Changeset 578 for branches/gui
- Timestamp:
- Jul 25, 2008, 7:24:26 PM (15 years ago)
- Location:
- branches/gui
- Files:
-
- 20 edited
Legend:
- Unmodified
- Added
- Removed
-
branches/gui/eml/streams.mso
r577 r578 125 125 pressure '''P''' and the enthalpy '''h'''. 126 126 127 Additionally, the liquid composition '''x''' andthe vapor128 composition '''y''' a re calculated.127 Additionally, the liquid composition '''x''', the vapor 128 composition '''y''' and the stream entropy are calculated. 129 129 "; 130 130 Pallete = false; … … 140 140 "Entropy" 141 141 s = (1-v)*PP.LiquidEntropy(T, P, x) + v*PP.VapourEntropy(T, P, y); 142 143 end144 145 Model source146 ATTRIBUTES147 Pallete = true;148 Icon = "icon/Source";149 Brief = "Material stream source";150 Info = "151 This model should be used for boundary streams.152 Usually these streams are known and come from another process153 units.154 155 The user should specify:156 * Total molar (mass or volumetric) flow157 * Temperature158 * Pressure159 * Molar (mass or volumetric) composition160 161 No matter the specification set, the model will calculate some162 additional properties:163 * Mass density164 * Mass flow165 * Mass compostions166 * Specific volume167 * Vapour fraction168 * Volumetric flow169 * Liquid and Vapour compositions170 ";171 172 PARAMETERS173 outer PP as Plugin (Brief = "External Physical Properties", Type="PP");174 outer NComp as Integer (Brief = "Number of chemical components", Lower = 1);175 M(NComp) as molweight (Brief = "Component Mol Weight");176 rhoModel as Switcher (Brief = "Density model", Valid = ["volume", "correlation"], Default="volume");177 178 SET179 180 M = PP.MolecularWeight();181 182 VARIABLES183 out Outlet as stream (Brief = "Outlet stream", PosX=1, PosY=0.5256, Symbol="_{out}");184 x(NComp) as fraction (Brief = "Liquid Molar Fraction",Hidden=true);185 y(NComp) as fraction (Brief = "Vapour Molar Fraction",Hidden=true);186 hl as enth_mol (Brief = "Liquid Enthalpy");187 hv as enth_mol (Brief = "Vapour Enthalpy");188 s as entr_mol (Brief = "Stream Entropy");189 sl as entr_mol (Brief = "Liquid Entropy");190 sv as entr_mol (Brief = "Vapour Entropy");191 zmass(NComp) as fraction (Brief = "Mass Fraction");192 Mw as molweight (Brief = "Average Mol Weight");193 vm as volume_mol (Brief = "Molar Volume");194 rho as dens_mass (Brief = "Stream Mass Density");195 rhom as dens_mol (Brief = "Stream Molar Density");196 Fw as flow_mass (Brief = "Stream Mass Flow");197 Fvol as flow_vol (Brief = "Volumetric Flow");198 T_Cdeg as temperature (Brief = "Temperature in °C", Lower=-200);199 200 EQUATIONS201 "Flash Calculation"202 [Outlet.v, x, y] = PP.Flash(Outlet.T, Outlet.P, Outlet.z);203 204 "Overall Enthalpy"205 Outlet.h = (1-Outlet.v)*hl + Outlet.v*hv;206 207 "Liquid Enthalpy"208 hl = PP.LiquidEnthalpy(Outlet.T, Outlet.P, x);209 210 "Vapour Enthalpy"211 hv = PP.VapourEnthalpy(Outlet.T, Outlet.P, y);212 213 "Overall Entropy"214 s = (1-Outlet.v)*sl + Outlet.v*sv;215 216 "Liquid Entropy"217 sl = PP.LiquidEntropy(Outlet.T, Outlet.P, x);218 219 "Vapour Entropy"220 sv = PP.VapourEntropy(Outlet.T, Outlet.P, y);221 222 "Average Molecular Weight"223 Mw = sum(M*Outlet.z);224 225 switch rhoModel226 case "volume":227 "Molar Density"228 rhom * vm = 1;229 230 case "correlation":231 "Mass Density"232 rho*((1-Outlet.v)/PP.LiquidDensity(Outlet.T,Outlet.P,x) + Outlet.v/PP.VapourDensity(Outlet.T,Outlet.P,y)) = 1;233 end234 235 "Mass or Molar Density"236 rhom * Mw = rho;237 238 "Flow Mass"239 Fw = Mw*Outlet.F;240 241 "Molar Volume"242 vm = (1-Outlet.v)*PP.LiquidVolume(Outlet.T, Outlet.P, x) + Outlet.v*PP.VapourVolume(Outlet.T,Outlet.P,y);243 244 "Volumetric Flow"245 Fvol = Outlet.F*vm ;246 247 "Mass Fraction"248 zmass = M*Outlet.z / Mw;249 250 "Temperature in °C"251 T_Cdeg = Outlet.T - 273.15 * 'K';252 142 253 143 end … … 532 422 end 533 423 534 Model source _testing424 Model source 535 425 536 426 ATTRIBUTES -
branches/gui/sample/controllers/Sample_flash_pid.mso
r560 r578 123 123 EQUATIONS 124 124 #Feed stream 125 s1. Outlet.z= [0.3, 0.3, 0.4];126 s1. Outlet.P = 5 * 'atm';125 s1.Composition = [0.3, 0.3, 0.4]; 126 s1.P = 5 * 'atm'; 127 127 128 128 #Disturbance 129 129 if time < 0.5*'h' then 130 s1. Outlet.T = 338 * 'K';131 s1. Outlet.F = 496.3 * 'kmol/h';130 s1.T = 338 * 'K'; 131 s1.F = 496.3 * 'kmol/h'; 132 132 else 133 s1. Outlet.T = 360 * 'K';134 s1. Outlet.F = 450 * 'kmol/h';133 s1.T = 360 * 'K'; 134 s1.F = 450 * 'kmol/h'; 135 135 end 136 136 -
branches/gui/sample/miscellaneous/sample_streams.mso
r218 r578 70 70 71 71 SPECIFY 72 sl.Outlet.F = 10 * 'kmol/h'; 73 sl.Outlet.T = 300 * 'K'; 74 sl.Outlet.P = 100 * 'kPa'; 75 sl.Outlet.z = [0.24596, 0.370278, 0.383762]; 76 # sl.Outlet.v = 0.0; #liquid stream 72 sl.F = 1 * 'kmol/h'; 73 sl.T = 300 * 'K'; 74 sl.P = 100 * 'kPa'; 75 sl.Composition = [0.24596, 0.370278, 0.383762]; 77 76 78 77 79 sv.Outlet.F = 10 * 'kmol/h'; 80 #sv.Outlet.h = 20248 * 'J/mol'; 81 sv.Outlet.T = 300 * 'K'; 82 sv.Outlet.P = 100 * 'kPa'; 83 #sv.Outlet.z = [0.824212, 0.12577, 0.0500176]; 84 # sv.Outlet.v = 1.0; #vapor stream 78 sv.F = 1 * 'kmol/h'; 79 sv.T = 300 * 'K'; 80 sv.P = 100 * 'kPa'; 81 sv.Composition = [0.824212, 0.12577, 0.0500176]; 85 82 86 EQUATIONS 87 "Liquid-Vapour equilibrium" 88 PP.VapourFugacityCoefficient(sv.Outlet.T, sv.Outlet.P, sv.Outlet.z) * sv.Outlet.z = 89 PP.LiquidFugacityCoefficient(sl.Outlet.T, sl.Outlet.P, sl.Outlet.z) * sl.Outlet.z; 90 83 84 91 85 OPTIONS 92 Dynamic= true;86 Dynamic= false; 93 87 end -
branches/gui/sample/mixers_splitters/sample_mixer.mso
