Changeset 796 for branches/gui
- Timestamp:
- Jul 18, 2009, 6:08:44 PM (14 years ago)
- Location:
- branches/gui
- Files:
-
- 9 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/stage_separators/flash.mso
r714 r796 24 24 Pallete = true; 25 25 Icon = "icon/Flash"; 26 Brief = "Model of a dynamic flash.";26 Brief = "Model of a Dynamic Flash Vessel."; 27 27 Info = 28 "== Assumptions == 29 * Both phases are perfectly mixed. 30 31 == Specify == 32 * The feed stream; 33 * The outlet flows: OutletVapour.F and OutletLiquid.F. 34 35 == Initial Conditions == 36 * The flash initial temperature (Temperature_Initial); 37 * The flash initial level (Levelpercent_Initial); 38 *The Outlet Liquid Composition (Composition_Initial). 28 "== ASSUMPTIONS == 29 * perfect mixing of both phases; 30 * thermodynamics equilibrium. 31 32 == SET == 33 *Orientation: vessel position - vertical or horizontal; 34 *Heads (bottom and top heads are identical) 35 **elliptical: 2:1 elliptical heads (25% of vessel diameter); 36 **hemispherical: hemispherical heads (50% of vessel diameter); 37 **flat: flat heads (0% of vessel diameter); 38 *Diameter: Vessel diameter; 39 *Lenght: Side length of the cylinder shell; 40 41 == SPECIFY == 42 * the Inlet stream; 43 * the outlet flows: OutletVapour.F and OutletLiquid.F; 44 * the InletQ (the model requires an energy stream, also you can use a controller for setting the heat duty using the heat_flow model). 45 46 == OPTIONAL == 47 * the Flash model has three control ports 48 ** TI OutletLiquid Temperature Indicator; 49 ** PI OutletLiquid Pressure Indicator; 50 ** LI Level Indicator; 51 52 == INITIAL CONDITIONS == 53 * Initial_Temperature : the Flash temperature (OutletLiquid.T); 54 * Initial_Level : the Flash liquid level (Level); 55 * Initial_Composition : (NoComps) OutletLiquid compositions. 39 56 "; 40 57 41 58 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 59 outer PP as Plugin (Brief = "External Physical Properties", Type="PP"); 60 outer NComp as Integer (Brief = "Number of components", Lower = 1); 61 62 Mw(NComp) as molweight (Brief="Mol Weight", Hidden=true); 63 pi as positive (Brief="Pi value", Default=3.141593,Hidden=true, Symbol="\pi"); 64 65 Orientation as Switcher (Valid=["vertical","horizontal"],Default="vertical"); 66 Heads as Switcher (Valid=["elliptical","hemispherical","flat"],Default="flat"); 67 Diameter as length (Brief="Vessel diameter", Symbol="D_{i}"); 68 Lenght as length (Brief="Side length of the cylinder shell", Symbol="L_{vessel}"); 69 70 Vhead_elliptical as volume (Brief="Elliptical Head Total Volume",Hidden=true, Symbol="V_{head}^{elliptical}"); 71 Vhead_hemispherical as volume (Brief="Hemispherical Head Total Volume",Hidden=true, Symbol="V_{head}^{hemispherical}"); 72 Vcylinder as volume (Brief="Cylinder Total Volume",Hidden=true, Symbol="V_{cylinder}"); 73 radius as length (Brief="Vessel radius",Hidden=true, Symbol="R_{cylinder}"); 74 75 Levelpercent_Initial as positive (Brief="Initial liquid height in Percent", Default = 0.70); 76 Temperature_Initial as temperature (Brief="Initial Liquid Temperature", Default = 330); 77 Composition_Initial(NComp) as fraction (Brief="Initial Composition", Default = 0.10); 78 55 79 SET 56 80 57 81 Mw=PP.MolecularWeight(); 58 82 83 Vhead_elliptical = (pi*Diameter^3)/12; 84 Vhead_hemispherical = (pi*Diameter^3)/6; 85 Vcylinder = 0.25*(pi*Diameter^2)*Lenght; 86 radius = 0.5*Diameter; 87 59 88 VARIABLES 60 89 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}"); 90 in Inlet as stream (Brief="Feed Stream", PosX=0, PosY=0.48, Symbol="_{in}"); 91 out OutletLiquid as liquid_stream (Brief="Liquid outlet stream", PosX=0.43, PosY=1, Symbol="_{out}^{Liquid}"); 92 out OutletVapour as vapour_stream (Brief="Vapour outlet stream", PosX=0.43, PosY=0, Symbol="_{out}^{Vapour}"); 93 in InletQ as power (Brief="Heat Duty", PosX=1, PosY=0.81, Protected =true,Symbol="Q_{in}"); 94 95 Vtotal as volume (Brief="Vessel total volume",Protected=true, Symbol="V_{total}"); 96 Vfilled as volume (Brief="Vessel volume