Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe.conf.json loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo", uses=false) Using package ThermoSysPro with version 4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo) Running command: translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe") translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe") Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8637/0.8637, allocations: 150.9 MB / 167.2 MB, free: 14.5 MB / 142.1 MB Notification: Performance of FrontEnd - loaded program: time 0.0003683/0.0003683, allocations: 16.02 kB / 237.8 MB, free: 1.926 MB / 190.1 MB Notification: Performance of FrontEnd - Absyn->SCode: time 0.05205/0.05243, allocations: 31.34 MB / 269.1 MB, free: 7.148 MB / 222.1 MB Notification: Automatically loaded package Complex 4.0.0 due to uses annotation from Modelica. Notification: Automatically loaded package ModelicaServices 4.0.0 due to uses annotation from Modelica. Notification: Automatically loaded package Modelica 4.0.0 due to usage. Notification: Performance of NFInst.instantiate(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe): time 1.643/1.695, allocations: 299.9 MB / 0.5557 GB, free: 8.156 MB / 446.1 MB Notification: Performance of NFInst.instExpressions: time 0.5189/2.214, allocations: 194.1 MB / 0.7452 GB, free: 14.82 MB / 0.6075 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001259/2.215, allocations: 33.25 kB / 0.7453 GB, free: 14.82 MB / 0.6075 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicTwoPhaseFlowPipe.mo:233:3-234:54:writable] Warning: Connector C1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicTwoPhaseFlowPipe.mo:237:3-238:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourceP.mo:58:3-59:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SinkP.mo:46:3-47:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicTwoPhaseFlowPipe.mo:233:3-234:54:writable] Warning: Connector C1 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicTwoPhaseFlowPipe.mo:237:3-238:52:writable] Warning: Connector C2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourceP.mo:58:3-59:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SinkP.mo:46:3-47:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0). Notification: Performance of NFTyping.typeComponents: time 0.001385/2.217, allocations: 451.3 kB / 0.7457 GB, free: 14.82 MB / 0.6075 GB Notification: Performance of NFTyping.typeBindings: time 0.002578/2.219, allocations: 1.24 MB / 0.7469 GB, free: 14.8 MB / 0.6075 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:783:9-783:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:850:9-850:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteam/IF97_packages.mo:1088:9-1088:27:writable] Warning: cv was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh1satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph.mo:69:3-69:60:writable] Warning: dh2satp was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du1satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/WaterSteamSimple/prop4_Ph_der.mo:167:3-170:49:writable] Warning: du2satp_der was used before it was defined (given a value). Additional such uses may exist for the variable, but some messages were suppressed. Notification: Performance of NFTyping.typeClassSections: time 0.03316/2.252, allocations: 13.18 MB / 0.7598 GB, free: 13.95 MB / 0.6075 GB Notification: Performance of NFFlatten.flatten: time 0.01524/2.268, allocations: 20.8 MB / 0.7801 GB, free: 9.512 MB / 0.6075 GB Notification: Performance of NFFlatten.resolveConnections: time 0.009507/2.277, allocations: 6.809 MB / 0.7867 GB, free: 6.754 MB / 0.6075 GB Notification: Performance of NFEvalConstants.evaluate: time 0.01062/2.288, allocations: 6.689 MB / 0.7933 GB, free: 4.328 MB / 0.6075 GB Notification: Performance of NFSimplifyModel.simplify: time 0.01753/2.305, allocations: 7.722 MB / 0.8008 GB, free: 256 kB / 0.6075 GB Notification: Performance of NFPackage.collectConstants: time 0.005476/2.311, allocations: 1.248 MB / 0.802 GB, free: 15.75 MB / 0.6231 GB Notification: Performance of NFFlatten.collectFunctions: time 0.04309/2.354, allocations: 22.27 MB / 0.8238 GB, free: 9.715 MB / 0.6387 GB Notification: Performance of NFScalarize.scalarize: time 0.007617/2.362, allocations: 4.949 MB / 0.8286 GB, free: 4.871 MB / 0.6387 GB Notification: Performance of NFVerifyModel.verify: time 0.01385/2.376, allocations: 6.305 MB / 0.8348 GB, free: 14.65 MB / 0.6544 GB Notification: Performance of NFConvertDAE.convert: time 0.04744/2.423, allocations: 25.55 MB / 0.8597 GB, free: 6.168 MB / 0.67 GB Notification: Performance of FrontEnd - DAE generated: time 9.358e-06/2.423, allocations: 0 / 0.8597 GB, free: 6.168 MB / 0.67 GB Notification: Performance of FrontEnd: time 2.033e-06/2.423, allocations: 3.938 kB / 0.8597 GB, free: 6.164 MB / 0.67 GB Notification: Performance of Transformations before backend: time 0.0004575/2.424, allocations: 0 / 0.8597 GB, free: 6.164 MB / 0.67 GB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 2967 * Number of variables: 2967 Notification: Performance of Generate backend data structure: time 0.06948/2.493, allocations: 16.36 MB / 0.8757 GB, free: 5.727 MB / 0.6856 GB Notification: Performance of prepare preOptimizeDAE: time 6.898e-05/2.493, allocations: 12.02 kB / 0.8757 GB, free: 5.715 MB / 0.6856 GB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.005629/2.499, allocations: 1.047 MB / 0.8767 GB, free: 4.656 MB / 0.6856 GB Notification: Performance of preOpt evaluateParameters (simulation): time 0.01139/2.51, allocations: 4.138 MB / 0.8808 GB, free: 496 kB / 0.6856 GB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.006444/2.517, allocations: 4.363 MB / 0.885 GB, free: 11.47 MB / 0.7012 GB Notification: Performance of preOpt expandDerOperator (simulation): time 0.005/2.522, allocations: 0.7828 MB / 0.8858 GB, free: 10.69 MB / 0.7012 GB Notification: Performance of preOpt clockPartitioning (simulation): time 0.06062/2.582, allocations: 21.51 MB / 0.9068 GB, free: 4.891 MB / 0.7169 GB Notification: Performance of preOpt findStateOrder (simulation): time 0.000396/2.583, allocations: 11.88 kB / 0.9068 GB, free: 4.879 MB / 0.7169 GB Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.004467/2.587, allocations: 324 kB / 0.9071 GB, free: 4.562 MB / 0.7169 GB Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0003254/2.588, allocations: 315.8 kB / 0.9074 GB, free: 4.254 MB / 0.7169 GB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.08156/2.669, allocations: 30.69 MB / 0.9374 GB, free: 5.531 MB / 0.7481 GB Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.8126/3.482, allocations: 105.1 MB / 1.04 GB, free: 179 MB / 0.8263 GB Notification: Performance of preOpt comSubExp (simulation): time 0.05468/3.537, allocations: 22.02 MB / 1.062 GB, free: 