r400 r578 37 37 stream1 as source; 38 38 stream2 as source; 39 mixer1 as mixer ;39 mixer1 as mixer_n; 40 40 41 41 … … 45 45 mixer1.Ninlet = 2; 46 46 47 stream1.ValidPhases = "Vapour-Liquid"; 48 stream1.CompostionBasis = "Molar"; 49 50 stream2.ValidPhases = "Vapour-Liquid"; 51 stream2.CompostionBasis = "Molar"; 52 47 53 CONNECTIONS 48 54 stream1.Outlet to mixer1.Inlet(1); … … 51 57 SPECIFY 52 58 53 stream1. Outlet.F = 20 * 'kmol/h';54 stream1. Outlet.P = 120 * 'kPa';55 stream1. Outlet.T = 400 * 'K';56 stream1. Outlet.z= [0.5, 0.1, 0.4];59 stream1.F = 20 * 'kmol/h'; 60 stream1.P = 120 * 'kPa'; 61 stream1.T = 400 * 'K'; 62 stream1.Composition = [0.5, 0.1, 0.4]; 57 63 58 64 59 stream2. Outlet.F = 10 * 'kmol/h';60 stream2. Outlet.P = 120 * 'kPa';61 stream2. Outlet.T = 290 * 'K';62 stream2. Outlet.z= [0.5, 0.1, 0.4];65 stream2.F = 10 * 'kmol/h'; 66 stream2.P = 120 * 'kPa'; 67 stream2.T = 290 * 'K'; 68 stream2.Composition = [0.5, 0.1, 0.4]; 63 69 64 70 OPTIONS -
branches/gui/sample/mixers_splitters/sample_sepComp.mso
r247 r578 48 48 sep.mainComp = 1; 49 49 sep.NOutlet = 3; 50 51 Stream.ValidPhases = "Vapour-Liquid"; 52 Stream.CompostionBasis = "Molar"; 50 53 51 54 SPECIFY 52 Stream. Outlet.F = 30 * 'kmol/h';53 Stream. Outlet.P = 120 * 'kPa';54 Stream. Outlet.T = 290 * 'K';55 Stream. Outlet.z= [0.6, 0.4];55 Stream.F = 30 * 'kmol/h'; 56 Stream.P = 120 * 'kPa'; 57 Stream.T = 290 * 'K'; 58 Stream.Composition = [0.6, 0.4]; 56 59 57 60 sep.Outlet(1).z(1) = 0.7; … … 88 91 NComp = PP.NumberOfComponents; 89 92 sep.mainComp = 1; 93 94 Stream.ValidPhases = "Vapour-Liquid"; 95 Stream.CompostionBasis = "Molar"; 90 96 91 97 SPECIFY 92 Stream. Outlet .F = 30 * 'kmol/h';93 Stream. Outlet .P = 120 * 'kPa';94 Stream. Outlet .T = 290 * 'K';95 Stream. Outlet .z= [0.6, 0.4];98 Stream.F = 30 * 'kmol/h'; 99 Stream.P = 120 * 'kPa'; 100 Stream.T = 290 * 'K'; 101 Stream.Composition = [0.6, 0.4]; 96 102 97 103 sep.Outlet1.z(1) = 0.7; -
branches/gui/sample/mixers_splitters/sample_splitter.mso
r366 r578 44 44 NComp = PP.NumberOfComponents; 45 45 Splitter.NOutlet = 3; 46 47 Stream.ValidPhases = "Vapour-Liquid"; 48 Stream.CompostionBasis = "Molar"; 46 49 47 50 SPECIFY 48 Stream. Outlet.F = 153 * 'kmol/h';49 Stream. Outlet.P = 150 * 'kPa';50 Stream. Outlet.T = 298.6 * 'K';51 Stream. Outlet.z= [0.6, 0.4];51 Stream.F = 153 * 'kmol/h'; 52 Stream.P = 150 * 'kPa'; 53 Stream.T = 298.6 * 'K'; 54 Stream.Composition = [0.6, 0.4]; 52 55 53 56 Splitter.frac(1) = 0.4; -
branches/gui/sample/optimization/ammonia.mso
r574 r578 155 155 156 156 SPECIFY 157 FEED. Outlet.F = 2000 * 'lbmol/h';158 FEED. Outlet.T = (27 + 273.15) * 'K';159 FEED. Outlet.P = 10 * 'atm';160 FEED. Outlet.z= [0.74, 0.24, 0.01, 0.01, 0.0];157 FEED.F = 2000 * 'lbmol/h'; 158 FEED.T = (27 + 273.15) * 'K'; 159 FEED.P = 10 * 'atm'; 160 FEED.Composition = [0.74, 0.24, 0.01, 0.01, 0.0]; 161 161 162 162 C101.Outlet.P = 200 * 'atm'; -
branches/gui/sample/optimization/ammonia_opt.mso
r428 r578 26 26 MINIMIZE 27 27 28 (abs(Q1.OutletQ .Q) + abs(Q2.OutletQ.Q))*1e-628 (abs(Q1.OutletQ) + abs(Q2.OutletQ))*1e-6 29 29 #loose / 'lbmol/h' 30 30 # C102.Pot/'kW'*180 -
branches/gui/sample/optimization/flash_opt.mso
r425 r578 54 54 55 55 SPECIFY 56 s1. Outlet.F = 496.3 * 'kmol/h';57 s1. Outlet.T = 338 * 'K';58 s1. Outlet.P = 507.1 * 'kPa';56 s1.F = 496.3 * 'kmol/h'; 57 s1.T = 338 * 'K'; 58 s1.P = 507.1 * 'kPa'; 59 59 #s1.Outlet.v = 0.1380; 60 s1. Outlet.z= [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283];60 s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283]; 61 61 62 62 fl.OutletL.P = 2.5 * 'atm'; -
branches/gui/sample/pressure_changers/sample_compressor.mso
r213 r578 46 46 SET 47 47 NComp = PP.NumberOfComponents; 48 49 S1.ValidPhases = "Liquid-Only"; 50 S1.CompostionBasis = "Molar"; 48 51 49 52 SPECIFY 50 53 C1.Effs = 0.75; 51 S1. Outlet.F = 41.05 * 'kmol/h';52 S1. Outlet.P = 1 * 'atm';53 S1. Outlet.T = 298 * 'K' ;54 S1. Outlet.z= [0.79,0.21];54 S1.F = 41.05 * 'kmol/h'; 55 S1.P = 1 * 'atm'; 56 S1.T = 298 * 'K' ; 57 S1.Composition = [0.79,0.21]; 55 58 56 59 C1.Outlet.P = 3 * 'atm'; -
branches/gui/sample/pressure_changers/sample_pump.mso
r372 r578 52 52 P1.Beta = 425e-6 * '1/K'; 53 53 54 S1.ValidPhases = "Vapour-Liquid"; 55 S1.CompostionBasis = "Molar"; 56 54 57 SPECIFY 55 S1. Outlet.F = 1000 * 'kmol/h';56 S1. Outlet.P = 10 * 'atm';57 S1. Outlet.T = 298 * 'K' ;58 S1. Outlet.z= [1,0];58 S1.F = 1000 * 'kmol/h'; 59 S1.P = 10 * 'atm'; 60 S1.T = 298 * 'K' ; 61 S1.Composition = [1,0]; 59 62 60 63 P1.Pdrop = -8 * 'kPa'; … … 74 77 NComp as Integer; 75 78 79 DEVICES 80 p1 as pump; 81 s1 as source; 82 76 83 SET 77 84 NComp = PP.NumberOfComponents; 78 85 79 DEVICES 80 p1 as pump; 81 s1 as source; 86 s1.ValidPhases = "Vapour-Liquid"; 87 s1.CompostionBasis = "Molar"; 88 89 82 90 83 91 CONNECTIONS … … 85 93 86 94 SPECIFY 87 s1. Outlet.F = 826 * 'kmol/h';88 s1. Outlet.P = 549 * 'kPa';89 s1. Outlet.T = 313 * 'K';90 s1. Outlet.z= 1/NComp;95 s1.F = 826 * 'kmol/h'; 96 s1.P = 549 * 'kPa'; 97 s1.T = 313 * 'K'; 98 s1.Composition = 1/NComp; 91 99 #s1.Outlet.v = 0.68; 92 100 -
branches/gui/sample/pressure_changers/sample_turbine.mso
r372 r578 30 30 DEVICES 31 31 S1 as source; 32 HT1 as Hidraulic _Turbine;32 HT1 as HidraulicTurbine; 33 33 34 34 CONNECTIONS … … 48 48 NComp = PP.NumberOfComponents(); 49 49 50 S1.ValidPhases = "Vapour-Liquid"; 51 S1.CompostionBasis = "Molar"; 52 50 53 SPECIFY 51 54 HT1.Beta = 425e-6 / 'K'; … … 53 56 HT1.Eff = 0.72; 54 57 55 S1. Outlet.F = 1000 * 'kmol/h';56 S1. Outlet.P = 5 * 'atm' ;57 S1. Outlet.T = 298 * 'K' ;58 S1. Outlet.z= [1];58 S1.F = 1000 * 'kmol/h'; 59 S1.P = 5 * 'atm' ; 60 S1.T = 298 * 'K' ; 61 S1.Composition = [1]; 59 62 60 63 #HT1.Pdrop = 100 * 'kPa'; -
branches/gui/sample/pressure_changers/sample_valve.mso
r573 r578 48 48 49 49 SPECIFY 50 s1. Outlet.P = 150 * 'kPa';51 s1. Outlet.T = 281.75 * 'K';52 s1. Outlet.z= [0.664, 0.336];50 s1.P = 150 * 'kPa'; 51 s1.T = 281.75 * 'K'; 52 s1.Composition = [0.664, 0.336]; 53 53 54 54 v1.x = 0.866; … … 87 87 88 88 SPECIFY 89 s1. Outlet.P = 185 * 'kPa';90 s1. Outlet.T = 328.12 * 'K';91 s1. Outlet.z= [0.001848, 0.9982];89 s1.P = 185 * 'kPa'; 90 s1.T = 328.12 * 'K'; 91 s1.Composition = [0.001848, 0.9982]; 92 92 93 93 v1.x = 0.3363; … … 127 127 128 128 SPECIFY 129 S1. Outlet.P = 2169.78 * 'kPa';130 S1. Outlet.T = 394.26 * 'K' ;131 S1. Outlet.z= [0.001848, 0.9982];129 S1.P = 2169.78 * 'kPa'; 130 S1.T = 394.26 * 'K' ; 131 S1.Composition = [0.001848, 0.9982]; 132 132 133 133 V1.Qv = 113.56 * 'm^3/h'; -
