stream (Brief="Connector for Liquid outlet stream From Reboiler", Hidden=true); 1187 in ConnectorSplitterTop as stream (Brief="Connector for Liquid outlet stream From Top Splitter", Hidden=true); 1188 1188 1189 1189 ConnectorHeatReboiler as power (Brief="Connector for Heat supplied to Reboiler", Hidden=true); 1190 1190 ConnectorHeatCondenser as power (Brief="Connector for Heat supplied to Condenser", Hidden=true); 1191 1191 ConnectorHeatRefluxDrum as power (Brief="Connector for Heat supplied to Reflux Drum", Hidden=true); 1192 1192 1193 1193 EQUATIONS 1194 1195 TI_reb = REBOILER.TI ; 1196 PI_reb = REBOILER.PI; 1197 1198 TI_cond = CONDENSER.TI; 1199 PI_cond = CONDENSER.PI; 1200 1201 TI_drum = REFLUX_DRUM.TI; 1202 PI_drum = REFLUX_DRUM.PI; 1203 LI_drum = REFLUX_DRUM.LI; 1204 1205 TI_sump = SUMP.TI; 1206 LI_sump = SUMP.LI; 1207 1208 for i in 1:NumberOfTrays do 1209 1210 if i equal FeedTrayLocation(1) then 1211 1212 "FeedTrayTop Inlet Flow" 1213 FeedTray.F= TRAYS(i).Inlet.F; 1214 1215 "FeedTrayTop Inlet Temperature" 1216 FeedTray.T = TRAYS(i).Inlet.T; 1217 1218 "FeedTrayTop Inlet Pressure" 1219 FeedTray.P = TRAYS(i).Inlet.P; 1220 1221 "FeedTrayTop Inlet Composition" 1222 FeedTray.z = TRAYS(i).Inlet.z; 1223 1224 "FeedTrayTop Inlet Vapour Fraction" 1225 FeedTray.v = TRAYS(i).Inlet.v; 1226 1227 "FeedTrayTop Inlet Enthalpy" 1228 FeedTray.h = TRAYS(i).Inlet.h; 1229 1230 else 1231 1232 "Inlet Tray - Flow Sealed" 1233 0*'mol/h'= TRAYS(i).Inlet.F; 1234 1235 "Inlet Tray - Temperature" 1236 FeedTray.T = TRAYS(i).Inlet.T; 1237 1238 "Inlet Tray - Pressure" 1239 FeedTray.P = TRAYS(i).Inlet.P; 1240 1241 "Inlet Tray - Composition" 1242 FeedTray.z = TRAYS(i).Inlet.z; 1243 1244 "Inlet Tray - Vapour Fraction" 1245 FeedTray.v = TRAYS(i).Inlet.v; 1246 1247 "Inlet Tray - Enthalpy" 1248 FeedTray.h = TRAYS(i).Inlet.h; 1249 1250 end 1251 1252 end 1194 1253 1195 1254 # Heat Connector Equations … … 1209 1268 ConnectorSplitterBottom.F = BottomProduct.F; 1210 1269 ConnectorSplitterBottom.z = BottomProduct.z; 1211 1270 1212 1271 CONNECTIONS 1213 1272 #vapor -
branches/gui/sample/stage_separators/Column_ThermSubcoling.pfd
r808 r809 11 11 <Dynamic>1</Dynamic> 12 12 <Time_Start>0</Time_Start> 13 <Time_Step>0. 01</Time_Step>14 <Time_End> 0.10</Time_End>13 <Time_Step>0.1</Time_Step> 14 <Time_End>1</Time_End> 15 15 <Time_Unit>h</Time_Unit> 16 16 <Sparse_Algebra>1</Sparse_Algebra> 17 17 <Integration_Index>0</Integration_Index> 18 18 <Integration_Text>original</Integration_Text> 19 <Initial_File>/home/bicca/Documentos/repositorio/alsoc/biblioteca/branches/gui/sample/stage_separators/Column_ThermSubcoling.rlt</Initial_File> 19 20 <NLASolver_File_Index>0</NLASolver_File_Index> 20 21 <NLASolver_File_Text>sundials</NLASolver_File_Text> … … 31 32 <View> 32 33 <Zoom_Level>1</Zoom_Level> 33 <Show_Grid> 0</Show_Grid>34 <Snap_to_Grid> 0</Snap_to_Grid>35 <Width> 1250</Width>34 <Show_Grid>1</Show_Grid> 35 <Snap_to_Grid>1</Snap_to_Grid> 36 <Width>919</Width> 36 37 <Height>509</Height> 37 <X>- 45</X>38 <Y>- 6</Y>38 <X>-158</X> 39 <Y>-300</Y> 39 40 </View> 40 41 <View> 41 42 <Zoom_Level>1</Zoom_Level> 42 <Show_Grid> 0</Show_Grid>43 <Snap_to_Grid> 0</Snap_to_Grid>44 <Width> 1250</Width>43 <Show_Grid>1</Show_Grid> 44 <Snap_to_Grid>1</Snap_to_Grid> 45 <Width>919</Width> 45 46 <Height>0</Height> 46 47 <X>0</X> … … 204 205 <Id_String>T1</Id_String> 205 206 <Image_File_Name>/home/bicca/Documentos/repositorio/alsoc/biblioteca/branches/gui/eml/stage_separators/icon/DistillationThermosyphonSubcooling.png</Image_File_Name> 206 <X>41 9</X>207 <X>418</X> 207 208 <Y>43</Y> 208 209 <Z>0</Z> … … 232 233 <Model_Name>InitializeSection</Model_Name> 233 234 <T_Connection>0</T_Connection> 235 <Parameters> 236 <Desc>NComp</Desc> 237 <Index>0</Index> 238 <Values>2</Values> 239 <Status>0</Status> 240 </Parameters> 241 <Parameters> 242 <Desc>TopTemperature</Desc> 243 <Index>0</Index> 244 <Values>300</Values> 245 <Status>0</Status> 246 <Unit>K</Unit> 247 </Parameters> 248 <Parameters> 249 <Desc>BottomTemperature</Desc> 250 <Index>0</Index> 251 <Values>330</Values> 252 <Status>0</Status> 253 <Unit>K</Unit> 254 </Parameters> 255 <Parameters> 256 <Desc>LevelFraction</Desc> 257 <Index>0</Index> 258 <Values>0.5</Values> 259 <Status>0</Status> 260 </Parameters> 261 <Parameters> 262 <Desc>TopComposition</Desc> 263 <Index>0</Index> 264 <Values>0.3</Values> 265 <Status>0</Status> 266 <Index>1</Index> 267 <Values>0.3</Values> 268 <Status>0</Status> 269 </Parameters> 270 <Parameters> 271 <Desc>BottomComposition</Desc> 272 <Index>0</Index> 273 <Values>0.3</Values> 274 <Status>0</Status> 275 <Index>1</Index> 276 <Values>0.3</Values> 277 <Status>0</Status> 278 </Parameters> 234 279 </Block_Properties> 235 280 </Base_Models> … … 248 293 <Model_Name>ControlSection</Model_Name> 249 294 <T_Connection>0</T_Connection> 295 <Parameters> 296 <Desc>NComp</Desc> 297 <Index>0</Index> 298 <Values>2</Values> 299 <Status>0</Status> 300 </Parameters> 250 301 <Parameters> 251 302 <Desc>Tindicator_TrayNumber</Desc> … … 294 345 <Model_Name>stream</Model_Name> 295 346 <T_Connection>1</T_Connection> 347 <Parameters> 348 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<Status>0</Status> 1294 <Unit>kmol/h</Unit> 1295 </Variables> 1296 <Variables> 1297 <Desc>T</Desc> 1298 <Index>0</Index> 1299 <Values>329.627</Values> 1300 <Status>0</Status> 1301 <Unit>K</Unit> 1302 </Variables> 1303 <Variables> 1304 <Desc>P</Desc> 1305 <Index>0</Index> 1306 <Values>20.9881</Values> 1307 <Status>0</Status> 1308 <Unit>atm</Unit> 1309 </Variables> 1310 <Variables> 1311 <Desc>h</Desc> 1312 <Index>0</Index> 1313 <Values>-11861.7</Values> 1314 <Status>0</Status> 1315 <Unit>kJ/kmol</Unit> 1316 </Variables> 1317 <Variables> 1318 <Desc>v</Desc> 1319 <Index>0</Index> 1320 <Values>0</Values> 1321 <Status>0</Status> 1322 </Variables> 1323 <Variables> 1324 <Desc>z</Desc> 1325 <Index>0</Index> 1326 <Values>0.403218</Values> 1327 <Status>0</Status> 1328 <Index>1</Index> 1329 <Values>0.596782</Values> 1330 <Status>0</Status> 1331 </Variables> 578 1332 </Block_Properties> 579 1333 </Base_Models> … … 606 1360 <Model_Name>stream</Model_Name> 607 1361 <T_Connection>2</T_Connection> 1362 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<Index>1</Index> 