177.7 MB / 0.8263 GB Notification: Performance of preOpt resolveLoops (simulation): time 0.05278/3.589, allocations: 16.24 MB / 1.077 GB, free: 177.6 MB / 0.8263 GB Notification: Performance of preOpt evalFunc (simulation): time 0.1571/3.747, allocations: 84.47 MB / 1.16 GB, free: 108.2 MB / 0.8263 GB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002055/3.747, allocations: 164.7 kB / 1.16 GB, free: 108.1 MB / 0.8263 GB Notification: Performance of pre-optimization done (n=2236): time 1.477e-05/3.747, allocations: 4 kB / 1.16 GB, free: 108.1 MB / 0.8263 GB Notification: Performance of matching and sorting (n=2246): time 0.2201/3.967, allocations: 78.19 MB / 1.236 GB, free: 29.95 MB / 0.8263 GB Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001205/3.967, allocations: 211.2 kB / 1.237 GB, free: 29.71 MB / 0.8263 GB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.002533/3.97, allocations: 2.104 MB / 1.239 GB, free: 27.57 MB / 0.8263 GB Notification: Performance of collectPreVariables (initialization): time 0.004202/3.974, allocations: 233.7 kB / 1.239 GB, free: 27.34 MB / 0.8263 GB [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicTwoPhaseFlowPipe.mo:15:3-16:73:writable] Warning: The parameter dynamicTwoPhaseFlowPipe1.dpfCorr has fixed = false and a binding equation dynamicTwoPhaseFlowPipe1.dpfCorr = 1.0, which is probably redundant. Setting fixed = false usually means there is an additional initial equation to determine the parameter value. The binding was ignored by old Modelica tools, but this is not according to the Modelica specification. Please remove the parameter binding, or bind the parameter to another parameter with fixed = false and no binding. Notification: Performance of collectInitialEqns (initialization): time 0.0009483/3.975, allocations: 1.546 MB / 1.24 GB, free: 25.79 MB / 0.8263 GB Notification: Performance of collectInitialBindings (initialization): time 0.008837/3.984, allocations: 7.413 MB / 1.248 GB, free: 18.44 MB / 0.8263 GB Notification: Performance of simplifyInitialFunctions (initialization): time 0.01343/3.997, allocations: 2.965 MB / 1.251 GB, free: 15.46 MB / 0.8263 GB Notification: Performance of setup shared object (initialization): time 4.216e-05/3.997, allocations: 309 kB / 1.251 GB, free: 15.16 MB / 0.8263 GB Notification: Performance of preBalanceInitialSystem (initialization): time 0.03299/4.03, allocations: 14.28 MB / 1.265 GB, free: 0.8633 MB / 0.8263 GB Notification: Performance of partitionIndependentBlocks (initialization): time 0.03918/4.069, allocations: 16.38 MB / 1.281 GB, free: 16 MB / 0.8575 GB Notification: It was not possible to check the given initialization system for consistency symbolically, because the relevant equations are part of an algebraic loop. This is not supported yet. Notification: Performance of analyzeInitialSystem (initialization): time 0.5554/4.625, allocations: 98.06 MB / 1.377 GB, free: 464 MB / 0.8888 GB Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.683e-05/4.625, allocations: 14.31 kB / 1.377 GB, free: 464 MB / 0.8888 GB Notification: Performance of matching and sorting (n=2462) (initialization): time 0.1004/4.725, allocations: 40.02 MB / 1.416 GB, free: 434.4 MB / 0.8888 GB Notification: Performance of prepare postOptimizeDAE: time 5.323e-05/4.725, allocations: 28.25 kB / 1.416 GB, free: 434.4 MB / 0.8888 GB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0001819/4.726, allocations: 79.97 kB / 1.416 GB, free: 434.3 MB / 0.8888 GB Notification: Performance of postOpt tearingSystem (initialization): time 0.09076/4.816, allocations: 37.67 MB / 1.453 GB, free: 396.6 MB / 0.8888 GB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.02154/4.838, allocations: 3.637 MB / 1.456 GB, free: 393 MB / 0.8888 GB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.05093/4.889, allocations: 40.68 MB / 1.496 GB, free: 350.9 MB / 0.8888 GB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01955/4.909, allocations: 2.666 MB / 1.498 GB, free: 348.3 MB / 0.8888 GB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.003911/4.912, allocations: 0.6594 MB / 1.499 GB, free: 347.6 MB / 0.8888 GB Warning: The initial conditions are over specified. The following 11 initial equations are redundant, so they are removed from the initialization system: $DER.dynamicTwoPhaseFlowPipe1.Q[1] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[1] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[2] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[3] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[4] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[5] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[6] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[7] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[8] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[10] = 0.0 $DER.dynamicTwoPhaseFlowPipe.Q[11] = 0.0. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 165 * Number of states: 0 () * Number of discrete variables: 12 (sourceP1.C.ftype,dynamicTwoPhaseFlowPipe1.fluid,sinkP1.fluid,sourceP1.fluid1,sourceP.C.ftype,dynamicTwoPhaseFlowPipe.fluid,sinkP.fluid,sourceP.fluid1,dynamicTwoPhaseFlowPipe1.C1.diff_on_2,dynamicTwoPhaseFlowPipe1.C2.diff_on_1,dynamicTwoPhaseFlowPipe.C1.diff_on_2,dynamicTwoPhaseFlowPipe.C2.diff_on_1) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (933): * Single equations (assignments): 885 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 36 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 12 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 10 systems {(1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%), (1,2,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(20,211), (23,297)} Notification: Performance of prepare postOptimizeDAE: time 0.009178/4.922, allocations: 2.622 MB / 1.502 GB, free: 345.1 MB / 0.8888 GB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.003751/4.925, allocations: 0.7943 MB / 1.502 GB, free: 344.3 MB / 0.8888 GB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1149/5.04, allocations: 47.08 MB / 1.548 GB, free: 297.1 MB / 0.8888 GB Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0004394/5.041, allocations: 63.75 kB / 1.548 GB, free: 297.1 MB / 0.8888 GB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.0002074/5.041, allocations: 47.97 kB / 1.548 GB, free: 297 MB / 0.8888 GB Notification: Performance of postOpt removeConstants (simulation): time 0.01181/5.053, allocations: 3.456 MB / 1.552 GB, free: 293.5 MB / 0.8888 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.004218/5.057, allocations: 259.8 kB / 1.552 GB, free: 293.3 MB / 0.8888 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.01741/5.074, allocations: 2.212 MB / 1.554 GB, free: 291.1 MB / 0.8888 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.00487/5.079, allocations: 1.118 MB / 1.555 GB, free: 289.9 MB / 0.8888 GB [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (14): (dynamicTwoPhaseFlowPipe.lsat2[11], dynamicTwoPhaseFlowPipe.vsat2[11]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[11] + sinkP.P0), dynamicTwoPhaseFlowPipe.fluid) Variables: 1: dynamicTwoPhaseFlowPipe.vsat2[11].