branches/gui/sample/processes/Sample_Flowsheet_with_results.pfd
r439 r578 1 <?xml version='1.0' encoding='ascii'?> 2 <Diagram> 3 <Physical_Properties> 4 <Component>benzene</Component> 5 <Component>water</Component> 6 <Liquid_Model>PR</Liquid_Model> 7 <Vapour_Model>PR</Vapour_Model> 8 </Physical_Properties> 9 <Options> 10 <Dynamic>1</Dynamic> 11 <Time_Step>1</Time_Step> 12 <Time_End>30</Time_End> 13 <Time_Unit_Index>1</Time_Unit_Index> 14 <Time_Unit_Text>min</Time_Unit_Text> 15 <Sparse_Algebra>1</Sparse_Algebra> 16 <Integration_Index>0</Integration_Index> 17 <Integration_Text>original</Integration_Text> 18 <NLASolver_File_Index>0</NLASolver_File_Index> 19 <NLASolver_File_Text>sundials</NLASolver_File_Text> 20 <DAESolver_File_Index>0</DAESolver_File_Index> 21 </Options> 22 <Width>2000</Width> 23 <Height>1000</Height> 24 <Grid_Spacing>20</Grid_Spacing> 25 <View> 26 <Zoom_Level>1</Zoom_Level> 27 <Show_Grid>1</Show_Grid> 28 <Snap_to_Grid>1</Snap_to_Grid> 29 <Width>851</Width> 30 <Height>521</Height> 31 <X>0</X> 32 <Y>-22</Y> 33 </View> 34 <View> 35 <Zoom_Level>1</Zoom_Level> 36 <Show_Grid>1</Show_Grid> 37 <Snap_to_Grid>1</Snap_to_Grid> 38 <Width>851</Width> 39 <Height>0</Height> 40 <X>0</X> 41 <Y>-15</Y> 42 </View> 43 <Block> 44 <Type>simple_sink</Type> 45 <Id_String>simple_sink_2</Id_String> 46 <Block_Name>simple_sink_2</Block_Name> 47 <Image_File_Name>E:\User\Arge\PROJETOS\Alsoc\EMSO\mso\eml\icon/Sink.png</Image_File_Name> 48 <X>580</X> 49 <Y>48</Y> 50 <Z>0</Z> 51 <Width>72.5</Width> 52 <Height>37</Height> 53 <Block_Properties> 54 <Sub_Models> 1 <?xml version="1.0"?> 2 <!-- VRTech xml file - http://www.vrtech.com.br --> 3 <Diagram version="1" revision="1"> 4 <Physical_Properties> 5 <Component>benzene</Component> 6 <Component>water</Component> 7 <Liquid_Model>PR</Liquid_Model> 8 <Vapour_Model>PR</Vapour_Model> 9 </Physical_Properties> 10 <Options> 11 <Dynamic>1</Dynamic> 12 <Time_Start></Time_Start> 13 <Time_Step>1</Time_Step> 14 <Time_End>30</Time_End> 15 <Time_Unit>s</Time_Unit> 16 <Sparse_Algebra>1</Sparse_Algebra> 17 <Integration_Index>0</Integration_Index> 18 <Integration_Text>original</Integration_Text> 19 <NLASolver_File_Index>0</NLASolver_File_Index> 20 <NLASolver_File_Text>sundials</NLASolver_File_Text> 21 <DAESolver_File_Index>2</DAESolver_File_Index> 22 <DAESolver_File_Text>dasslc</DAESolver_File_Text> 23 <DAESolver_Relative_Accuracy>1e-3</DAESolver_Relative_Accuracy> 24 <DAESolver_Absolute_Accuracy>1e-6</DAESolver_Absolute_Accuracy> 25 <DAESolver_Evt_Accuracy>1e-2</DAESolver_Evt_Accuracy> 26 </Options> 27 <Width>2000</Width> 28 <Height>1000</Height> 29 <Grid_Spacing>20</Grid_Spacing> 30 <View> 31 <Zoom_Level>1</Zoom_Level> 32 <Show_Grid>0</Show_Grid> 33 <Snap_to_Grid>0</Snap_to_Grid> 34 <Width>925</Width> 35 <Height>518</Height> 36 <X>0</X> 37 <Y>-22</Y> 38 </View> 39 <View> 40 <Zoom_Level>1</Zoom_Level> 41 <Show_Grid>0</Show_Grid> 42 <Snap_to_Grid>0</Snap_to_Grid> 43 <Width>925</Width> 44 <Height>0</Height> 45 <X>0</X> 46 <Y>-15</Y> 47 </View> 48 <Block> 49 <Type>simple_sink</Type> 50 <Id_String>simple_sink_2</Id_String> 51 <Image_File_Name>D:\Apps\repositorio\branches\gui\eml\icon/Sink.png</Image_File_Name> 52 <X>580</X> 53 <Y>48</Y> 54 <Z>0</Z> 55 <Width>72.5</Width> 56 <Height>37</Height> 57 <Block_Properties> 58 <Model_File_Path>streams</Model_File_Path> 59 <Instance_Id>simple_sink_2</Instance_Id> 60 <Model_Name>simple_sink</Model_Name> 61 <T_Connection>0</T_Connection> 62 <Sub_Models> 55 63 <Block_Properties> 56 <Base_Models> 64 <Model_File_Path>streams</Model_File_Path> 65 <Instance_Id>Inlet</Instance_Id> 66 <Model_Name>Inlet</Model_Name> 67 <T_Connection>1</T_Connection> 68 <Base_Models> 69 <Block_Properties> 70 <Model_File_Path>streams</Model_File_Path> 71 <Instance_Id>Inlet</Instance_Id> 72 <Model_Name>stream</Model_Name> 73 <T_Connection>1</T_Connection> 74 <Parameters> 75 <Desc>NComp</Desc> 76 <Index>0</Index> 77 <Values>2</Values> 78 <Status>0</Status> 79 </Parameters> 80 <Variables> 81 <Desc>F</Desc> 82 <Index>0</Index> 83 <Values>70</Values> 84 <Status>0</Status> 85 <Unit>kmol/h</Unit> 86 </Variables> 87 <Variables> 88 <Desc>T</Desc> 89 <Index>0</Index> 90 <Values>299.09</Values> 91 <Status>0</Status> 92 <Unit>K</Unit> 93 </Variables> 94 <Variables> 95 <Desc>P</Desc> 96 <Index>0</Index> 97 <Values>0.196926</Values> 98 <Status>0</Status> 99 <Unit>atm</Unit> 100 </Variables> 101 <Variables> 102 <Desc>h</Desc> 103 <Index>0</Index> 104 <Values>-95.3809</Values> 105 <Status>0</Status> 106 <Unit>kJ/kmol</Unit> 107 </Variables> 108 <Variables> 109 <Desc>v</Desc> 110 <Index>0</Index> 111 <Values>1</Values> 112 <Status>0</Status> 113 </Variables> 114 <Variables> 115 <Desc>z</Desc> 116 <Index>0</Index> 117 <Values>0.600793</Values> 118 <Status>0</Status> 119 <Index>1</Index> 120 <Values>0.399207</Values> 121 <Status>0</Status> 122 </Variables> 123 </Block_Properties> 124 </Base_Models> 125 </Block_Properties> 126 </Sub_Models> 127 </Block_Properties> 128 </Block> 129 <Block> 130 <Type>simple_sink</Type> 131 <Id_String>simple_sink_1</Id_String> 132 <Image_File_Name>D:\Apps\repositorio\branches\gui\eml\icon/Sink.png</Image_File_Name> 133 <X>587</X> 134 <Y>421</Y> 135 <Z>0</Z> 136 <Width>72.5</Width> 137 <Height>37</Height> 138 <Block_Properties> 139 <Model_File_Path>streams</Model_File_Path> 140 <Instance_Id>simple_sink_1</Instance_Id> 141 <Model_Name>simple_sink</Model_Name> 142 <T_Connection>0</T_Connection> 143 <Sub_Models> 57 144 <Block_Properties> 58 <Model_File_Path>streams</Model_File_Path> 59 <Instance_Id>Inlet.