1408 <Values>0.570775</Values> 1409 <Status>0</Status> 1410 </Variables> 608 1411 </Block_Properties> 609 1412 </Base_Models> … … 624 1427 <Status>0</Status> 625 1428 </Parameters> 1429 <Parameters> 1430 <Desc>NComp</Desc> 1431 <Index>0</Index> 1432 <Values>2</Values> 1433 <Status>0</Status> 1434 </Parameters> 1435 <Variables> 1436 <Desc>M</Desc> 1437 <Index>0</Index> 1438 <Values>0.122465</Values> 1439 <Status>0</Status> 1440 <Unit>kmol</Unit> 1441 <Index>1</Index> 1442 <Values>0.171948</Values> 1443 <Status>0</Status> 1444 <Unit>kmol</Unit> 1445 </Variables> 1446 <Variables> 1447 <Desc>ML</Desc> 1448 <Index>0</Index> 1449 <Values>0.150123</Values> 1450 <Status>0</Status> 1451 <Unit>kmol</Unit> 1452 </Variables> 1453 <Variables> 1454 <Desc>MV</Desc> 1455 <Index>0</Index> 1456 <Values>0.14429</Values> 1457 <Status>0</Status> 1458 <Unit>kmol</Unit> 1459 </Variables> 1460 <Variables> 1461 <Desc>E</Desc> 1462 <Index>0</Index> 1463 <Values>-2144.98</Values> 1464 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<Desc>rhoV</Desc> 1508 <Index>0</Index> 1509 <Values>49.2572</Values> 1510 <Status>0</Status> 1511 <Unit>kg/m^3</Unit> 1512 </Variables> 628 1513 </Block_Properties> 629 1514 </Base_Models> … … 633 1518 <Block_Properties> 634 1519 <Model_File_Path>stage_separators/column</Model_File_Path> 635 <Instance_Id>TRAYS( 4)</Instance_Id>1520 <Instance_Id>TRAYS(1.</Instance_Id> 636 1521 <Model_Name>TRAYS</Model_Name> 637 1522 <T_Connection>0</T_Connection> … … 639 1524 <Block_Properties> 640 1525 <Model_File_Path>stage_separators/tray</Model_File_Path> 641 <Instance_Id>TRAYS( 4)</Instance_Id>1526 <Instance_Id>TRAYS(1.</Instance_Id> 642 1527 <Model_Name>tray</Model_Name> 643 1528 <T_Connection>0</T_Connection> … … 645 1530 <Block_Properties> 646 1531 <Model_File_Path>stage_separators/tray</Model_File_Path> 647 <Instance_Id>TRAYS( 4)</Instance_Id>1532 <Instance_Id>TRAYS(1.</Instance_Id> 648 1533 <Model_Name>trayBasic</Model_Name> 649 1534 <T_Connection>0</T_Connection> … … 660 1545 <Model_Name>stream</Model_Name> 661 1546 <T_Connection>1</T_Connection> 1547 <Parameters> 1548 <Desc>NComp</Desc> 1549 <Index>0</Index> 1550 <Values>2</Values> 1551 <Status>0</Status> 1552 </Parameters> 1553 <Variables> 1554 <Desc>F</Desc> 1555 <Index>0</Index> 1556 <Values>31.6277</Values> 1557 <Status>0</Status> 1558 <Unit>kmol/h</Unit> 1559 </Variables> 1560 <Variables> 1561 <Desc>T</Desc> 1562 <Index>0</Index> 1563 <Values>329.627</Values> 1564 <Status>0</Status> 1565 <Unit>K</Unit> 1566 </Variables> 1567 <Variables> 1568 <Desc>P</Desc> 1569 <Index>0</Index> 1570 <Values>20.9881</Values> 1571 <Status>0</Status> 1572 <Unit>atm</Unit> 1573 </Variables> 1574 <Variables> 1575 <Desc>h</Desc> 1576 <Index>0</Index> 1577 <Values>-11861.7</Values> 1578 <Status>0</Status> 1579 <Unit>kJ/kmol</Unit> 1580 </Variables> 1581 <Variables> 1582 <Desc>v</Desc> 1583 <Index>0</Index> 1584 <Values>0</Values> 1585 <Status>0</Status> 1586 </Variables> 1587 <Variables> 1588 <Desc>z</Desc> 1589 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<Status>0</Status> 1644 <Unit>kJ/kmol</Unit> 