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 2: dynamicTwoPhaseFlowPipe.vsat2[11].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 3: dynamicTwoPhaseFlowPipe.vsat2[11].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 4: dynamicTwoPhaseFlowPipe.lsat2[11].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 5: dynamicTwoPhaseFlowPipe.lsat2[11].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 6: dynamicTwoPhaseFlowPipe.h[11]:VARIABLE(start = 256076.18568728055 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 7: dynamicTwoPhaseFlowPipe.pro2[11].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 8: dynamicTwoPhaseFlowPipe.pro2[11].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 9: dynamicTwoPhaseFlowPipe.pro2[11].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 10: $cse31.x:VARIABLE(protected = true ) type: Real unreplaceable 11: dynamicTwoPhaseFlowPipe.pro2[11].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 12: dynamicTwoPhaseFlowPipe.pro2[11].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 13: dynamicTwoPhaseFlowPipe.pro2[11].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 14: dynamicTwoPhaseFlowPipe.pro2[11].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation: 1/1 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[1] * dynamicTwoPhaseFlowPipe.Q[1] + heatSource.W0[1] + dynamicTwoPhaseFlowPipe.J[1] - dynamicTwoPhaseFlowPipe.hb[2] * dynamicTwoPhaseFlowPipe.Q[2] 2/2 (1): dynamicTwoPhaseFlowPipe.J[1] = dynamicTwoPhaseFlowPipe.Je[1] + dynamicTwoPhaseFlowPipe.Js[1] 3/3 (1): dynamicTwoPhaseFlowPipe.Je[1] = if sourceP.diffusion then dynamicTwoPhaseFlowPipe.re[1] * dynamicTwoPhaseFlowPipe.gamma_e[1] * (dynamicTwoPhaseFlowPipe.h[1] - dynamicTwoPhaseFlowPipe.h[2]) else 0.0 4/4 (1): dynamicTwoPhaseFlowPipe.re[1] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[1] * dynamicTwoPhaseFlowPipe.diff_res_e[1]) ^ 2.0) 5/5 (1): dynamicTwoPhaseFlowPipe.diff_res_e[1] = dynamicTwoPhaseFlowPipe.rho2[1] * dynamicTwoPhaseFlowPipe.cpl2[1] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[1] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[1]) 6/6 (1): dynamicTwoPhaseFlowPipe.kl2[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[1], dynamicTwoPhaseFlowPipe.T2[1], 0.5 * (sourceP.P0 + dynamicTwoPhaseFlowPipe.P[2]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 7/7 (1): dynamicTwoPhaseFlowPipe.mul2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[1], dynamicTwoPhaseFlowPipe.T2[1], dynamicTwoPhaseFlowPipe.fluid) 8/8 (1): dynamicTwoPhaseFlowPipe.Rel2[1] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[1] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[1])) 9/9 (1): dynamicTwoPhaseFlowPipe.lambdal[1] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[1] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[1] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 10/10 (1): dynamicTwoPhaseFlowPipe.filo[1] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[1] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[1] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[1] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[1] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[1]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[1]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[1] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[1] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[1]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[1])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[1] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[1] * dynamicTwoPhaseFlowPipe.lambdav[1] / (dynamicTwoPhaseFlowPipe.lambdal[1] * dynamicTwoPhaseFlowPipe.rhov2[1]) 11/11 (1): dynamicTwoPhaseFlowPipe.khi[1] = dynamicTwoPhaseFlowPipe.filo[1] * dynamicTwoPhaseFlowPipe.lambdal[1] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 12/12 (1): dynamicTwoPhaseFlowPipe.dpf[1] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[1] * dynamicTwoPhaseFlowPipe.Q[1] * abs(dynamicTwoPhaseFlowPipe.Q[1]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[1]) 13/13 (1): $DER.dynamicTwoPhaseFlowPipe.Q[1] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = sourceP.P0 + (-dynamicTwoPhaseFlowPipe.dpf[1]) - dynamicTwoPhaseFlowPipe.P[2] - dynamicTwoPhaseFlowPipe.dpg[1] 14/14 (1): $DER.dynamicTwoPhaseFlowPipe.Q[1] = der(dynamicTwoPhaseFlowPipe.Q[2]) 15/15 (1): $DER.dynamicTwoPhaseFlowPipe.Q[11] = der(dynamicTwoPhaseFlowPipe.Q[2]) 16/16 (1): $DER.dynamicTwoPhaseFlowPipe.Q[11] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[11] + (-dynamicTwoPhaseFlowPipe.dpf[11]) - sinkP.P0 - dynamicTwoPhaseFlowPipe.dpg[11] 17/17 (1): dynamicTwoPhaseFlowPipe.dpg[11] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[11] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 18/18 (1): dynamicTwoPhaseFlowPipe.rhov2[11] = if noEvent(sinkP.P0 > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[11] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[11] else min(dynamicTwoPhaseFlowPipe.rho2[11], dynamicTwoPhaseFlowPipe.vsat2[11].rho) 19/19 (1): dynamicTwoPhaseFlowPipe.muv2[11] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[11], dynamicTwoPhaseFlowPipe.T2[11], dynamicTwoPhaseFlowPipe.fluid) 20/20 (1): dynamicTwoPhaseFlowPipe.Rev2[11] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[11] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[11])) 21/21 (1): dynamicTwoPhaseFlowPipe.lambdav[11] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[11] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[11] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 22/22 (1): dynamicTwoPhaseFlowPipe.filo[11] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[11] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[11] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[11] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[11] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[11]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[11]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[11] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[11] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[11]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[11])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[11] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[11] * dynamicTwoPhaseFlowPipe.lambdav[11] / (dynamicTwoPhaseFlowPipe.lambdal[11] * dynamicTwoPhaseFlowPipe.rhov2[11]) 23/23 (1): dynamicTwoPhaseFlowPipe.khi[11] = dynamicTwoPhaseFlowPipe.filo[11] * dynamicTwoPhaseFlowPipe.lambdal[11] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 24/24 (1): dynamicTwoPhaseFlowPipe.dpf[11] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[11] * dynamicTwoPhaseFlowPipe.Q[11] * abs(dynamicTwoPhaseFlowPipe.Q[11]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[11]) 25/25 (1): dynamicTwoPhaseFlowPipe.rhol2[11] = if noEvent(sinkP.P0 > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[11] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[11] else max(dynamicTwoPhaseFlowPipe.rho2[11], dynamicTwoPhaseFlowPipe.lsat2[11].rho) 26/26 (1): $cse20 = min(dynamicTwoPhaseFlowPipe.P[11], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 27/27 (1): dynamicTwoPhaseFlowPipe.Pb[11] = max($cse20, dynamicTwoPhaseFlowPipe.ptriple) 28/28 (1): $cse18 = min(dynamicTwoPhaseFlowPipe.P[10], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 29/29 (1): dynamicTwoPhaseFlowPipe.Pb[10] = max($cse18, dynamicTwoPhaseFlowPipe.ptriple) 30/30 (1): dynamicTwoPhaseFlowPipe.filo[10] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[10] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[10] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[10] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[10] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[10]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[10]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[10] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[10] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[10]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[10])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[10] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[10] * dynamicTwoPhaseFlowPipe.lambdav[10] / (dynamicTwoPhaseFlowPipe.lambdal[10] * dynamicTwoPhaseFlowPipe.rhov2[10]) 31/31 (1): dynamicTwoPhaseFlowPipe.khi[10] = dynamicTwoPhaseFlowPipe.filo[10] * dynamicTwoPhaseFlowPipe.lambdal[10] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 32/32 (1): dynamicTwoPhaseFlowPipe.lambdal[10] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[10] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[10] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 33/33 (1): dynamicTwoPhaseFlowPipe.Rel2[10] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[10] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[10])) 34/34 (1): dynamicTwoPhaseFlowPipe.mul2[10] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[10], dynamicTwoPhaseFlowPipe.T2[10], dynamicTwoPhaseFlowPipe.fluid) 35/35 (1): dynamicTwoPhaseFlowPipe.kl2[10] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[10], dynamicTwoPhaseFlowPipe.T2[10], 0.5 * (dynamicTwoPhaseFlowPipe.P[10] + dynamicTwoPhaseFlowPipe.P[11]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 36/36 (1): dynamicTwoPhaseFlowPipe.diff_res_e[10] = dynamicTwoPhaseFlowPipe.rho2[10] * dynamicTwoPhaseFlowPipe.cpl2[10] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[10] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[10]) 37/37 (1): dynamicTwoPhaseFlowPipe.re[10] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[10] * dynamicTwoPhaseFlowPipe.diff_res_e[10]) ^ 2.0) 38/38 (1): dynamicTwoPhaseFlowPipe.Je[10] = dynamicTwoPhaseFlowPipe.re[10] * dynamicTwoPhaseFlowPipe.gamma_e[10] * (dynamicTwoPhaseFlowPipe.h[10] - dynamicTwoPhaseFlowPipe.h[11]) 39/39 (1): dynamicTwoPhaseFlowPipe.J[10] = dynamicTwoPhaseFlowPipe.Je[10] + dynamicTwoPhaseFlowPipe.Js[10] 40/40 (1): dynamicTwoPhaseFlowPipe.Js[10] = if sinkP.diffusion then dynamicTwoPhaseFlowPipe.rs[10] * dynamicTwoPhaseFlowPipe.gamma_s[10] * (dynamicTwoPhaseFlowPipe.h[12] - dynamicTwoPhaseFlowPipe.h[11]) else 0.0 41/41 (1): dynamicTwoPhaseFlowPipe.rs[10] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[11] * dynamicTwoPhaseFlowPipe.diff_res_s[10]) ^ 2.0) 42/42 (1): dynamicTwoPhaseFlowPipe.diff_res_s[10] = dynamicTwoPhaseFlowPipe.rho2[11] * dynamicTwoPhaseFlowPipe.cpl2[11] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[11] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[11]) 43/43 (1): dynamicTwoPhaseFlowPipe.mul2[11] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[11], dynamicTwoPhaseFlowPipe.T2[11], dynamicTwoPhaseFlowPipe.fluid) 44/44 (1): dynamicTwoPhaseFlowPipe.Rel2[11] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[11] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[11])) 45/45 (1): dynamicTwoPhaseFlowPipe.lambdal[11] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[11] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[11] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 46/46 (1): dynamicTwoPhaseFlowPipe.kl2[11] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[11], dynamicTwoPhaseFlowPipe.T2[11], 0.5 * (dynamicTwoPhaseFlowPipe.P[11] + sinkP.P0), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 47/47 (1): dynamicTwoPhaseFlowPipe.gamma_s[10] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_s[10] 48/48 (1): dynamicTwoPhaseFlowPipe.re[10] = dynamicTwoPhaseFlowPipe.rs[9] 49/49 (1): dynamicTwoPhaseFlowPipe.Js[9] = dynamicTwoPhaseFlowPipe.rs[9] * dynamicTwoPhaseFlowPipe.gamma_s[9] * (dynamicTwoPhaseFlowPipe.h[11] - dynamicTwoPhaseFlowPipe.h[10]) 50/50 (1): dynamicTwoPhaseFlowPipe.J[9] = dynamicTwoPhaseFlowPipe.Je[9] + dynamicTwoPhaseFlowPipe.Js[9] 51/51 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[9] * dynamicTwoPhaseFlowPipe.Q[9] + heatSource.W0[9] + dynamicTwoPhaseFlowPipe.J[9] - dynamicTwoPhaseFlowPipe.hb[10] * dynamicTwoPhaseFlowPipe.Q[10] 52/52 (10): $cse29 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[9] + dynamicTwoPhaseFlowPipe.P[10]), dynamicTwoPhaseFlowPipe.hb[9], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 53/62 (1): $cse16 = min(dynamicTwoPhaseFlowPipe.P[9], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 54/63 (1): dynamicTwoPhaseFlowPipe.Pb[9] = max($cse16, dynamicTwoPhaseFlowPipe.ptriple) 55/64 (1): dynamicTwoPhaseFlowPipe.filo[9] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[9] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[9] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[9] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[9] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[9]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[9]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[9] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[9] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[9]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[9])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[9] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[9] * dynamicTwoPhaseFlowPipe.lambdav[9] / (dynamicTwoPhaseFlowPipe.lambdal[9] * dynamicTwoPhaseFlowPipe.rhov2[9]) 56/65 (1): dynamicTwoPhaseFlowPipe.lambdav[9] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[9] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[9] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 