</Instance_Id> 60 <Model_Name>stream</Model_Name> 61 <T_Connection>1</T_Connection> 62 <Parameters> 63 <Desc>Inlet.NComp</Desc> 64 <Index>0</Index> 65 <Values>2</Values> 66 <Status>0</Status> 67 </Parameters> 68 <Variables> 69 <Desc>Inlet.F</Desc> 70 <Index>0</Index> 71 <Values>70</Values> 72 <Status>0</Status> 73 <Unit>kmol/h</Unit> 74 </Variables> 75 <Variables> 76 <Desc>Inlet.T</Desc> 77 <Index>0</Index> 78 <Values>299.09</Values> 79 <Status>0</Status> 80 <Unit>K</Unit> 81 </Variables> 82 <Variables> 83 <Desc>Inlet.P</Desc> 84 <Index>0</Index> 85 <Values>0.196926</Values> 86 <Status>0</Status> 87 <Unit>atm</Unit> 88 </Variables> 89 <Variables> 90 <Desc>Inlet.z</Desc> 91 <Index>0</Index> 92 <Values>0.600793</Values> 93 <Status>0</Status> 94 <Index>1</Index> 95 <Values>0.399207</Values> 96 <Status>0</Status> 97 </Variables> 98 <Variables> 99 <Desc>Inlet.h</Desc> 100 <Index>0</Index> 101 <Values>-95.3809</Values> 102 <Status>0</Status> 103 <Unit>kJ/kmol</Unit> 104 </Variables> 105 <Variables> 106 <Desc>Inlet.v</Desc> 107 <Index>0</Index> 108 <Values>1</Values> 109 <Status>0</Status> 110 </Variables> 145 <Model_File_Path>streams</Model_File_Path> 146 <Instance_Id>Inlet</Instance_Id> 147 <Model_Name>Inlet</Model_Name> 148 <T_Connection>1</T_Connection> 149 <Base_Models> 150 <Block_Properties> 151 <Model_File_Path>streams</Model_File_Path> 152 <Instance_Id>Inlet</Instance_Id> 153 <Model_Name>stream</Model_Name> 154 <T_Connection>1</T_Connection> 155 <Parameters> 156 <Desc>NComp</Desc> 157 <Index>0</Index> 158 <Values>2</Values> 159 <Status>0</Status> 160 </Parameters> 161 <Variables> 162 <Desc>F</Desc> 163 <Index>0</Index> 164 <Values>430</Values> 165 <Status>0</Status> 166 <Unit>kmol/h</Unit> 167 </Variables> 168 <Variables> 169 <Desc>T</Desc> 170 <Index>0</Index> 171 <Values>299.09</Values> 172 <Status>0</Status> 173 <Unit>K</Unit> 174 </Variables> 175 <Variables> 176 <Desc>P</Desc> 177 <Index>0</Index> 178 <Values>0.196926</Values> 179 <Status>0</Status> 180 <Unit>atm</Unit> 181 </Variables> 182 <Variables> 183 <Desc>h</Desc> 184 <Index>0</Index> 185 <Values>-32439.6</Values> 186 <Status>0</Status> 187 <Unit>kJ/kmol</Unit> 188 </Variables> 189 <Variables> 190 <Desc>v</Desc> 191 <Index>0</Index> 192 <Values>0</Values> 193 <Status>0</Status> 194 </Variables> 195 <Variables> 196 <Desc>z</Desc> 197 <Index>0</Index> 198 <Values>0.832429</Values> 199 <Status>0</Status> 200 <Index>1</Index> 201 <Values>0.167571</Values> 202 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<Status>0</Status> 479 </Parameters> 480 <Parameters> 481 <Desc>V</Desc> 482 <Index>0</Index> 483 <Values>10</Values> 484 <Status>0</Status> 485 <Unit>m^3</Unit> 486 </Parameters> 487 <Parameters> 488 <Desc>orientation</Desc> 489 <Index>0</Index> 490 <Values>vertical</Values> 491 <Status>0</Status> 492 </Parameters> 493 <Parameters> 494 <Desc>diameter</Desc> 495 <Index>0</Index> 496 <Values>1</Values> 497 <Status>0</Status> 498 <Unit>m</Unit> 499 </Parameters> 500 <Variables> 501 <Desc>M</Desc> 502 <Index>0</Index> 503 <Values>3.60581</Values> 504 <Status>0</Status> 505 <Unit>kmol</Unit> 506 <Index>1</Index> 507 <Values>0.747591</Values> 508 <Status>0</Status> 509 <Unit>kmol</Unit> 510 </Variables> 511 <Variables> 512 <Desc>ML</Desc> 513 <Index>0</Index> 514 <Values>4.27532</Values> 515 <Status>0</Status> 516 <Unit>kmol</Unit> 517 </Variables> 518 <Variables> 519 <Desc>MV</Desc> 520 <Index>0</Index> 521 <Values>0.0780847</Values> 522 <Status>0</Status> 523 <Unit>kmol</Unit> 524 </Variables> 525 <Variables> 526 <Desc>E</Desc> 527 <Index>0</Index> 528 <Values>-138897</Values> 529 <Status>0</Status> 530 <Unit>kJ</Unit> 531 </Variables> 532 <Variables> 533 <Desc>vL</Desc> 534 <Index>0</Index> 535 <Values>7.66096e-005</Values> 536 <Status>0</Status> 537 <Unit>m^3/mol</Unit> 538 </Variables> 539 <Variables> 540 <Desc>vV</Desc> 541 <Index>0</Index> 542 <Values>0.123872</Values> 543 <Status>0</Status> 544 <Unit>m^3/mol</Unit> 545 </Variables> 546 <Variables> 547 <Desc>Level</Desc> 548 <Index>0</Index> 549 <Values>0.417025</Values> 550 <Status>2</Status> 551 <Unit>m</Unit> 552 </Variables> 553 <Variables> 554 <Desc>Across</Desc> 555 <Index>0</Index> 556 <Values>0.785398</Values> 557 <Status>0</Status> 558 <Unit>m^2</Unit> 559 </Variables> 560 <Variables> 561 <Desc>vfrac</Desc> 562 <Index>0</Index> 563 <Values>0.14</Values> 564 <Status>0</Status> 565 </Variables> 566 </Block_Properties> 567 </Block> 568 <Block> 569 <Type>source</Type> 570 <Id_String>source_1</Id_String> 571 <Block_Name>source_1</Block_Name> 572 <Image_File_Name>E:\User\Arge\PROJETOS\Alsoc\EMSO\mso\eml\icon/Source.png</Image_File_Name> 573 <X>28</X> 574 <Y>236</Y> 575 <Z>0</Z> 576 <Width>72.5</Width> 577 <Height>37</Height> 578 <Block_Properties> 579 <Sub_Models> 580 <Block_Properties> 581 <Base_Models> 582 <Block_Properties> 583 <Model_File_Path>streams</Model_File_Path> 584 <Instance_Id>Outlet.</Instance_Id> 585 <Model_Name>stream</Model_Name> 586 <T_Connection>2</T_Connection> 587 <Parameters> 588 <Desc>Outlet.NComp</Desc> 589 <Index>0</Index> 590 <Values>2</Values> 591 <Status>0</Status> 592 </Parameters> 593 <Variables> 594 <Desc>Outlet.F</Desc> 595 <Index>0</Index> 596 <Values>500</Values> 597 <Status>1</Status> 598 <Unit>kmol/h</Unit> 599 </Variables> 600 <Variables> 601 <Desc>Outlet.T</Desc> 602 <Index>0</Index> 603 <Values>338</Values> 604 <Status>1</Status> 605 <Unit>K</Unit> 606 </Variables> 607 <Variables> 608 <Desc>Outlet.P</Desc> 609 <Index>0</Index> 610 <Values>507</Values> 611 <Status>1</Status> 612 <Unit>kPa</Unit> 613 </Variables> 614 <Variables> 615 <Desc>Outlet.z</Desc> 616 <Index>0</Index> 617 <Values>0.8</Values> 618 <Status>1</Status> 619 <Index>1</Index> 620 <Values>0.2</Values> 621 <Status>1</Status> 622 </Variables> 623 <Variables> 624 <Desc>Outlet.h</Desc> 625 <Index>0</Index> 626 <Values>-27911.4</Values> 627 <Status>0</Status> 628 <Unit>kJ/kmol</Unit> 629 </Variables> 630 <Variables> 631 <Desc>Outlet.v</Desc> 632 <Index>0</Index> 633 <Values>0</Values> 634 <Status>0</Status> 635 </Variables> 636 </Block_Properties> 637 </Base_Models> 638 <Model_File_Path>streams</Model_File_Path> 639 <Instance_Id>Outlet</Instance_Id> 640 <Model_Name>Outlet</Model_Name> 641 <T_Connection>2</T_Connection> 642 </Block_Properties> 643 </Sub_Models> 644 <Model_File_Path>streams</Model_File_Path> 645 <Instance_Id></Instance_Id> 646 <Model_Name>source</Model_Name> 647 <T_Connection>0</T_Connection> 648 <Parameters> 649 <Desc>PP</Desc> 650 <Index>0</Index> 651 <Values>PP</Values> 652 <Status>0</Status> 653 </Parameters> 654 <Parameters> 655 <Desc>NComp</Desc> 656 <Index>0</Index> 657 <Values>2</Values> 658 <Status>0</Status> 659 </Parameters> 660 <Parameters> 661 <Desc>rhoModel</Desc> 662 <Index>0</Index> 663 <Values>volume</Values> 664 <Status>0</Status> 665 </Parameters> 666 <Variables> 667 <Desc>x</Desc> 668 <Index>0</Index> 669 <Values>0.8</Values> 670 <Status>0</Status> 671 <Index>1</Index> 672 <Values>0.2</Values> 673 <Status>0</Status> 674 </Variables> 675 <Variables> 676 <Desc>y</Desc> 677 <Index>0</Index> 678 <Values>0.593741</Values> 679 <Status>0</Status> 680 <Index>1</Index> 681 <Values>0.406259</Values> 682 <Status>0</Status> 683 </Variables> 684 <Variables> 685 <Desc>hl</Desc> 686 <Index>0</Index> 687 <Values>-27911.4</Values> 688 <Status>0</Status> 689 <Unit>kJ/kmol</Unit> 690 </Variables> 691 <Variables> 692 <Desc>hv</Desc> 693 <Index>0</Index> 694 <Values>1610.68</Values> 695 <Status>0</Status> 696 <Unit>kJ/kmol</Unit> 697 </Variables> 698 <Variables> 699 <Desc>s</Desc> 700 <Index>0</Index> 701 <Values>-171.721</Values> 702 <Status>0</Status> 703 <Unit>kJ/kmol/K</Unit> 704 </Variables> 705 <Variables> 706 <Desc>sl</Desc> 707 <Index>0</Index> 708 <Values>-171.721</Values> 709 <Status>0</Status> 710 <Unit>kJ/kmol/K</Unit> 711 </Variables> 712 <Variables> 713 <Desc>sv</Desc> 714 <Index>0</Index> 715 <Values>-97.4206</Values> 716 <Status>0</Status> 717 <Unit>kJ/kmol/K</Unit> 718 </Variables> 719 <Variables> 720 <Desc>zmass</Desc> 721 <Index>0</Index> 722 <Values>0.945486</Values> 723 <Status>0</Status> 724 <Index>1</Index> 725 <Values>0.0545141</Values> 726 <Status>0</Status> 727 </Variables> 728 <Variables> 729 <Desc>Mw</Desc> 730 <Index>0</Index> 731 <Values>66.0938</Values> 732 <Status>0</Status> 733 <Unit>kg/kmol</Unit> 734 </Variables> 735 <Variables> 736 <Desc>vm</Desc> 737 <Index>0</Index> 738 <Values>7.77911e-005</Values> 739 <Status>0</Status> 740 <Unit>m^3/mol</Unit> 741 </Variables> 742 <Variables> 743 <Desc>rho</Desc> 744 <Index>0</Index> 745 <Values>849.632</Values> 746 <Status>0</Status> 747 <Unit>kg/m^3</Unit> 748 </Variables> 749 <Variables> 750 <Desc>rhom</Desc> 751 <Index>0</Index> 752 <Values>12.8549</Values> 753 <Status>0</Status> 754 <Unit>kmol/m^3</Unit> 755 </Variables> 756 <Variables> 757 <Desc>Fw</Desc> 758 <Index>0</Index> 759 <Values>33046.9</Values> 760 <Status>0</Status> 761 <Unit>kg/h</Unit> 762 </Variables> 763 <Variables> 764 <Desc>Fvol</Desc> 765 <Index>0</Index> 766 <Values>38.8955</Values> 767 <Status>0</Status> 768 <Unit>m^3/h</Unit> 769 </Variables> 770 </Block_Properties> 771 </Block> 772 <Block> 773 <Type>energy_source</Type> 774 <Id_String>energy_source_1</Id_String> 775 <Block_Name>energy_source_1</Block_Name> 776 <Image_File_Name>E:\User\Arge\PROJETOS\Alsoc\EMSO\mso\eml\icon/energy_source.png</Image_File_Name> 777 <X>523</X> 778 <Y>241</Y> 779 <Z>0</Z> 780 <Width>72.5</Width> 781 <Height>38</Height> 782 <Block_Properties> 783 <Sub_Models> 784 <Block_Properties> 785 <Base_Models> 786 <Block_Properties> 787 <Model_File_Path>streams</Model_File_Path> 788 <Instance_Id>OutletQ.</Instance_Id> 789 <Model_Name>energy_stream</Model_Name> 790 <T_Connection>2</T_Connection> 791 <Variables> 792 <Desc>OutletQ.Q</Desc> 793 <Index>0</Index> 794 <Values>0</Values> 795 <Status>1</Status> 796 <Unit>kJ/s</Unit> 797 </Variables> 798 </Block_Properties> 799 </Base_Models> 800 <Model_File_Path>streams</Model_File_Path> 801 <Instance_Id>OutletQ</Instance_Id> 802 <Model_Name>OutletQ</Model_Name> 803 <T_Connection>2</T_Connection> 804 </Block_Properties> 805 </Sub_Models> 806 <Model_File_Path>streams</Model_File_Path> 807 <Instance_Id></Instance_Id> 808 <Model_Name>energy_source</Model_Name> 809 <T_Connection>0</T_Connection> 810 </Block_Properties> 811 </Block> 812 <Line> 813 <Line_Name>line_4</Line_Name> 814 <X1>322.712</X1> 815 <Y1>110</Y1> 816 <X2>580</X2> 817 <Y2>64.9856</Y2> 818 <Block_Source>flash_1</Block_Source> 819 <Port_Source>flash_1.OutletV</Port_Source> 820 <Block_Target>simple_sink_2</Block_Target> 821 <Port_Target>simple_sink_2.Inlet</Port_Target> 822 </Line> 823 <Line> 824 <Line_Name>line_3</Line_Name> 825 <X1>321.094</X1> 826 <Y1>388</Y1> 827 <X2>587</X2> 828 <Y2>442.232</Y2> 829 <Block_Source>flash_1</Block_Source> 830 <Port_Source>flash_1.OutletL</Port_Source> 831 <Block_Target>simple_sink_1</Block_Target> 832 <Port_Target>simple_sink_1.Inlet</Port_Target> 833 </Line> 834 <Line> 835 <Line_Name>line_2</Line_Name> 836 <X1>564</X1> 837 <Y1>261.861</Y1> 838 <X2>418</X2> 839 <Y2>320.14</Y2> 840 <Block_Source>energy_source_1</Block_Source> 841 <Port_Source>energy_source_1.OutletQ</Port_Source> 842 <Block_Target>flash_1</Block_Target> 843 <Port_Target>flash_1.InletQ</Port_Target> 844 </Line> 845 <Line> 846 <Line_Name>line_1</Line_Name> 847 <X1>66</X1> 848 <Y1>260.178</Y1> 849 <X2>232</X2> 850 <Y2>260.704</Y2> 851 <Block_Source>source_1</Block_Source> 852 <Port_Source>source_1.Outlet</Port_Source> 853 <Block_Target>flash_1</Block_Target> 854 <Port_Target>flash_1.Inlet</Port_Target> 855 </Line> 599 </Sub_Models> 600 <Parameters> 601 <Desc>PP</Desc> 602 <Index>0</Index> 603 <Values>PP</Values> 604 <Status>0</Status> 605 </Parameters> 606 <Parameters> 607 <Desc>CompostionBasis</Desc> 608 <Index>0</Index> 609 <Values>Molar</Values> 610 <Status>4</Status> 611 </Parameters> 612 <Parameters> 613 <Desc>ValidPhases</Desc> 614 <Index>0</Index> 615 <Values>Vapour-Liquid</Values> 616 <Status>4</Status> 617 </Parameters> 618 <Variables> 619 <Desc>Composition</Desc> 620 <Index>0</Index> 621 <Values>0.8</Values> 622 <Status>1</Status> 623 <Index>1</Index> 624 <Values>0.2</Values> 625 <Status>1</Status> 626 </Variables> 627 <Variables> 628 <Desc>F</Desc> 629 <Index>0</Index> 630 <Values>500</Values> 631 <Status>1</Status> 632 <Unit>kmol/h</Unit> 633 </Variables> 634 <Variables> 635 <Desc>T</Desc> 636 <Index>0</Index> 637 <Values>338</Values> 638 <Status>1</Status> 639 <Unit>K</Unit> 640 </Variables> 641 <Variables> 