content",Protected=true, Symbol="V_{filled}"); 65 97 66 98 TotalHoldup(NComp) as mol (Brief="Molar Holdup in the Vessel", Protected=true); 67 LiquidHoldup 68 VapourHoldup 69 70 E as energy 99 LiquidHoldup as mol (Brief="Molar liquid holdup", Protected=true); 100 VapourHoldup as mol (Brief="Molar vapour holdup", Protected=true); 101 102 E as energy (Brief="Total Energy Holdup in the Vessel", Protected=true); 71 103 vL as volume_mol (Brief="Liquid Molar Volume", Protected=true); 72 104 vV as volume_mol (Brief="Vapour Molar volume", Protected=true); 73 Level as length 74 Across as area (Brief="Flash Cross section area", Protected=true);75 vfrac as positive 76 Pratio as positive 105 Level as length (Brief="liquid height", Protected=true); 106 Across as area (Brief="Vessel cylinder shell Cross section area", Hidden=true, Symbol="A_{cross}"); 107 vfrac as positive (Brief="Vapourization fraction", Symbol="\phi", Protected=true); 108 Pratio as positive (Brief = "Pressure Ratio", Symbol ="P_{ratio}", Protected=true); 77 109 Pdrop as press_delta (Brief = "Pressure Drop", DisplayUnit = 'kPa', Symbol ="\Delta P", Protected=true); 78 110 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);111 out TI as control_signal (Brief="Temperature Indicator", PosX=1, PosY=0.39, Protected=true); 112 out PI as control_signal (Brief="Pressure Indicator", PosX=1, PosY=0.21, Protected=true); 113 out LI as control_signal (Brief="Level Indicator", PosX=1, PosY=0.59, Protected=true); 82 114 83 115 INITIAL 84 116 85 # Initial level Percent 117 "Initial level Percent" 86 118 LI = Levelpercent_Initial; 87 119 88 # Initial Outlet Liquid Temperature 120 "Initial Outlet Liquid Temperature" 89 121 OutletLiquid.T = Temperature_Initial; 90 122 91 # Initial Outlet Liquid Composition Normalized 123 "Initial Outlet Liquid Composition Normalized" 92 124 OutletLiquid.z(1:NComp - 1) = Composition_Initial(1:NComp - 1)/sum(Composition_Initial); 93 125 94 126 EQUATIONS 127 128 switch Orientation 129 130 case "vertical": 131 132 "Vessel Cross Section Area" 133 Across = 0.25*(pi*Diameter^2); 134 135 switch Heads 136 137 case "elliptical": 138 139 "Vessel Total Volume" 140 Vtotal = Vhead_elliptical + Vcylinder; 141 142 if Level < 0.25*Diameter then 143 144 "Vessel Filled Volume" 145 Vfilled = 0.25*pi*(((Diameter*Level)/(0.25*Diameter))^2)*(0.25*Diameter-Level/3); 146 147 else 148 149 "Vessel Filled Volume" 150 Vfilled = 0.25*pi*(Diameter^2)*(Level - 0.25*Diameter/3); 151 152 end 153 154 case "hemispherical": 155 156 "Vessel Total Volume" 157 Vtotal = Vhead_hemispherical + Vcylinder; 158 159 if Level < 0.5*Diameter then 160 161 "Vessel Filled Volume" 162 Vfilled = 0.25*pi*(Level^2)*(2*Diameter-4*Level/3); 163 164 else 165 166 "Vessel Filled Volume" 167 Vfilled = 0.25*pi*((2/3)*((0.5*Diameter)^3) - (0.25*(Diameter)^3) + Level*Diameter^2); 168 169 end 170 171 case "flat": 172 173 "Vessel Total Volume" 174 Vtotal = Vcylinder; 175 176 "Vessel Filled Volume" 177 Vfilled = Across*Level; 178 179 end 180 181 case "horizontal": 182 183 "Vessel Cross Section Area" 184 Across = (radius^2)*acos((radius-Level)/radius)-(radius-Level)*sqrt((2*radius*Level-Level^2)); 185 186 switch Heads 187 188 case "elliptical": 189 190 "Vessel Total Volume" 191 Vtotal = Vhead_elliptical + Vcylinder; 192 193 "Vessel Filled Volume" 194 Vfilled = 0.5236*Level^2*(1.5*Diameter-Level) + Across*Lenght; 195 196 case "hemispherical": 197 198 "Vessel Total Volume" 199 Vtotal = Vhead_hemispherical + Vcylinder; 200 201 "Vessel Filled Volume" 202 Vfilled = 1.0472*Level^2*(1.5*Diameter-Level) + Across*Lenght; 203 204 case "flat": 205 206 "Vessel Total Volume" 207 Vtotal = Vcylinder; 208 209 "Vessel Filled Volume" 210 Vfilled = Across*Lenght; 211 212 end 213 214 end 95 215 96 216 "Component Molar Balance" … … 104 224 105 225 "Energy Holdup" 106 E = LiquidHoldup*OutletLiquid.h + VapourHoldup*OutletVapour.h - OutletLiquid.P*V esselVolume;226 E = LiquidHoldup*OutletLiquid.h + VapourHoldup*OutletVapour.h - OutletLiquid.P*Vtotal; 107 227 108 228 "Mol fraction