57/66 (1): dynamicTwoPhaseFlowPipe.Rev2[9] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[9] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[9])) 58/67 (1): dynamicTwoPhaseFlowPipe.muv2[9] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[9], dynamicTwoPhaseFlowPipe.T2[9], dynamicTwoPhaseFlowPipe.fluid) 59/68 (1): dynamicTwoPhaseFlowPipe.mul2[9] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[9], dynamicTwoPhaseFlowPipe.T2[9], dynamicTwoPhaseFlowPipe.fluid) 60/69 (1): dynamicTwoPhaseFlowPipe.Rel2[9] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[9] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[9])) 61/70 (1): dynamicTwoPhaseFlowPipe.lambdal[9] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[9] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[9] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 62/71 (1): dynamicTwoPhaseFlowPipe.khi[9] = dynamicTwoPhaseFlowPipe.filo[9] * dynamicTwoPhaseFlowPipe.lambdal[9] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 63/72 (1): dynamicTwoPhaseFlowPipe.kl2[9] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[9], dynamicTwoPhaseFlowPipe.T2[9], 0.5 * (dynamicTwoPhaseFlowPipe.P[9] + dynamicTwoPhaseFlowPipe.P[10]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 64/73 (1): dynamicTwoPhaseFlowPipe.diff_res_e[9] = dynamicTwoPhaseFlowPipe.rho2[9] * dynamicTwoPhaseFlowPipe.cpl2[9] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[9] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[9]) 65/74 (1): dynamicTwoPhaseFlowPipe.re[9] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[9] * dynamicTwoPhaseFlowPipe.diff_res_e[9]) ^ 2.0) 66/75 (1): dynamicTwoPhaseFlowPipe.Je[9] = dynamicTwoPhaseFlowPipe.re[9] * dynamicTwoPhaseFlowPipe.gamma_e[9] * (dynamicTwoPhaseFlowPipe.h[9] - dynamicTwoPhaseFlowPipe.h[10]) 67/76 (1): dynamicTwoPhaseFlowPipe.re[9] = dynamicTwoPhaseFlowPipe.rs[8] 68/77 (1): dynamicTwoPhaseFlowPipe.Js[8] = dynamicTwoPhaseFlowPipe.rs[8] * dynamicTwoPhaseFlowPipe.gamma_s[8] * (dynamicTwoPhaseFlowPipe.h[10] - dynamicTwoPhaseFlowPipe.h[9]) 69/78 (1): dynamicTwoPhaseFlowPipe.J[8] = dynamicTwoPhaseFlowPipe.Je[8] + dynamicTwoPhaseFlowPipe.Js[8] 70/79 (1): dynamicTwoPhaseFlowPipe.Je[8] = dynamicTwoPhaseFlowPipe.re[8] * dynamicTwoPhaseFlowPipe.gamma_e[8] * (dynamicTwoPhaseFlowPipe.h[8] - dynamicTwoPhaseFlowPipe.h[9]) 71/80 (1): dynamicTwoPhaseFlowPipe.hb[8] = if dynamicTwoPhaseFlowPipe.Q[8] > 0.0 then dynamicTwoPhaseFlowPipe.h[8] else dynamicTwoPhaseFlowPipe.h[9] 72/81 (1): dynamicTwoPhaseFlowPipe.hb[9] = if dynamicTwoPhaseFlowPipe.Q[9] > 0.0 then dynamicTwoPhaseFlowPipe.h[9] else dynamicTwoPhaseFlowPipe.h[10] 73/82 (1): dynamicTwoPhaseFlowPipe.hb[10] = if dynamicTwoPhaseFlowPipe.Q[10] > 0.0 then dynamicTwoPhaseFlowPipe.h[10] else dynamicTwoPhaseFlowPipe.h[11] 74/83 (10): $cse30 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[10] + dynamicTwoPhaseFlowPipe.P[11]), dynamicTwoPhaseFlowPipe.hb[10], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 75/93 (1): dynamicTwoPhaseFlowPipe.muv2[10] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[10], dynamicTwoPhaseFlowPipe.T2[10], dynamicTwoPhaseFlowPipe.fluid) 76/94 (1): dynamicTwoPhaseFlowPipe.Rev2[10] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[10] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[10])) 77/95 (1): dynamicTwoPhaseFlowPipe.lambdav[10] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[10] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[10] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 78/96 (1): dynamicTwoPhaseFlowPipe.cpl2[10] = if noEvent(dynamicTwoPhaseFlowPipe.P[11] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[10] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[10].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[10] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[10].cp else dynamicTwoPhaseFlowPipe.lsat2[10].cp 79/97 (1): dynamicTwoPhaseFlowPipe.rhov2[10] = if noEvent(dynamicTwoPhaseFlowPipe.P[11] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[10] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[10] else min(dynamicTwoPhaseFlowPipe.rho2[10], dynamicTwoPhaseFlowPipe.vsat2[10].rho) 80/98 (1): dynamicTwoPhaseFlowPipe.rhol2[10] = if noEvent(dynamicTwoPhaseFlowPipe.P[11] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[10] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[10] else max(dynamicTwoPhaseFlowPipe.rho2[10], dynamicTwoPhaseFlowPipe.lsat2[10].rho) 81/99 (1): dynamicTwoPhaseFlowPipe.xv2[10] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[10] + dynamicTwoPhaseFlowPipe.P[11]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[10] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[10].x 82/100 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[10], dynamicTwoPhaseFlowPipe.rho2[10], dynamicTwoPhaseFlowPipe.pro2[10].u, dynamicTwoPhaseFlowPipe.pro2[10].s, dynamicTwoPhaseFlowPipe.pro2[10].cp, dynamicTwoPhaseFlowPipe.pro2[10].ddhp, dynamicTwoPhaseFlowPipe.pro2[10].ddph, dynamicTwoPhaseFlowPipe.pro2[10].duph, dynamicTwoPhaseFlowPipe.pro2[10].duhp, dynamicTwoPhaseFlowPipe.pro2[10].x) = $cse30 83/110 (1): dynamicTwoPhaseFlowPipe.dpg[10] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[10] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 84/111 (1): $DER.dynamicTwoPhaseFlowPipe.Q[10] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[10] + (-dynamicTwoPhaseFlowPipe.dpf[10]) - dynamicTwoPhaseFlowPipe.P[11] - dynamicTwoPhaseFlowPipe.dpg[10] 85/112 (1): dynamicTwoPhaseFlowPipe.dpf[10] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[10] * dynamicTwoPhaseFlowPipe.Q[10] * abs(dynamicTwoPhaseFlowPipe.Q[10]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[10]) 86/113 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[10] * dynamicTwoPhaseFlowPipe.Q[10] + heatSource.W0[10] + dynamicTwoPhaseFlowPipe.J[10] - dynamicTwoPhaseFlowPipe.hb[11] * dynamicTwoPhaseFlowPipe.Q[11] 87/114 (1): dynamicTwoPhaseFlowPipe.Js[7] = dynamicTwoPhaseFlowPipe.rs[7] * dynamicTwoPhaseFlowPipe.gamma_s[7] * (dynamicTwoPhaseFlowPipe.h[9] - dynamicTwoPhaseFlowPipe.h[8]) 88/115 (1): dynamicTwoPhaseFlowPipe.J[7] = dynamicTwoPhaseFlowPipe.Je[7] + dynamicTwoPhaseFlowPipe.Js[7] 89/116 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[7] * dynamicTwoPhaseFlowPipe.Q[7] + heatSource.W0[7] + dynamicTwoPhaseFlowPipe.J[7] - dynamicTwoPhaseFlowPipe.hb[8] * dynamicTwoPhaseFlowPipe.Q[8] 90/117 (10): $cse28 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[8] + dynamicTwoPhaseFlowPipe.P[9]), dynamicTwoPhaseFlowPipe.hb[8], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 91/127 (1): dynamicTwoPhaseFlowPipe.mul2[8] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[8], dynamicTwoPhaseFlowPipe.T2[8], dynamicTwoPhaseFlowPipe.fluid) 92/128 (1): dynamicTwoPhaseFlowPipe.Rel2[8] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[8] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[8])) 93/129 (1): dynamicTwoPhaseFlowPipe.lambdal[8] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[8] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[8] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 94/130 (1): dynamicTwoPhaseFlowPipe.filo[8] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[8] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[8] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[8] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[8] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[8]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[8]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[8] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[8] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[8]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[8])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[8] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[8] * dynamicTwoPhaseFlowPipe.lambdav[8] / (dynamicTwoPhaseFlowPipe.lambdal[8] * dynamicTwoPhaseFlowPipe.rhov2[8]) 95/131 (1): dynamicTwoPhaseFlowPipe.lambdav[8] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[8] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[8] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 96/132 (1): dynamicTwoPhaseFlowPipe.Rev2[8] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[8] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[8])) 97/133 (1): dynamicTwoPhaseFlowPipe.muv2[8] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[8], dynamicTwoPhaseFlowPipe.T2[8], dynamicTwoPhaseFlowPipe.fluid) 98/134 (1): dynamicTwoPhaseFlowPipe.rhov2[8] = if noEvent(dynamicTwoPhaseFlowPipe.P[9] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[8] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[8] else min(dynamicTwoPhaseFlowPipe.rho2[8], dynamicTwoPhaseFlowPipe.vsat2[8].rho) 99/135 (1): $cse14 = min(dynamicTwoPhaseFlowPipe.P[8], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 100/136 (1): dynamicTwoPhaseFlowPipe.Pb[8] = max($cse14, dynamicTwoPhaseFlowPipe.ptriple) 101/137 (1): $cse12 = min(dynamicTwoPhaseFlowPipe.P[7], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 102/138 (1): dynamicTwoPhaseFlowPipe.Pb[7] = max($cse12, dynamicTwoPhaseFlowPipe.ptriple) 103/139 (1): dynamicTwoPhaseFlowPipe.filo[7] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[7] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[7] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[7] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[7] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[7]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[7]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[7] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[7] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[7]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[7])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[7] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[7] * dynamicTwoPhaseFlowPipe.lambdav[7] / (dynamicTwoPhaseFlowPipe.lambdal[7] * dynamicTwoPhaseFlowPipe.rhov2[7]) 104/140 (1): dynamicTwoPhaseFlowPipe.lambdal[7] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[7] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[7] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 105/141 (1): dynamicTwoPhaseFlowPipe.Rel2[7] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[7] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[7])) 106/142 (1): dynamicTwoPhaseFlowPipe.mul2[7] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[7], dynamicTwoPhaseFlowPipe.T2[7], dynamicTwoPhaseFlowPipe.fluid) 107/143 (1): dynamicTwoPhaseFlowPipe.muv2[7] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[7], dynamicTwoPhaseFlowPipe.T2[7], dynamicTwoPhaseFlowPipe.fluid) 108/144 (1): dynamicTwoPhaseFlowPipe.Rev2[7] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[7] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[7])) 109/145 (1): dynamicTwoPhaseFlowPipe.lambdav[7] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[7] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[7] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 110/146 (1): dynamicTwoPhaseFlowPipe.kl2[7] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[7], dynamicTwoPhaseFlowPipe.T2[7], 0.5 * (dynamicTwoPhaseFlowPipe.P[7] + dynamicTwoPhaseFlowPipe.P[8]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 111/147 (1): dynamicTwoPhaseFlowPipe.diff_res_e[7] = dynamicTwoPhaseFlowPipe.rho2[7] * dynamicTwoPhaseFlowPipe.cpl2[7] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[7] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[7]) 112/148 (1): dynamicTwoPhaseFlowPipe.rhov2[7] = if noEvent(dynamicTwoPhaseFlowPipe.P[8] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[7] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[7] else min(dynamicTwoPhaseFlowPipe.rho2[7], dynamicTwoPhaseFlowPipe.vsat2[7].rho) 113/149 (1): dynamicTwoPhaseFlowPipe.rhol2[7] = if noEvent(dynamicTwoPhaseFlowPipe.P[8] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[7] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[7] else max(dynamicTwoPhaseFlowPipe.rho2[7], dynamicTwoPhaseFlowPipe.lsat2[7].rho) 114/150 (1): dynamicTwoPhaseFlowPipe.dpf[7] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[7] * dynamicTwoPhaseFlowPipe.Q[7] * abs(dynamicTwoPhaseFlowPipe.Q[7]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[7]) 115/151 (1): dynamicTwoPhaseFlowPipe.khi[7] = dynamicTwoPhaseFlowPipe.filo[7] * dynamicTwoPhaseFlowPipe.lambdal[7] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 116/152 (10): $cse27 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[7] + dynamicTwoPhaseFlowPipe.P[8]), dynamicTwoPhaseFlowPipe.hb[7], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 117/162 (1): dynamicTwoPhaseFlowPipe.xv2[7] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[7] + dynamicTwoPhaseFlowPipe.P[8]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[7] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[7].x 118/163 (1): dynamicTwoPhaseFlowPipe.cpl2[7] = if noEvent(dynamicTwoPhaseFlowPipe.P[8] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[7] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[7].