642 <Desc>P</Desc> 643 <Index>0</Index> 644 <Values>507</Values> 645 <Status>1</Status> 646 <Unit>kPa</Unit> 647 </Variables> 648 </Block_Properties> 649 </Block> 650 <Line> 651 <Line_Name>line_4</Line_Name> 652 <X1>322.712</X1> 653 <Y1>110</Y1> 654 <X2>580</X2> 655 <Y2>64.9856</Y2> 656 <Block_Source>flash_1</Block_Source> 657 <Port_Source>OutletV</Port_Source> 658 <Block_Target>simple_sink_2</Block_Target> 659 <Port_Target>Inlet</Port_Target> 660 </Line> 661 <Line> 662 <Line_Name>line_3</Line_Name> 663 <X1>321.094</X1> 664 <Y1>388</Y1> 665 <X2>587</X2> 666 <Y2>442.232</Y2> 667 <Block_Source>flash_1</Block_Source> 668 <Port_Source>OutletL</Port_Source> 669 <Block_Target>simple_sink_1</Block_Target> 670 <Port_Target>Inlet</Port_Target> 671 </Line> 672 <Line> 673 <Line_Name>line_2</Line_Name> 674 <X1>564</X1> 675 <Y1>261.861</Y1> 676 <X2>418</X2> 677 <Y2>320.14</Y2> 678 <Block_Source>energy_source_1</Block_Source> 679 <Port_Source>OutletQ</Port_Source> 680 <Block_Target>flash_1</Block_Target> 681 <Port_Target>InletQ</Port_Target> 682 </Line> 683 <Line> 684 <Line_Name>1</Line_Name> 685 <X1>107</X1> 686 <Y1>189.768</Y1> 687 <X2>237</X2> 688 <Y2>231</Y2> 689 <Block_Source>source_2</Block_Source> 690 <Port_Source>Outlet</Port_Source> 691 <Block_Target>flash_1</Block_Target> 692 <Port_Target>Inlet</Port_Target> 693 </Line> 856 694 </Diagram> -
branches/gui/sample/processes/info_stream_diagram.pfd
r570 r578 14 14 <Time_Step>10</Time_Step> 15 15 <Time_End>100</Time_End> 16 <Time_Unit _Text>s</Time_Unit_Text>16 <Time_Unit></Time_Unit> 17 17 <Sparse_Algebra>1</Sparse_Algebra> 18 18 <Integration_Index>0</Integration_Index> … … 21 21 <NLASolver_File_Text>sundials</NLASolver_File_Text> 22 22 <DAESolver_File_Index>0</DAESolver_File_Index> 23 <DAESolver_Relative_Accuracy>1e-3</DAESolver_Relative_Accuracy> 24 <DAESolver_Absolute_Accuracy>1e-6</DAESolver_Absolute_Accuracy> 25 <DAESolver_Evt_Accuracy>1e-2</DAESolver_Evt_Accuracy> 23 26 </Options> 24 27 <Width>2000</Width> … … 27 30 <View> 28 31 <Zoom_Level>1</Zoom_Level> 29 <Show_Grid> 1</Show_Grid>30 <Snap_to_Grid> 1</Snap_to_Grid>32 <Show_Grid>0</Show_Grid> 33 <Snap_to_Grid>0</Snap_to_Grid> 31 34 <Width>925</Width> 32 <Height>5 25</Height>35 <Height>518</Height> 33 36 <X>0</X> 34 37 <Y>0</Y> … … 36 39 <View> 37 40 <Zoom_Level>1</Zoom_Level> 38 <Show_Grid> 1</Show_Grid>39 <Snap_to_Grid> 1</Snap_to_Grid>41 <Show_Grid>0</Show_Grid> 42 <Snap_to_Grid>0</Snap_to_Grid> 40 43 <Width>925</Width> 41 44 <Height>0</Height> … … 1177 1180 </Block> 1178 1181 <Block> 1179 <Type>source</Type>1180 <Id_String>source_1</Id_String>1181 <Image_File_Name>D:\Apps\repositorio\branches\gui\eml\icon/Source.png</Image_File_Name>1182 <X>185</X>1183 <Y>439</Y>1184 <Z>0</Z>1185 <Width>68</Width>1186 <Height>30</Height>1187 <Block_Properties>1188 <Model_File_Path>streams</Model_File_Path>1189 <Instance_Id>source_1</Instance_Id>1190 <Model_Name>source</Model_Name>1191 <T_Connection>0</T_Connection>1192 <Sub_Models>1193 <Block_Properties>1194 <Model_File_Path>streams</Model_File_Path>1195 <Instance_Id>Outlet</Instance_Id>1196 <Model_Name>Outlet</Model_Name>1197 <T_Connection>2</T_Connection>1198 <Base_Models>1199 <Block_Properties>1200 <Model_File_Path>streams</Model_File_Path>1201 <Instance_Id>Outlet</Instance_Id>1202 <Model_Name>stream</Model_Name>1203 <T_Connection>2</T_Connection>1204 <Parameters>1205 <Desc>NComp</Desc>1206 <Index>0</Index>1207 <Values>3</Values>1208 <Status>0</Status>1209 </Parameters>1210 <Variables>1211 <Desc>F</Desc>1212 <Index>0</Index>1213 <Values>5</Values>1214 <Status>1</Status>1215 <Unit>kmol/h</Unit>1216 </Variables>1217 <Variables>1218 <Desc>T</Desc>1219 <Index>0</Index>1220 <Values>313</Values>1221 <Status>1</Status>1222 <Unit>K</Unit>1223 </Variables>1224 <Variables>1225 <Desc>P</Desc>1226 <Index>0</Index>1227 <Values>1</Values>1228 <Status>1</Status>1229 <Unit>atm</Unit>1230 </Variables>1231 <Variables>1232 <Desc>h</Desc>1233 <Index>0</Index>1234 <Values>-13074.5</Values>1235 <Status>0</Status>1236 <Unit>kJ/kmol</Unit>1237 </Variables>1238 <Variables>1239 <Desc>v</Desc>1240 <Index>0</Index>1241 <Values>0.528908</Values>1242 <Status>0</Status>1243 </Variables>1244 <Variables>1245 <Desc>z</Desc>1246 <Index>0</Index>1247 <Values>0</Values>1248 <Status>1</Status>1249 <Index>1</Index>1250 <Values>0.5</Values>1251 <Status>1</Status>1252 <Index>2</Index>1253 <Values>0.5</Values>1254 <Status>1</Status>1255 </Variables>1256 </Block_Properties>1257 </Base_Models>1258 </Block_Properties>1259 </Sub_Models>1260 <Parameters>1261 <Desc>PP</Desc>1262 <Index>0</Index>1263 <Values>PP</Values>1264 <Status>0</Status>1265 </Parameters>1266 <Parameters>1267 <Desc>NComp</Desc>1268 <Index>0</Index>1269 <Values>3</Values>1270 <Status>0</Status>1271 </Parameters>1272 <Parameters>1273 <Desc>M</Desc>1274 <Index>0</Index>1275 <Values>18.0152</Values>1276 <Status>0</Status>1277 <Unit>kg/kmol</Unit>1278 <Index>1</Index>1279 <Values>58.123</Values>1280 <Status>0</Status>1281 <Unit>kg/kmol</Unit>1282 <Index>2</Index>1283 <Values>78.1134</Values>1284 <Status>0</Status>1285 <Unit>kg/kmol</Unit>1286 </Parameters>1287 <Parameters>1288 <Desc>rhoModel</Desc>1289 <Index>0</Index>1290 <Values>volume</Values>1291 <Status>0</Status>1292 </Parameters>1293 <Variables>1294 <Desc>hl</Desc>1295 <Index>0</Index>1296 <Values>-28967.4</Values>1297 <Status>0</Status>1298 <Unit>kJ/kmol</Unit>1299 </Variables>1300 <Variables>1301 <Desc>hv</Desc>1302 <Index>0</Index>1303 <Values>1081.08</Values>1304 <Status>0</Status>1305 <Unit>kJ/kmol</Unit>1306 </Variables>1307 <Variables>1308 <Desc>s</Desc>1309 <Index>0</Index>1310 <Values>-129.831</Values>1311 <Status>0</Status>1312 <Unit>kJ/kmol/K</Unit>1313 </Variables>1314 <Variables>1315 <Desc>sl</Desc>1316 <Index>0</Index>1317 <Values>-177.065</Values>1318 <Status>0</Status>1319 <Unit>kJ/kmol/K</Unit>1320 </Variables>1321 <Variables>1322 <Desc>sv</Desc>1323 <Index>0</Index>1324 <Values>-87.7611</Values>1325 <Status>0</Status>1326 <Unit>kJ/kmol/K</Unit>1327 </Variables>1328 <Variables>1329 <Desc>zmass</Desc>1330 <Index>0</Index>1331 <Values>0</Values>1332 <Status>0</Status>1333 <Index>1</Index>1334 <Values>0.426633</Values>1335 <Status>0</Status>1336 <Index>2</Index>1337 <Values>0.573367</Values>1338 <Status>0</Status>1339 </Variables>1340 <Variables>1341 <Desc>Mw</Desc>1342 <Index>0</Index>1343 <Values>68.1182</Values>1344 <Status>0</Status>1345 <Unit>kg/kmol</Unit>1346 </Variables>1347 <Variables>1348 <Desc>vm</Desc>1349 <Index>0</Index>1350 <Values>0.0132504</Values>1351 <Status>0</Status>1352 <Unit>m^3/mol</Unit>1353 </Variables>1354 <Variables>1355 <Desc>rho</Desc>1356 <Index>0</Index>1357 <Values>5.14085</Values>1358 <Status>0</Status>1359 <Unit>kg/m^3</Unit>1360 </Variables>1361 <Variables>1362 <Desc>rhom</Desc>1363 <Index>0</Index>1364 <Values>0.0754696</Values>1365 <Status>0</Status>1366 <Unit>kmol/m^3</Unit>1367 </Variables>1368 <Variables>1369 <Desc>Fw</Desc>1370 <Index>0</Index>1371 <Values>340.591</Values>1372 <Status>0</Status>1373 <Unit>kg/h</Unit>1374 </Variables>1375 <Variables>1376 <Desc>Fvol</Desc>1377 <Index>0</Index>1378 <Values>66.2519</Values>1379 <Status>0</Status>1380 <Unit>m^3/h</Unit>1381 </Variables>1382 <Variables>1383 <Desc>T_Cdeg</Desc>1384 <Index>0</Index>1385 <Values>39.85</Values>1386 <Status>0</Status>1387 <Unit>K</Unit>1388 </Variables>1389 </Block_Properties>1390 </Block>1391 <Block>1392 1182 <Type>info_stream</Type> 1393 1183 <Id_String>info_stream_2</Id_String> … … 2177 1967 </Block_Properties> 2178 1968 </Block> 1969 <Block> 1970 <Type>source</Type> 1971 <Id_String>source_2</Id_String> 1972 <Image_File_Name>D:\Apps\repositorio\branches\gui\eml\icon/Source.png</Image_File_Name> 1973 <X>224</X> 1974 <Y>433</Y> 1975 <Z>0</Z> 1976 <Width>68</Width> 1977 <Height>30</Height> 1978 <Block_Properties> 1979 <Model_File_Path>streams</Model_File_Path> 1980 <Instance_Id>source_2</Instance_Id> 1981 <Model_Name>source</Model_Name> 1982 <T_Connection>0</T_Connection> 1983 <Sub_Models> 1984 <Block_Properties> 1985 <Model_File_Path>streams</Model_File_Path> 1986 <Instance_Id>Outlet</Instance_Id> 1987 <Model_Name>Outlet</Model_Name> 1988 <T_Connection>2</T_Connection> 1989 <Base_Models> 1990 <Block_Properties> 1991 <Model_File_Path>streams</Model_File_Path> 1992 <Instance_Id>Outlet</Instance_Id> 1993 <Model_Name>stream</Model_Name> 1994 <T_Connection>2</T_Connection> 1995 </Block_Properties> 1996 </Base_Models> 1997 </Block_Properties> 1998 </Sub_Models> 1999 <Parameters> 2000 <Desc>PP</Desc> 2001 <Index>0</Index> 2002 <Values>PP</Values> 2003 <Status>0</Status> 2004 </Parameters> 2005 <Parameters> 2006 <Desc>CompostionBasis</Desc> 2007 <Index>0</Index> 2008 <Values>Molar</Values> 2009 <Status>4</Status> 2010 </Parameters> 2011 <Parameters> 2012 <Desc>ValidPhases</Desc> 2013 <Index>0</Index> 2014 <Values>Vapour-Liquid</Values> 2015 <Status>4</Status> 2016 </Parameters> 2017 <Variables> 2018 <Desc>Composition</Desc> 2019 <Index>0</Index> 2020 <Values>0</Values> 2021 <Status>1</Status> 2022 <Index>1</Index> 2023 <Values>0.5</Values> 2024 <Status>1</Status> 2025 <Index>2</Index> 2026 <Values>0.5</Values> 2027 <Status>1</Status> 2028 </Variables> 2029 <Variables> 2030 <Desc>F</Desc> 2031 <Index>0</Index> 2032 <Values>5</Values> 2033 <Status>1</Status> 2034 <Unit>kmol/h</Unit> 2035 </Variables> 2036 <Variables> 2037 <Desc>T</Desc> 2038 <Index>0</Index> 2039 <Values>313</Values> 2040 <Status>1</Status> 2041 <Unit>K</Unit> 2042 </Variables> 2043 <Variables> 2044 <Desc>P</Desc> 2045 <Index>0</Index> 2046 <Values>1</Values> 2047 <Status>1</Status> 2048 <Unit>atm</Unit> 2049 </Variables> 2050 </Block_Properties> 2051 </Block> 2179 2052 <Line> 2180 2053 <Line_Name>line_1</Line_Name> … … 2197 2070 <Port_Source>Outlet</Port_Source> 2198 2071 <Block_Target>Heatex_NTU_1</Block_Target> 2199 <Port_Target>InletCold</Port_Target>2200 </Line>2201 <Line>2202 <Line_Name>3</Line_Name>2203 <X1>253</X1>2204 <Y1>454.768</Y1>2205 <X2>589.036</X2>2206 <Y2>414</Y2>2207 <Block_Source>source_1</Block_Source>2208 <Port_Source>Outlet</Port_Source>2209 <Block_Target>Heatex_LMTD_1</Block_Target>2210 2072 <Port_Target>InletCold</Port_Target> 2211 2073 </Line> … … 2276 2138 <Port_Target>Inlet</Port_Target> 2277 2139 </Line> 2140 <Line> 2141 <Line_Name>3</Line_Name> 2142 <X1>292</X1> 2143 <Y1>448.768</Y1> 2144 <X2>592</X2> 2145 <Y2>414</Y2> 2146 <Block_Source>source_2</Block_Source> 2147 <Port_Source>Outlet</Port_Source> 2148 <Block_Target>Heatex_LMTD_1</Block_Target> 2149 <Port_Target>InletCold</Port_Target> 2150 </Line> 2278 2151 </Diagram> -
branches/gui/sample/processes/sample_source_testing.pfd
r577 r578 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> 1260</Width>37 <Height>5 73</Height>34 <Show_Grid>0</Show_Grid> 35 <Snap_to_Grid>0</Snap_to_Grid> 36 <Width>925</Width> 37 <Height>518</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> 1260</Width>43 <Show_Grid>0</Show_Grid> 44 <Snap_to_Grid>0</Snap_to_Grid> 45 <Width>925</Width> 46 46 <Height>0</Height> 47 47 <X>0</X> … … 240 240 </Block> 241 241 <Block> 242 <Type>source _testing</Type>243 <Id_String>source_ testing_1</Id_String>242 <Type>source</Type> 243 <Id_String>source_1</Id_String> 244 244 <Image_File_Name>D:\Apps\repositorio\branches\gui\eml\icon/Source.png</Image_File_Name> 245 <X> 54</X>246 <Y> 142</Y>245 <X>74</X> 246 <Y>61</Y> 247 247 <Z>0</Z> 248 248 <Width>68</Width> … … 250 250 <Block_Properties> 251 251 <Model_File_Path>streams</Model_File_Path> 252 <Instance_Id>source_ testing_1</Instance_Id>253 <Model_Name>source _testing</Model_Name>252 <Instance_Id>source_1</Instance_Id> 253 <Model_Name>source</Model_Name> 254 254 <T_Connection>0</T_Connection> 255 255 <Sub_Models> … … 265 265 <Model_Name>stream</Model_Name> 266 266 <T_Connection>2</T_Connection> 267 <Parameters>268 <Desc>NComp</Desc>269 <Index>0</Index>270 <Values>3</Values>271 <Status>0</Status>272 </Parameters>273 <Variables>274 <Desc>F</Desc>275 <Index>0</Index>276 <Values>35630.2</Values>277 <Status>0</Status>278 <Unit>kmol/h</Unit>279 </Variables>280 <Variables>281 <Desc>T</Desc>282 <Index>0</Index>283 <Values>338</Values>284 <Status>0</Status>285 <Unit>K</Unit>286 </Variables>287 <Variables>288 <Desc>P</Desc>289 <Index>0</Index>290 <Values>1</Values>291 <Status>0</Status>292 <Unit>atm</Unit>293 </Variables>294 <Variables>295 <Desc>h</Desc>296 <Index>0</Index>297 <Values>-22818.8</Values>298 <Status>0</Status>299 <Unit>kJ/kmol</Unit>300 </Variables>301 <Variables>302 <Desc>v</Desc>303 <Index>0</Index>304 <Values>0</Values>305 <Status>0</Status>306 </Variables>307 <Variables>308 <Desc>z</Desc>309 <Index>0</Index>310 <Values>0.3</Values>311 <Status>0</Status>312 <Index>1</Index>313 <Values>0.4</Values>314 <Status>0</Status>315 <Index>2</Index>316 <Values>0.3</Values>317 <Status>0</Status>318 </Variables>319 267 </Block_Properties> 320 268 </Base_Models> … … 328 276 </Parameters> 329 277 <Parameters> 330 <Desc>NComp</Desc>331 <Index>0</Index>332 <Values>3</Values>333 <Status>0</Status>334 </Parameters>335 <Parameters>336 <Desc>M</Desc>337 <Index>0</Index>338 <Values>58.123</Values>339 <Status>0</Status>340 <Unit>kg/kmol</Unit>341 <Index>1</Index>342 <Values>78.1134</Values>343 <Status>0</Status>344 <Unit>kg/kmol</Unit>345 <Index>2</Index>346 <Values>114.23</Values>347 <Status>0</Status>348 <Unit>kg/kmol</Unit>349 </Parameters>350 <Parameters>351 <Desc>rhoModel</Desc>352 <Index>0</Index>353 <Values>correlation</Values>354 <Status>4</Status>355 </Parameters>356 <Parameters>357 278 <Desc>CompostionBasis</Desc> 358 279 <Index>0</Index> … … 372 293 <Status>1</Status> 373 294 <Index>1</Index> 295 <Values>0.3</Values> 296 <Status>1</Status> 297 <Index>2</Index> 374 298 <Values>0.4</Values> 375 299 <Status>1</Status> 376 <Index>2</Index>377 <Values>0.3</Values>378 <Status>1</Status>379 </Variables>380 <Variables>381 <Desc>F</Desc>382 <Index>0</Index>383 <Values>35630.2</Values>384 <Status>0</Status>385 <Unit>kmol/h</Unit>386 300 </Variables> 387 301 <Variables> 388 302 <Desc>Fw</Desc> 389 303 <Index>0</Index> 390 <Values>2 .95557e+006</Values>391 <Status> 0</Status>304 <Values>20</Values> 305 <Status>1</Status> 392 306 <Unit>kg/h</Unit> 393 307 </Variables> 394 308 <Variables> 395 <Desc>Fvol</Desc> 396 <Index>0</Index> 397 <Values>4924.66</Values> 398 <Status>1</Status> 399 <Unit>m^3/h</Unit> 400 </Variables> 401 <Variables> 402 <Desc>T</Desc> 403 <Index>0</Index> 404 <Values>338</Values> 405 <Status>0</Status> 309 <Desc>T_Cdeg</Desc> 310 <Index>0</Index> 311 <Values>25</Values> 312 <Status>1</Status> 406 313 <Unit>K</Unit> 407 314 </Variables> 408 315 <Variables> 409 <Desc>T_Cdeg</Desc>410 <Index>0</Index>411 <Values>64.85</Values>412 <Status>1</Status>413 <Unit>K</Unit>414 </Variables>415 <Variables>416 316 <Desc>P</Desc> 417 317 <Index>0</Index> … … 419 319 <Status>1</Status> 420 320 <Unit>atm</Unit> 421 </Variables>422 <Variables>423 <Desc>Mw</Desc>424 <Index>0</Index>425 <Values>82.9513</Values>426 <Status>0</Status>427 <Unit>kg/kmol</Unit>428 </Variables>429 <Variables>430 <Desc>vm</Desc>431 <Index>0</Index>432 <Values>0.000138216</Values>433 <Status>0</Status>434 <Unit>m^3/mol</Unit>435 </Variables>436 <Variables>437 <Desc>rho</Desc>438 <Index>0</Index>439 <Values>600.156</Values>440 <Status>0</Status>441 <Unit>kg/m^3</Unit>442 </Variables>443 <Variables>444 <Desc>rhom</Desc>445 <Index>0</Index>446 <Values>7.23505</Values>447 <Status>0</Status>448 <Unit>kmol/m^3</Unit>449 </Variables>450 <Variables>451 <Desc>zmass</Desc>452 <Index>0</Index>453 <Values>0.210207</Values>454 <Status>0</Status>455 <Index>1</Index>456 <Values>0.376671</Values>457 <Status>0</Status>458 <Index>2</Index>459 <Values>0.413122</Values>460 <Status>0</Status>461 321 </Variables> 462 322 </Block_Properties> … … 464 324 <Line> 465 325 <Line_Name>1</Line_Name> 466 <X1>1 22</X1>467 <Y1> 157.768</Y1>326 <X1>142</X1> 327 <Y1>76.768</Y1> 468 328 <X2>466</X2> 469 <Y2>34 6</Y2>470 <Block_Source>source_ testing_1</Block_Source>329 <Y2>348</Y2> 330 <Block_Source>source_1</Block_Source> 471 331 <Port_Source>Outlet</Port_Source> 472 332 <Block_Target>Product</Block_Target> -
branches/gui/sample/reactors/sample_cstr.mso
r574 r578 47 47 Reac.stoic = [-1, 0, -1, 1]; 48 48 49 s1.ValidPhases = "Vapour-Liquid"; 50 s1.CompostionBasis = "Molar"; 51 49 52 EQUATIONS 50 53 … … 54 57 55 58 SPECIFY 56 s1. Outlet.F = 52126 * 'mol/h';57 s1. Outlet.P = 1 * 'atm';58 s1. Outlet.T = 534.67* 'degR';59 s1. Outlet.z= [0.0468, 0.0783, 0.8749, 0];59 s1.F = 52126 * 'mol/h'; 60 s1.P = 1 * 'atm'; 61 s1.T = 534.67* 'degR'; 62 s1.Composition = [0.0468, 0.0783, 0.8749, 0]; 60 63 61 64 Reac.Vr = 300 * 'gal'; -
branches/gui/sample/reactors/sample_pfr.mso
r574 r578 55 55 NComp = PP.NumberOfComponents; 56 56 57 s1.ValidPhases = "Vapour-Liquid"; 58 s1.CompostionBasis = "Molar"; 59 57 60 Reac.NDisc = 10; 58 61 Reac.Across = 0.7 * 'in^2'; … … 79 82 80 83 SPECIFY 81 s1. Outlet.F = 138/1000 * 'kmol/h';82 s1. Outlet.T = 1035 * 'K';83 s1. Outlet.P = 1.6 * 'atm';84 s1. Outlet.z= [1, 0, 0];84 s1.F = 138/1000 * 'kmol/h'; 85 s1.T = 1035 * 'K'; 86 s1.P = 1.6 * 'atm'; 87 s1.Composition = [1, 0, 0]; 85 88 86 89 Reac.q = 0 * 'J/s'; -
branches/gui/sample/reconciliation/flash.dat
r548 r578 1 MEASURE s1. Outlet.F fl.OutletL.F fl.OutletV.F1 MEASURE s1.F fl.OutletL.F fl.OutletV.F 2 2 VARIANCE 1.0 1.0 1.0 3 3 DATA 498.3 344.0 150.0 -
branches/gui/sample/reconciliation/flash_rec.mso
r548 r578 28 28 29 29 SPECIFY 30 s1. Outlet.F = 496.3 * 'kmol/h';31 s1. Outlet.T = 338 * 'K';32 s1. Outlet.P = 507.1 * 'kPa';33 s1. Outlet.z= [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283];30 s1.F = 496.3 * 'kmol/h'; 31 s1.T = 338 * 'K'; 32 s1.P = 507.1 * 'kPa'; 33 s1.Composition = [0.2379,0.3082,0.09959,0.1373,0.08872,0.1283]; 34 34 35 35 fl.OutletL.P = 2.5 * 'atm'; … … 45 45 46 46 RECONCILE 47 s1. Outlet.F; fl.OutletL.F; fl.OutletV.F;47 s1.F; fl.OutletL.F; fl.OutletV.F; 48 48 49 49 FREE 50 s1. Outlet.F;50 s1.F; 51 51 52 52 EXPERIMENTS 53 53 # FILE WEIGTH 54 54 "flash.dat" 1; 55 55 56 56 57 OPTIONS
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