normalisation" … … 138 258 139 259 "Geometry Constraint" 140 V esselVolume= LiquidHoldup * vL + VapourHoldup * vV;141 142 "Temperature indicator in Celsius Degree"143 TI * 'K' = OutletLiquid.T - 273.15*'K';260 Vtotal = LiquidHoldup * vL + VapourHoldup * vV; 261 262 "Temperature indicator" 263 TI * 'K' = OutletLiquid.T; 144 264 145 265 "Pressure indicator" … … 147 267 148 268 "Level indicator" 149 LI*VesselVolume= Level*Across; 150 151 switch Orientation 152 case "vertical": 153 "Cross Section Area" 154 Across = 0.5 * asin(1) * Diameter^2; 155 156 "Liquid Level" 157 LiquidHoldup * vL = Across * Level; 158 159 case "horizontal": 160 "Cylindrical Side Area" 161 Across = 0.25*Diameter^2 * (asin(1) - asin((Diameter - 2*Level)/Diameter)) + 162 (Level - 0.5*Diameter)*sqrt(Level*(Diameter - Level)); 163 164 "Liquid Level" 165 0.5 * asin(1) * Diameter^2 * LiquidHoldup* vL = Across * VesselVolume; 166 end 269 LI*Vtotal= Vfilled; 270 271 "Liquid Level" 272 LiquidHoldup * vL = Vfilled; 167 273 168 274 end -
branches/gui/eml/stage_separators/icon/Flash.svg
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branches/gui/sample/stage_separators/Sample_flash_PID.mso
r749 r796 26 26 27 27 SPECIFY 28 HeatToFlash.OutletQ = 102 6.32* 'kW';28 HeatToFlash.OutletQ = 1027 * 'kW'; 29 29 30 30 INITIAL … … 100 100 PID_LC.tauSet = 1 * 's'; 101 101 PID_LC.MinInput = 0; 102 PID_LC.MaxInput = 2;102 PID_LC.MaxInput = 1; 103 103 PID_LC.MinOutput = 0; 104 104 PID_LC.MaxOutput = 1; … … 141 141 142 142 DEVICES 143 LiquidProduct as simple_sink; 144 145 SET 146 147 SPECIFY 148 149 INITIAL 150 151 GUESS 152 153 DEVICES 143 154 F101_1 as flash; 144 155 145 156 SET 146 F101_1.VesselVolume = 8 * 'm^3';147 157 F101_1.Orientation = "vertical"; 158 F101_1.Heads = "flat"; 148 159 F101_1.Diameter = 3.1 * 'm'; 149 F101_1.Levelpercent_Initial = 0.70; 150 F101_1.Temperature_Initial = 383 * 'K'; 151 F101_1.Composition_Initial(1) = 0.3; 152 F101_1.Composition_Initial(2) = 0.4; 153 F101_1.Composition_Initial(3) = 0.3; 154 155 SPECIFY 156 157 INITIAL 158 159 GUESS 160 161 DEVICES 162 LiquidProduct as simple_sink; 163 164 SET 160 F101_1.Lenght = 6 * 'm'; 161 F101_1.Levelpercent_Initial = 0.80; 162 F101_1.Temperature_Initial = 373 * 'K'; 163 F101_1.Composition_Initial(1) = 0.30; 164 F101_1.Composition_Initial(2) = 0.40; 165 F101_1.Composition_Initial(3) = 0.30; 165 166 166 167 SPECIFY … … 174 175 PID_LC.Output to valve_liquid.FlowFraction; 175 176 PID_PC.Output to valve_Vapour.FlowFraction; 177 valve_liquid.Outlet to LiquidProduct.Inlet; 178 Feed.Outlet to F101_1.Inlet; 176 179 F101_1.OutletVapour to valve_Vapour.Inlet; 180 HeatToFlash.OutletQ to F101_1.InletQ; 177 181 F101_1.OutletLiquid to valve_liquid.Inlet; 178 Feed.Outlet to F101_1.Inlet;179 HeatToFlash.OutletQ to F101_1.InletQ;180 182 F101_1.LI to PID_LC.Input; 181 183 F101_1.PI to PID_PC.Input; 182 valve_liquid.Outlet to LiquidProduct.Inlet;183 184 184 185 OPTIONS 185 186 Dynamic = true; 186 187 TimeStep = 0.2; 187 TimeEnd = 1 ;188 TimeEnd = 12; 188 189 TimeUnit = 'h'; 189 190 Integration = "original"; -
branches/gui/sample/stage_separators/Sample_flash_PID.pfd
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1336 <Desc>T</Desc> 1253 1337 <Index>0</Index> 1254 <Values>2 31.817</Values>1338 <Values>272.072</Values> 1255 1339 <Status>0</Status> 1256 1340 <Unit>K</Unit> … … 1259 1343 <Desc>P</Desc> 1260 1344 <Index>0</Index> 1261 <Values>0.0 00131171</Values>1345 <Values>0.0208251</Values> 1262 1346 <Status>0</Status> 1263 1347 <Unit>atm</Unit> … … 1266 1350 <Desc>h</Desc> 1267 1351 <Index>0</Index> 1268 <Values>- 7420.84</Values>1352 <Values>-2699.45</Values> 1269 1353 <Status>0</Status> 1270 1354 <Unit>kJ/kmol</Unit> … … 1279 1363 <Desc>z</Desc> 1280 1364 <Index>0</Index> 1281 <Values>0. 33122</Values>1365 <Values>0.646174</Values> 1282 1366 <Status>0</Status> 1283 1367 <Index>1</Index> 1284 <Values>0. 360461</Values>1368 <Values>0.289474</Values> 1285 1369 <Status>0</Status> 1286 1370 <Index>2</Index> 1287 <Values>0. 