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[7] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[7].cp else dynamicTwoPhaseFlowPipe.lsat2[7].cp 119/164 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[7], dynamicTwoPhaseFlowPipe.rho2[7], dynamicTwoPhaseFlowPipe.pro2[7].u, dynamicTwoPhaseFlowPipe.pro2[7].s, dynamicTwoPhaseFlowPipe.pro2[7].cp, dynamicTwoPhaseFlowPipe.pro2[7].ddhp, dynamicTwoPhaseFlowPipe.pro2[7].ddph, dynamicTwoPhaseFlowPipe.pro2[7].duph, dynamicTwoPhaseFlowPipe.pro2[7].duhp, dynamicTwoPhaseFlowPipe.pro2[7].x) = $cse27 120/174 (1): dynamicTwoPhaseFlowPipe.hb[7] = if dynamicTwoPhaseFlowPipe.Q[7] > 0.0 then dynamicTwoPhaseFlowPipe.h[7] else dynamicTwoPhaseFlowPipe.h[8] 121/175 (1): dynamicTwoPhaseFlowPipe.Je[7] = dynamicTwoPhaseFlowPipe.re[7] * dynamicTwoPhaseFlowPipe.gamma_e[7] * (dynamicTwoPhaseFlowPipe.h[7] - dynamicTwoPhaseFlowPipe.h[8]) 122/176 (1): dynamicTwoPhaseFlowPipe.Js[6] = dynamicTwoPhaseFlowPipe.rs[6] * dynamicTwoPhaseFlowPipe.gamma_s[6] * (dynamicTwoPhaseFlowPipe.h[8] - dynamicTwoPhaseFlowPipe.h[7]) 123/177 (1): dynamicTwoPhaseFlowPipe.re[7] = dynamicTwoPhaseFlowPipe.rs[6] 124/178 (1): dynamicTwoPhaseFlowPipe.re[7] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[7] * dynamicTwoPhaseFlowPipe.diff_res_e[7]) ^ 2.0) 125/179 (1): dynamicTwoPhaseFlowPipe.gamma_e[7] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[7] 126/180 (1): dynamicTwoPhaseFlowPipe.gamma_s[6] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[7] 127/181 (1): dynamicTwoPhaseFlowPipe.Je[6] = dynamicTwoPhaseFlowPipe.re[6] * dynamicTwoPhaseFlowPipe.gamma_e[6] * (dynamicTwoPhaseFlowPipe.h[6] - dynamicTwoPhaseFlowPipe.h[7]) 128/182 (1): dynamicTwoPhaseFlowPipe.J[6] = dynamicTwoPhaseFlowPipe.Je[6] + dynamicTwoPhaseFlowPipe.Js[6] 129/183 (1): dynamicTwoPhaseFlowPipe.hb[6] = if dynamicTwoPhaseFlowPipe.Q[6] > 0.0 then dynamicTwoPhaseFlowPipe.h[6] else dynamicTwoPhaseFlowPipe.h[7] 130/184 (10): $cse26 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[6] + dynamicTwoPhaseFlowPipe.P[7]), dynamicTwoPhaseFlowPipe.hb[6], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 131/194 (1): $cse10 = min(dynamicTwoPhaseFlowPipe.P[6], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 132/195 (1): dynamicTwoPhaseFlowPipe.Pb[6] = max($cse10, dynamicTwoPhaseFlowPipe.ptriple) 133/196 (1): dynamicTwoPhaseFlowPipe.filo[6] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[6] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[6] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[6] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[6] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[6]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[6]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[6] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[6] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[6]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[6])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[6] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[6] * dynamicTwoPhaseFlowPipe.lambdav[6] / (dynamicTwoPhaseFlowPipe.lambdal[6] * dynamicTwoPhaseFlowPipe.rhov2[6]) 134/197 (1): dynamicTwoPhaseFlowPipe.khi[6] = dynamicTwoPhaseFlowPipe.filo[6] * dynamicTwoPhaseFlowPipe.lambdal[6] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 135/198 (1): dynamicTwoPhaseFlowPipe.dpf[6] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[6] * dynamicTwoPhaseFlowPipe.Q[6] * abs(dynamicTwoPhaseFlowPipe.Q[6]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[6]) 136/199 (1): $DER.dynamicTwoPhaseFlowPipe.Q[6] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[6] + (-dynamicTwoPhaseFlowPipe.dpf[6]) - dynamicTwoPhaseFlowPipe.P[7] - dynamicTwoPhaseFlowPipe.dpg[6] 137/200 (1): dynamicTwoPhaseFlowPipe.dpg[6] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[6] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 138/201 (1): dynamicTwoPhaseFlowPipe.rhov2[6] = if noEvent(dynamicTwoPhaseFlowPipe.P[7] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[6] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[6] else min(dynamicTwoPhaseFlowPipe.rho2[6], dynamicTwoPhaseFlowPipe.vsat2[6].rho) 139/202 (1): dynamicTwoPhaseFlowPipe.muv2[6] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[6], dynamicTwoPhaseFlowPipe.T2[6], dynamicTwoPhaseFlowPipe.fluid) 140/203 (1): dynamicTwoPhaseFlowPipe.Rev2[6] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[6] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[6])) 141/204 (1): dynamicTwoPhaseFlowPipe.lambdav[6] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[6] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[6] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 142/205 (1): dynamicTwoPhaseFlowPipe.rhol2[6] = if noEvent(dynamicTwoPhaseFlowPipe.P[7] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[6] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[6] else max(dynamicTwoPhaseFlowPipe.rho2[6], dynamicTwoPhaseFlowPipe.lsat2[6].rho) 143/206 (1): dynamicTwoPhaseFlowPipe.mul2[6] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[6], dynamicTwoPhaseFlowPipe.T2[6], dynamicTwoPhaseFlowPipe.fluid) 144/207 (1): dynamicTwoPhaseFlowPipe.Rel2[6] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[6] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[6])) 145/208 (1): dynamicTwoPhaseFlowPipe.lambdal[6] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[6] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[6] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 146/209 (1): dynamicTwoPhaseFlowPipe.kl2[6] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[6], dynamicTwoPhaseFlowPipe.T2[6], 0.5 * (dynamicTwoPhaseFlowPipe.P[6] + dynamicTwoPhaseFlowPipe.P[7]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 147/210 (1): dynamicTwoPhaseFlowPipe.diff_res_e[6] = dynamicTwoPhaseFlowPipe.rho2[6] * dynamicTwoPhaseFlowPipe.cpl2[6] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[6] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[6]) 148/211 (1): dynamicTwoPhaseFlowPipe.re[6] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[6] * dynamicTwoPhaseFlowPipe.diff_res_e[6]) ^ 2.0) 149/212 (1): dynamicTwoPhaseFlowPipe.re[6] = dynamicTwoPhaseFlowPipe.rs[5] 150/213 (1): dynamicTwoPhaseFlowPipe.Js[5] = dynamicTwoPhaseFlowPipe.rs[5] * dynamicTwoPhaseFlowPipe.gamma_s[5] * (dynamicTwoPhaseFlowPipe.h[7] - dynamicTwoPhaseFlowPipe.h[6]) 151/214 (1): dynamicTwoPhaseFlowPipe.J[5] = dynamicTwoPhaseFlowPipe.Je[5] + dynamicTwoPhaseFlowPipe.Js[5] 152/215 (1): dynamicTwoPhaseFlowPipe.Je[5] = dynamicTwoPhaseFlowPipe.re[5] * dynamicTwoPhaseFlowPipe.gamma_e[5] * (dynamicTwoPhaseFlowPipe.h[5] - dynamicTwoPhaseFlowPipe.h[6]) 153/216 (1): dynamicTwoPhaseFlowPipe.gamma_e[5] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[5] 154/217 (1): dynamicTwoPhaseFlowPipe.re[5] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[5] * dynamicTwoPhaseFlowPipe.diff_res_e[5]) ^ 2.0) 155/218 (1): dynamicTwoPhaseFlowPipe.re[5] = dynamicTwoPhaseFlowPipe.rs[4] 156/219 (1): dynamicTwoPhaseFlowPipe.Js[4] = dynamicTwoPhaseFlowPipe.rs[4] * dynamicTwoPhaseFlowPipe.gamma_s[4] * (dynamicTwoPhaseFlowPipe.h[6] - dynamicTwoPhaseFlowPipe.h[5]) 157/220 (1): dynamicTwoPhaseFlowPipe.hb[5] = if dynamicTwoPhaseFlowPipe.Q[5] > 0.0 then dynamicTwoPhaseFlowPipe.h[5] else dynamicTwoPhaseFlowPipe.h[6] 