1645 </Variables> 1646 <Variables> 1647 <Desc>v</Desc> 1648 <Index>0</Index> 1649 <Values>1</Values> 1650 <Status>0</Status> 1651 </Variables> 1652 <Variables> 1653 <Desc>z</Desc> 1654 <Index>0</Index> 1655 <Values>0.428247</Values> 1656 <Status>0</Status> 1657 <Index>1</Index> 1658 <Values>0.571753</Values> 1659 <Status>0</Status> 1660 </Variables> 678 1661 </Block_Properties> 679 1662 </Base_Models> … … 698 1681 <Model_Name>stream</Model_Name> 699 1682 <T_Connection>2</T_Connection> 1683 <Parameters> 1684 <Desc>NComp</Desc> 1685 <Index>0</Index> 1686 <Values>2</Values> 1687 <Status>0</Status> 1688 </Parameters> 1689 <Variables> 1690 <Desc>F</Desc> 1691 <Index>0</Index> 1692 <Values>31.5415</Values> 1693 <Status>0</Status> 1694 <Unit>kmol/h</Unit> 1695 </Variables> 1696 <Variables> 1697 <Desc>T</Desc> 1698 <Index>0</Index> 1699 <Values>329.637</Values> 1700 <Status>0</Status> 1701 <Unit>K</Unit> 1702 </Variables> 1703 <Variables> 1704 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<Desc>NComp</Desc> 1831 <Index>0</Index> 1832 <Values>2</Values> 1833 <Status>0</Status> 1834 </Parameters> 1835 <Variables> 1836 <Desc>M</Desc> 1837 <Index>0</Index> 1838 <Values>0.122204</Values> 1839 <Status>0</Status> 1840 <Unit>kmol</Unit> 1841 <Index>1</Index> 1842 <Values>0.17213</Values> 1843 <Status>0</Status> 1844 <Unit>kmol</Unit> 1845 </Variables> 1846 <Variables> 1847 <Desc>ML</Desc> 1848 <Index>0</Index> 1849 <Values>0.150019</Values> 1850 <Status>0</Status> 1851 <Unit>kmol</Unit> 1852 </Variables> 1853 <Variables> 1854 <Desc>MV</Desc> 1855 <Index>0</Index> 1856 <Values>0.144314</Values> 1857 <Status>0</Status> 1858 <Unit>kmol</Unit> 1859 </Variables> 1860 <Variables> 1861 <Desc>E</Desc> 1862 <Index>0</Index> 1863 <Values>-2143.5</Values> 1864 <Status>0</Status> 1865 <Unit>kJ</Unit> 1866 </Variables> 1867 <Variables> 1868 <Desc>vL</Desc> 1869 <Index>0</Index> 1870 <Values>9.94623e-05</Values> 1871 <Status>0</Status> 1872 <Unit>m^3/mol</Unit> 1873 </Variables> 1874 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<Model_File_Path>stage_separators/column</Model_File_Path> 757 <Instance_Id>TRAYS( 5)</Instance_Id>1920 <Instance_Id>TRAYS(1.</Instance_Id> 758 1921 <Model_Name>TRAYS</Model_Name> 759 1922 <T_Connection>0</T_Connection> … … 761 1924 <Block_Properties> 762 1925 <Model_File_Path>stage_separators/tray</Model_File_Path> 763 <Instance_Id>TRAYS( 5)</Instance_Id>1926 <Instance_Id>TRAYS(1.</Instance_Id> 764 1927 <Model_Name>tray</Model_Name> 765 1928 <T_Connection>0</T_Connection> … … 767 1930 <Block_Properties> 768 1931 <Model_File_Path>stage_separators/tray</Model_File_Path> 769 <Instance_Id>TRAYS( 5)</Instance_Id>1932 <Instance_Id>TRAYS(1.</Instance_Id> 770 1933 <Model_Name>trayBasic</Model_Name> 771 1934 <T_Connection>0</T_Connection> … … 782 1945 <Model_Name>stream</Model_Name> 783 1946 <T_Connection>1</T_Connection> 1947 <Parameters> 1948 <Desc>NComp</Desc> 1949 <Index>0</Index> 1950 <Values>2</Values> 1951 <Status>0</Status> 1952 </Parameters> 1953 <Variables> 1954 <Desc>F</Desc> 1955 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