30832</Values>1371 <Values>0.0643512</Values> 1288 1372 <Status>0</Status> 1289 1373 </Variables> … … 1313 1397 </Parameters> 1314 1398 <Parameters> 1315 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<Status>0</Status> 1407 1511 <Unit>m^3/mol</Unit> … … 1410 1514 <Desc>vV</Desc> 1411 1515 <Index>0</Index> 1412 <Values>1 45.016</Values>1516 <Values>1.06688</Values> 1413 1517 <Status>0</Status> 1414 1518 <Unit>m^3/mol</Unit> … … 1417 1521 <Desc>Level</Desc> 1418 1522 <Index>0</Index> 1419 <Values> 0.197717</Values>1523 <Values>2.42265</Values> 1420 1524 <Status>0</Status> 1421 1525 <Unit>m</Unit> 1422 1526 </Variables> 1423 1527 <Variables> 1424 <Desc>Across</Desc>1425 <Index>0</Index>1426 <Values>7.54768</Values>1427 <Status>0</Status>1428 <Unit>m^2</Unit>1429 </Variables>1430 <Variables>1431 1528 <Desc>vfrac</Desc> 1432 1529 <Index>0</Index> 1433 <Values>0. 907012</Values>1530 <Values>0.295889</Values> 1434 1531 <Status>0</Status> 1435 1532 </Variables> … … 1437 1534 <Desc>Pratio</Desc> 1438 1535 <Index>0</Index> 1439 <Values> 2.62341e-05</Values>1536 <Values>0.00416502</Values> 1440 1537 <Status>0</Status> 1441 1538 </Variables> … … 1443 1540 <Desc>Pdrop</Desc> 1444 1541 <Index>0</Index> 1445 <Values>50 6.612</Values>1542 <Values>504.515</Values> 1446 1543 <Status>0</Status> 1447 1544 <Unit>kPa</Unit> … … 1450 1547 <Desc>TI</Desc> 1451 1548 <Index>0</Index> 1452 <Values> -41.333</Values>1549 <Values>272.072</Values> 1453 1550 <Status>0</Status> 1454 1551 </Variables> … … 1456 1553 <Desc>PI</Desc> 1457 1554 <Index>0</Index> 1458 <Values>0.0 00131171</Values>1555 <Values>0.0208251</Values> 1459 1556 <Status>0</Status> 1460 1557 </Variables> … … 1462 1559 <Desc>LI</Desc> 1463 1560 <Index>0</Index> 1464 <Values>0.186538</Values> 1465 <Status>0</Status> 1466 </Variables> 1467 </Block_Properties> 1468 </Block> 1469 <Block> 1470 <Type>simple_sink</Type> 1471 <Id_String>LiquidProduct</Id_String> 1472 <Image_File_Name>/home/bicca/apps/biblioteca/branches/gui/eml/icon/Sink.png</Image_File_Name> 1473 <X>877</X> 1474 <Y>523</Y> 1475 <Z>0</Z> 1476 <Width>68</Width> 1477 <Height>30</Height> 1478 <Block_Properties> 1479 <Model_File_Path>streams</Model_File_Path> 1480 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<X2>880</X2> 1571 <Y2>117.924</Y2> 1559 1572 <Block_Source>valve_Vapour</Block_Source> 1560 1573 <Port_Source>Outlet</Port_Source> … … 1564 1577 <Line> 1565 1578 <Line_Name>6</Line_Name> 1566 <X1> 694.02</X1>1567 <Y1> 416</Y1>1579 <X1>713.74</X1> 1580 <Y1>358</Y1> 1568 1581 <X2>543.769</X2> 1569 1582 <Y2>505</Y2> … … 1575 1588 <Line> 1576 1589 <Line_Name>9</Line_Name> 1577 <X1>9 07.02</X1>1578 <Y1>27 5</Y1>1590 <X1>927.18</X1> 1591 <Y1>274</Y1> 1579 1592 <X2>659</X2> 1580 1593 <Y2>22</Y2> … … 1583 1596 <Block_Target>valve_Vapour</Block_Target> 1584 1597 <Port_Target>FlowFraction</Port_Target> 1585 </Line>1586 <Line>1587 <Line_Name>1</Line_Name>1588 <X1>428.278</X1>1589 <Y1>134</Y1>1590 <X2>621</X2>1591 <Y2>68</Y2>1592 <Block_Source>F101_1</Block_Source>1593 <Port_Source>OutletVapour</Port_Source>1594 <Block_Target>valve_Vapour</Block_Target>1595 <Port_Target>Inlet</Port_Target>1596 </Line>1597 <Line>1598 <Line_Name>2</Line_Name>1599 <X1>427.06</X1>1600 <Y1>359</Y1>1601 <X2>500</X2>1602 <Y2>542</Y2>1603 <Block_Source>F101_1</Block_Source>1604 <Port_Source>OutletLiquid</Port_Source>1605 <Block_Target>valve_liquid</Block_Target>1606 <Port_Target>Inlet</Port_Target>1607 </Line>1608 <Line>1609 <Line_Name>3</Line_Name>1610 <X1>148</X1>1611 <Y1>146.768</Y1>1612 <X2>366</X2>1613 <Y2>254</Y2>1614 <Block_Source>Feed</Block_Source>1615 <Port_Source>Outlet</Port_Source>1616 <Block_Target>F101_1</Block_Target>1617 <Port_Target>Inlet</Port_Target>1618 </Line>1619 <Line>1620 <Line_Name>4</Line_Name>1621 <X1>301.5</X1>1622 <Y1>398.48</Y1>1623 <X2>500</X2>1624 <Y2>310</Y2>1625 <Block_Source>HeatToFlash</Block_Source>1626 <Port_Source>OutletQ</Port_Source>1627 <Block_Target>F101_1</Block_Target>1628 <Port_Target>InletQ</Port_Target>1629 </Line>1630 <Line>1631 <Line_Name>7</Line_Name>1632 <X1>500</X1>1633 <Y1>224</Y1>1634 <X2>636</X2>1635 <Y2>357</Y2>1636 <Block_Source>F101_1</Block_Source>1637 <Port_Source>LI</Port_Source>1638 <Block_Target>PID_LC</Block_Target>1639 <Port_Target>Input</Port_Target>1640 </Line>1641 <Line>1642 <Line_Name>8</Line_Name>1643 <X1>500</X1>1644 <Y1>201.5</Y1>1645 <X2>849</X2>1646 <Y2>213</Y2>1647 <Block_Source>F101_1</Block_Source>1648 <Port_Source>PI</Port_Source>1649 <Block_Target>PID_PC</Block_Target>1650 <Port_Target>Input</Port_Target>1651 1598 </Line> 1652 1599 <Line> … … 1661 1608 <Port_Target>Inlet</Port_Target> 1662 1609 </Line> 1610 <Line> 1611 <Line_Name>1</Line_Name> 1612 <X1>148</X1> 1613 <Y1>146.768</Y1> 1614 <X2>311</X2> 1615 <Y2>287.6</Y2> 1616 <Block_Source>Feed</Block_Source> 1617 <Port_Source>Outlet</Port_Source> 1618 <Block_Target>F101_1</Block_Target> 1619 <Port_Target>Inlet</Port_Target> 1620 </Line> 1621 <Line> 1622 <Line_Name>2</Line_Name> 1623 <X1>352.71</X1> 1624 <Y1>212</Y1> 1625 <X2>622</X2> 1626 <Y2>68</Y2> 1627 <Block_Source>F101_1</Block_Source> 1628 <Port_Source>OutletVapour</Port_Source> 1629 <Block_Target>valve_Vapour</Block_Target> 1630 <Port_Target>Inlet</Port_Target> 1631 </Line> 1632 <Line> 1633 <Line_Name>3</Line_Name> 1634 <X1>550.5</X1> 1635 <Y1>344.2</Y1> 1636 <X2>407</X2> 1637 <Y2>337</Y2> 1638 <Block_Source>HeatToFlash</Block_Source> 1639 <Port_Source>OutletQ</Port_Source> 1640 <Block_Target>F101_1</Block_Target> 1641 <Port_Target>InletQ</Port_Target> 1642 </Line> 1643 <Line> 1644 <Line_Name>4</Line_Name> 1645 <X1>352.71</X1> 1646 <Y1>369.5</Y1> 1647 <X2>499</X2> 1648 <Y2>546</Y2> 1649 <Block_Source>F101_1</Block_Source> 1650 <Port_Source>OutletLiquid</Port_Source> 1651 <Block_Target>valve_liquid</Block_Target> 1652 <Port_Target>Inlet</Port_Target> 1653 </Line> 1654 <Line> 1655 <Line_Name>7</Line_Name> 1656 <X1>408</X1> 1657 <Y1>304.925</Y1> 1658 <X2>677</X2> 1659 <Y2>322</Y2> 1660 <Block_Source>F101_1</Block_Source> 1661 <Port_Source>LI</Port_Source> 1662 <Block_Target>PID_LC</Block_Target> 1663 <Port_Target>Input</Port_Target> 1664 </Line> 1665 <Line> 1666 <Line_Name>8</Line_Name> 1667 <X1>408</X1> 1668 <Y1>245.075</Y1> 1669 <X2>890</X2> 1670 <Y2>238</Y2> 1671 <Block_Source>F101_1</Block_Source> 1672 <Port_Source>PI</Port_Source> 1673 <Block_Target>PID_PC</Block_Target> 1674 <Port_Target>Input</Port_Target> 1675 </Line> 1663 1676 </Diagram> -
branches/gui/sample/stage_separators/Sample_flash_PIDincr.mso
r749 r796 36 36 37 37 SET 38 F101.VesselVolume = 8 * 'm^3';39 38 F101.Orientation = "vertical"; 39 F101.Heads = "flat"; 40 40 F101.Diameter = 3.1 * 'm'; 41 F101.Lenght = 6 * 'm'; 41 42 F101.Levelpercent_Initial = 0.70; 42 43 F101.Temperature_Initial = 383 * 'K'; … … 137 138 PIDIncr_LC.tauSet = 1 * 's'; 138 139 PIDIncr_LC.MinInput = 0; 139 PIDIncr_LC.MaxInput = 2.36;140 PIDIncr_LC.MaxInput = 1; 140 141 PIDIncr_LC.MinOutput = 0; 141 142 PIDIncr_LC.MaxOutput = 1; … … 188 189 OPTIONS 189 190 Dynamic = true; 190 TimeStep = 0. 02;191 TimeStep = 0.2; 191 192 TimeEnd = 1; 192 193 TimeUnit = 'h'; … … 194 195 NLASolver( 195 196 File = "sundials", 196 RelativeAccuracy = 1e- 3,197 RelativeAccuracy = 1e-2, 197 198 AbsoluteAccuracy = 1e-3, 198 199 MaxIterations = 100 … … 200 201 DAESolver( 201 202 File = "sundials", 202 RelativeAccuracy = 1e- 3,203 RelativeAccuracy = 1e-2, 203 204 AbsoluteAccuracy = 1e-6, 204 205 EventAccuracy = 1e-2 -
branches/gui/sample/stage_separators/Sample_flash_PIDincr.pfd
r714 r796 12 12 <Dynamic>1</Dynamic> 13 13 <Time_Start>0</Time_Start> 14 <Time_Step>0. 02</Time_Step>14 <Time_Step>0.2</Time_Step> 15 15 <Time_End>1</Time_End> 16 16 <Time_Unit>h</Time_Unit> … … 20 20 <NLASolver_File_Index>0</NLASolver_File_Index> 21 21 <NLASolver_File_Text>sundials</NLASolver_File_Text> 22 <NLASolver_Relative_Accuracy>1e-2</NLASolver_Relative_Accuracy> 22 23 <NLASolver_Absolute_Accuracy>1e-3</NLASolver_Absolute_Accuracy> 23 24 <DAESolver_File_Index>0</DAESolver_File_Index> 24 25 <DAESolver_File_Text>sundials</DAESolver_File_Text> 25 <DAESolver_Relative_Accuracy>1e- 3</DAESolver_Relative_Accuracy>26 <DAESolver_Relative_Accuracy>1e-2</DAESolver_Relative_Accuracy> 26 27 <DAESolver_Absolute_Accuracy>1e-6</DAESolver_Absolute_Accuracy> 27 28 <DAESolver_Evt_Accuracy>1e-2</DAESolver_Evt_Accuracy> … … 34 35 <Show_Grid>0</Show_Grid> 35 36 <Snap_to_Grid>0</Snap_to_Grid> 36 <Width>1 020</Width>37 <Height>5 41</Height>37 <Width>1248</Width> 38 <Height>511</Height> 38 39 <X>0</X> 39 <Y> 0</Y>40 <Y>-100</Y> 40 41 </View> 41 42 <View> … … 43 44 <Show_Grid>0</Show_Grid> 44 45 <Snap_to_Grid>0</Snap_to_Grid> 45 <Width>1 020</Width>46 <Width>1248</Width> 46 47 <Height>0</Height> 47 48 <X>0</X> … … 51 52 <Type>energy_source</Type> 52 53 <Id_String>HeatToFlash</Id_String> 53 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/icon/energy_source.png</Image_File_Name>54 <X>1 41</X>55 <Y> 401</Y>54 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/energy_source.png</Image_File_Name> 55 <X>131</X> 56 <Y>391</Y> 56 57 <Z>0</Z> 57 58 <Width>72.5</Width> … … 74 75 <Type>flash</Type> 75 76 <Id_String>F101</Id_String> 76 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/stage_separators/icon/Flash.png</Image_File_Name>77 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/stage_separators/icon/Flash.png</Image_File_Name> 77 78 <X>254</X> 78 <Y>8 2</Y>79 <Y>83</Y> 79 80 <Z>0</Z> 80 <Width>1 95</Width>81 <Height>2 56</Height>81 <Width>114</Width> 82 <Height>200</Height> 82 83 <Block_Properties> 83 84 <Model_File_Path>stage_separators/flash</Model_File_Path> … … 330 331 </Parameters> 331 332 <Parameters> 332 <Desc>VesselVolume</Desc>333 <Index>0</Index>334 <Values>8</Values>335 <Status>4</Status>336 <Unit>m^3</Unit>337 </Parameters>338 <Parameters>339 333 <Desc>Orientation</Desc> 340 334 <Index>0</Index> … … 343 337 </Parameters> 344 338 <Parameters> 339 <Desc>Heads</Desc> 340 <Index>0</Index> 341 <Values>flat</Values> 342 <Status>4</Status> 343 </Parameters> 344 <Parameters> 345 345 <Desc>Diameter</Desc> 346 346 <Index>0</Index> 347 347 <Values>3.1</Values> 348 <Status>4</Status> 349 <Unit>m</Unit> 350 </Parameters> 351 <Parameters> 352 <Desc>Lenght</Desc> 353 <Index>0</Index> 354 <Values>6</Values> 348 355 <Status>4</Status> 349 356 <Unit>m</Unit> … … 437 444 <Status>0</Status> 438 445 <Unit>m</Unit> 439 </Variables>440 <Variables>441 <Desc>Across</Desc>442 <Index>0</Index>443 <Values>7.54768</Values>444 <Status>0</Status>445 <Unit>m^2</Unit>446 446 </Variables> 447 447 <Variables> … … 487 487 <Type>simple_source</Type> 488 488 <Id_String>Feed</Id_String> 489 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/icon/Source.png</Image_File_Name>489 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/Source.png</Image_File_Name> 490 490 <X>18</X> 491 491 <Y>242</Y> … … 650 650 <Type>sink</Type> 651 651 <Id_String>VaporProduct</Id_String> 652 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/icon/Sink.png</Image_File_Name>653 <X>10 17</X>654 <Y> 77</Y>652 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/Sink.png</Image_File_Name> 653 <X>1000</X> 654 <Y>224</Y> 655 655 <Z>0</Z> 656 656 <Width>68</Width> … … 822 822 <Type>sink</Type> 823 823 <Id_String>LiquidProduct</Id_String> 824 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/icon/Sink.png</Image_File_Name>824 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/icon/Sink.png</Image_File_Name> 825 825 <X>888</X> 826 826 <Y>509</Y> … … 994 994 <Type>PIDIncr</Type> 995 995 <Id_String>PIDIncr_PC</Id_String> 996 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/controllers/icon/PIDincr.png</Image_File_Name>997 <X> 701</X>998 <Y>1 38</Y>996 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/PIDincr.png</Image_File_Name> 997 <X>526</X> 998 <Y>100</Y> 999 999 <Z>0</Z> 1000 <Width> 113</Width>1001 <Height> 121</Height>1000 <Width>56</Width> 1001 <Height>57</Height> 1002 1002 <Block_Properties> 1003 1003 <Model_File_Path>controllers/PIDIncr</Model_File_Path> … … 1134 1134 <Type>PIDIncr</Type> 1135 1135 <Id_String>PIDIncr_LC</Id_String> 1136 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/controllers/icon/PIDincr.png</Image_File_Name>1137 <X>6 42</X>1138 <Y>3 22</Y>1136 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/controllers/icon/PIDincr.png</Image_File_Name> 1137 <X>685</X> 1138 <Y>386</Y> 1139 1139 <Z>0</Z> 1140 <Width> 113</Width>1141 <Height> 121</Height>1140 <Width>56</Width> 1141 <Height>50</Height> 1142 1142 <Block_Properties> 1143 1143 <Model_File_Path>controllers/PIDIncr</Model_File_Path> … … 1236 1236 <Desc>MaxInput</Desc> 1237 1237 <Index>0</Index> 1238 <Values> 2.36</Values>1238 <Values>1</Values> 1239 1239 <Status>4</Status> 1240 1240 </Parameters> … … 1274 1274 <Type>valve_flow</Type> 1275 1275 <Id_String>valve_liquid</Id_String> 1276 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/pressure_changers/icon/Valve.png</Image_File_Name>1276 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/pressure_changers/icon/Valve.png</Image_File_Name> 1277 1277 <X>573</X> 1278 1278 <Y>517</Y> … … 1458 1458 <Type>valve_flow</Type> 1459 1459 <Id_String>valve_vapour</Id_String> 1460 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/pressure_changers/icon/Valve.png</Image_File_Name>1461 <X> 563</X>1462 <Y> 62</Y>1460 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/pressure_changers/icon/Valve.png</Image_File_Name> 1461 <X>712</X> 1462 <Y>109</Y> 1463 1463 <Z>0</Z> 1464 1464 <Width>52</Width> … … 1641 1641 <Line> 1642 1642 <Line_Name>2</Line_Name> 1643 <X1>2 13.5</X1>1644 <Y1>4 18.48</Y1>1645 <X2> 449</X2>1646 <Y2>2 75.51</Y2>1643 <X1>203.5</X1> 1644 <Y1>406.2</Y1> 1645 <X2>368</X2> 1646 <Y2>245</Y2> 1647 1647 <Block_Source>HeatToFlash</Block_Source> 1648 1648 <Port_Source>OutletQ</Port_Source> … … 1655 1655 <Y1>257.768</Y1> 1656 1656 <X2>254</X2> 1657 <Y2> 220.778</Y2>1657 <Y2>179</Y2> 1658 1658 <Block_Source>Feed</Block_Source> 1659 1659 <Port_Source>Outlet</Port_Source> … … 1663 1663 <Line> 1664 1664 <Line_Name>8</Line_Name> 1665 <X1> 449</X1>1666 <Y1>1 58.8</Y1>1667 <X2> 701</X2>1668 <Y2>1 98.5</Y2>1665 <X1>368</X1> 1666 <Y1>125</Y1> 1667 <X2>526</X2> 1668 <Y2>128.5</Y2> 1669 1669 <Block_Source>F101</Block_Source> 1670 1670 <Port_Source>PI</Port_Source> … … 1674 1674 <Line> 1675 1675 <Line_Name>4</Line_Name> 1676 <X1> 449</X1>1677 <Y1> 184.4</Y1>1678 <X2>6 46</X2>1679 <Y2> 388</Y2>1676 <X1>368</X1> 1677 <Y1>201</Y1> 1678 <X2>685</X2> 1679 <Y2>411</Y2> 1680 1680 <Block_Source>F101</Block_Source> 1681 1681 <Port_Source>LI</Port_Source> … … 1685 1685 <Line> 1686 1686 <Line_Name>1</Line_Name> 1687 <X1>7 03.02</X1>1688 <Y1>4 43</Y1>1687 <X1>715.24</X1> 1688 <Y1>436</Y1> 1689 1689 <X2>596</X2> 1690 1690 <Y2>522</Y2> … … 1707 1707 <Line> 1708 1708 <Line_Name>5</Line_Name> 1709 <X1> 615</X1>1710 <Y1> 95.5108</Y1>1711 <X2>10 18</X2>1712 <Y2> 92</Y2>1709 <X1>764</X1> 1710 <Y1>142.511</Y1> 1711 <X2>1000</X2> 1712 <Y2>239.924</Y2> 1713 1713 <Block_Source>valve_vapour</Block_Source> 1714 1714 <Port_Source>Outlet</Port_Source> … … 1718 1718 <Line> 1719 1719 <Line_Name>9</Line_Name> 1720 <X1> 762.02</X1>1721 <Y1> 259</Y1>1722 <X2> 589</X2>1723 <Y2> 62</Y2>1720 <X1>556.24</X1> 1721 <Y1>157</Y1> 1722 <X2>738</X2> 1723 <Y2>109</Y2> 1724 1724 <Block_Source>PIDIncr_PC</Block_Source> 1725 1725 <Port_Source>Output</Port_Source> … … 1729 1729 <Line> 1730 1730 <Line_Name>3</Line_Name> 1731 <X1>3 47.405</X1>1732 <Y1> 338</Y1>1731 <X1>303.02</X1> 1732 <Y1>283</Y1> 1733 1733 <X2>576</X2> 1734 1734 <Y2>551</Y2> … … 1740 1740 <Line> 1741 1741 <Line_Name>6</Line_Name> 1742 <X1>3 49.101</X1>1743 <Y1>8 2</Y1>1744 <X2> 569</X2>1745 <Y2> 92</Y2>1742 <X1>303.02</X1> 1743 <Y1>83</Y1> 1744 <X2>712</X2> 1745 <Y2>142.511</Y2> 1746 1746 <Block_Source>F101</Block_Source> 1747 1747 <Port_Source>OutletVapour</Port_Source> -
branches/gui/sample/stage_separators/sample_flash.mso
r749 r796 3 3 *----------------------------------------------*# 4 4 5 using "pressure_changers/valve"; 5 6 using "streams"; 7 using "controllers/PIDs"; 6 8 using "stage_separators/flash"; 7 using "pressure_changers/valve";8 using "controllers/PIDs";9 9 10 10 FlowSheet sample_flash … … 19 19 SET 20 20 NComp = PP.NumberOfComponents; 21 22 DEVICES23 Heat as energy_source;24 25 SET26 27 SPECIFY28 Heat.OutletQ = 1026.32 * 'kW';29 30 INITIAL31 32 GUESS33 34 DEVICES35 F101 as flash;36 37 SET38 F101.VesselVolume = 8 * 'm^3';39 F101.Orientation = "vertical";40 F101.Diameter = 2 * 'm';41 F101.Levelpercent_Initial = 0.80;42 F101.Temperature_Initial = 373 * 'K';43 F101.Composition_Initial(1) = 0.30;44 F101.Composition_Initial(2) = 0.40;45 F101.Composition_Initial(3) = 0.30;46 47 SPECIFY48 49 INITIAL50 51 GUESS52 21 53 22 DEVICES … … 200 169 GUESS 201 170 171 DEVICES 172 F101 as flash; 173 174 SET 175 F101.Orientation = "vertical"; 176 F101.Heads = "hemispherical"; 177 F101.Diameter = 2 * 'm'; 178 F101.Lenght = 5 * 'm'; 179 F101.Levelpercent_Initial = 0.80; 180 F101.Temperature_Initial = 373 * 'K'; 181 F101.Composition_Initial(1) = 0.30; 182 F101.Composition_Initial(2) = 0.40; 183 F101.Composition_Initial(3) = 0.30; 184 185 SPECIFY 186 187 INITIAL 188 189 GUESS 190 191 DEVICES 192 heat_duty as energy_source2; 193 194 SET 195 196 SPECIFY 197 heat_duty.OutletQ = 1026.32 * 'kW'; 198 199 INITIAL 200 201 GUESS 202 202 203 CONNECTIONS 203 Heat.OutletQ to F101.InletQ;204 204 PCV.Outlet to VaporProduct.Inlet; 205 205 LCV.Outlet to LiquidProduct.Inlet; 206 206 Feed.Outlet to FeedValve.Inlet; 207 207 FeedStep.OutSignal to FeedValve.FlowFraction; 208 PID_LC.Output to LCV.FlowFraction; 209 PID_PC.Output to PCV.FlowFraction; 208 210 FeedValve.Outlet to F101.Inlet; 209 F101.LI to PID_LC.Input; 210 PID_LC.Output to LCV.FlowFraction; 211 F101.PI to PID_PC.Input; 212 PID_PC.Output to PCV.FlowFraction; 211 heat_duty.OutletQ to F101.InletQ; 213 212 F101.OutletLiquid to LCV.Inlet; 214 213 F101.OutletVapour to PCV.Inlet; 214 F101.LI to PID_LC.Input; 215 F101.PI to PID_PC.Input; 215 216 216 217 OPTIONS -
branches/gui/sample/stage_separators/sample_flash.pfd
r711 r796 32 32 <View> 33 33 <Zoom_Level>1</Zoom_Level> 34 <Show_Grid> 0</Show_Grid>35 <Snap_to_Grid> 0</Snap_to_Grid>36 <Width>1 016</Width>37 <Height> 495</Height>34 <Show_Grid>1</Show_Grid> 35 <Snap_to_Grid>1</Snap_to_Grid> 36 <Width>1248</Width> 37 <Height>511</Height> 38 38 <X>0</X> 39 <Y> -100</Y>39 <Y>0</Y> 40 40 </View> 41 41 <View> 42 42 <Zoom_Level>1</Zoom_Level> 43 <Show_Grid> 0</Show_Grid>44 <Snap_to_Grid> 0</Snap_to_Grid>45 <Width>1 016</Width>43 <Show_Grid>1</Show_Grid> 44 <Snap_to_Grid>1</Snap_to_Grid> 45 <Width>1248</Width> 46 46 <Height>0</Height> 47 47 <X>0</X> 48 <Y>- 241</Y>48 <Y>-57</Y> 49 49 </View> 50 50 <Block> 51 <Type> energy_source</Type>52 <Id_String> Heat</Id_String>53 <Image_File_Name>/home/ bicca/apps/biblioteca/branches/gui/eml/icon/energy_source.png</Image_File_Name>54 <X> 39</X>55 <Y> 343</Y>51 <Type>valve_flow</Type> 52 <Id_String>LCV</Id_String> 53 <Image_File_Name>/home/gerson/repositorio/alsoc/biblioteca/branches/gui/eml/pressure_changers/icon/Valve.png</Image_File_Name> 54 <X>504</X> 55 <Y>423</Y> 56 56 <Z>0</Z> 57 <Width>72.5</Width> 58 <Height>38</Height> 57 <Width>64</Width> 58 <Height>43</Height> 59 <Block_Properties> 60 <Model_File_Path>pressure_changers/valve</Model_File_Path> 61 <Instance_Id>LCV</Instance_Id> 62 <Model_Name>valve_flow</Model_Name> 63 <T_Connection>0</T_Connection> 64 <Sub_Models> 65 <Block_Properties> 66 <Model_File_Path>pressure_changers/valve</Model_File_Path> 67 <Instance_Id>Inlet</Instance_Id> 68 <Model_Name>Inlet</Model_Name> 69 <T_Connection>1</T_Connection> 70 <Base_Models> 71 <Block_Properties> 72 <Model_File_Path>streams</Model_File_Path> 73 <Instance_Id>Inlet</Instance_Id> 74 <Model_Name>stream</Model_Name> 75 <T_Connection>1</T_Connection> 76 <Parameters> 77 <Desc>NComp</Desc> 78 <Index>0</Index> 79 <Values>3</Values> 80 <Status>0</Status> 81 </Parameters> 82 <Variables> 83 <Desc>F</Desc> 84 <Index>0</Index> 85 <Values>390.714</Values> 86 <Status>0</Status> 87 <Unit>kmol/h</Unit> 88 </Variables> 89 <Variables> 90 <Desc>T</Desc> 91 <Index>0</Index> 92 <Values>368.654</Values> 93 <Status>0</Status> 94 <Unit>K</Unit> 95 </Variables> 96 <Variables> 97 <Desc>P</Desc> 98 <Index>0</Index>