158/221 (1): dynamicTwoPhaseFlowPipe.Je[4] = dynamicTwoPhaseFlowPipe.re[4] * dynamicTwoPhaseFlowPipe.gamma_e[4] * (dynamicTwoPhaseFlowPipe.h[4] - dynamicTwoPhaseFlowPipe.h[5]) 159/222 (1): dynamicTwoPhaseFlowPipe.J[4] = dynamicTwoPhaseFlowPipe.Je[4] + dynamicTwoPhaseFlowPipe.Js[4] 160/223 (1): dynamicTwoPhaseFlowPipe.hb[4] = if dynamicTwoPhaseFlowPipe.Q[4] > 0.0 then dynamicTwoPhaseFlowPipe.h[4] else dynamicTwoPhaseFlowPipe.h[5] 161/224 (1): $cse6 = min(dynamicTwoPhaseFlowPipe.P[4], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 162/225 (1): dynamicTwoPhaseFlowPipe.Pb[4] = max($cse6, dynamicTwoPhaseFlowPipe.ptriple) 163/226 (1): dynamicTwoPhaseFlowPipe.filo[4] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[4] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[4] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[4] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[4] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[4]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[4]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[4] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[4] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[4]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[4])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[4] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[4] * dynamicTwoPhaseFlowPipe.lambdav[4] / (dynamicTwoPhaseFlowPipe.lambdal[4] * dynamicTwoPhaseFlowPipe.rhov2[4]) 164/227 (1): dynamicTwoPhaseFlowPipe.khi[4] = dynamicTwoPhaseFlowPipe.filo[4] * dynamicTwoPhaseFlowPipe.lambdal[4] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 165/228 (1): dynamicTwoPhaseFlowPipe.dpf[4] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[4] * dynamicTwoPhaseFlowPipe.Q[4] * abs(dynamicTwoPhaseFlowPipe.Q[4]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[4]) 166/229 (1): dynamicTwoPhaseFlowPipe.mul2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[4], dynamicTwoPhaseFlowPipe.T2[4], dynamicTwoPhaseFlowPipe.fluid) 167/230 (1): dynamicTwoPhaseFlowPipe.Rel2[4] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[4] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[4])) 168/231 (1): dynamicTwoPhaseFlowPipe.lambdal[4] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[4] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[4] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 169/232 (1): dynamicTwoPhaseFlowPipe.kl2[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[4], dynamicTwoPhaseFlowPipe.T2[4], 0.5 * (dynamicTwoPhaseFlowPipe.P[4] + dynamicTwoPhaseFlowPipe.P[5]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 170/233 (1): dynamicTwoPhaseFlowPipe.diff_res_e[4] = dynamicTwoPhaseFlowPipe.rho2[4] * dynamicTwoPhaseFlowPipe.cpl2[4] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[4] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[4]) 171/234 (1): dynamicTwoPhaseFlowPipe.re[4] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[4] * dynamicTwoPhaseFlowPipe.diff_res_e[4]) ^ 2.0) 172/235 (1): dynamicTwoPhaseFlowPipe.re[4] = dynamicTwoPhaseFlowPipe.rs[3] 173/236 (1): dynamicTwoPhaseFlowPipe.Js[3] = dynamicTwoPhaseFlowPipe.rs[3] * dynamicTwoPhaseFlowPipe.gamma_s[3] * (dynamicTwoPhaseFlowPipe.h[5] - dynamicTwoPhaseFlowPipe.h[4]) 174/237 (1): dynamicTwoPhaseFlowPipe.J[3] = dynamicTwoPhaseFlowPipe.Je[3] + dynamicTwoPhaseFlowPipe.Js[3] 175/238 (1): dynamicTwoPhaseFlowPipe.Je[3] = dynamicTwoPhaseFlowPipe.re[3] * dynamicTwoPhaseFlowPipe.gamma_e[3] * (dynamicTwoPhaseFlowPipe.h[3] - dynamicTwoPhaseFlowPipe.h[4]) 176/239 (1): dynamicTwoPhaseFlowPipe.re[3] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[3] * dynamicTwoPhaseFlowPipe.diff_res_e[3]) ^ 2.0) 177/240 (1): dynamicTwoPhaseFlowPipe.diff_res_e[3] = dynamicTwoPhaseFlowPipe.rho2[3] * dynamicTwoPhaseFlowPipe.cpl2[3] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[3] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[3]) 178/241 (1): dynamicTwoPhaseFlowPipe.cpl2[3] = if noEvent(dynamicTwoPhaseFlowPipe.P[4] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[3] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[3].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[3] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[3].cp else dynamicTwoPhaseFlowPipe.lsat2[3].cp 179/242 (1): dynamicTwoPhaseFlowPipe.xv2[3] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[3] + dynamicTwoPhaseFlowPipe.P[4]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[3] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[3].x 180/243 (1): dynamicTwoPhaseFlowPipe.filo[3] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[3] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[3] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[3] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[3] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[3]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[3]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[3] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[3] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[3]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[3])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[3] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[3] * dynamicTwoPhaseFlowPipe.lambdav[3] / (dynamicTwoPhaseFlowPipe.lambdal[3] * dynamicTwoPhaseFlowPipe.rhov2[3]) 181/244 (1): dynamicTwoPhaseFlowPipe.khi[3] = dynamicTwoPhaseFlowPipe.filo[3] * dynamicTwoPhaseFlowPipe.lambdal[3] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 182/245 (1): dynamicTwoPhaseFlowPipe.dpf[3] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[3] * dynamicTwoPhaseFlowPipe.Q[3] * abs(dynamicTwoPhaseFlowPipe.Q[3]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[3]) 183/246 (1): dynamicTwoPhaseFlowPipe.mul2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[3], dynamicTwoPhaseFlowPipe.T2[3], dynamicTwoPhaseFlowPipe.fluid) 184/247 (1): dynamicTwoPhaseFlowPipe.Rel2[3] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[3] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[3])) 185/248 (1): dynamicTwoPhaseFlowPipe.lambdal[3] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[3] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[3] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 186/249 (1): dynamicTwoPhaseFlowPipe.kl2[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[3], dynamicTwoPhaseFlowPipe.T2[3], 0.5 * (dynamicTwoPhaseFlowPipe.P[3] + dynamicTwoPhaseFlowPipe.P[4]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 187/250 (1): dynamicTwoPhaseFlowPipe.rhol2[3] = if noEvent(dynamicTwoPhaseFlowPipe.P[4] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[3] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[3] else max(dynamicTwoPhaseFlowPipe.rho2[3], dynamicTwoPhaseFlowPipe.lsat2[3].rho) 188/251 (1): $cse4 = min(dynamicTwoPhaseFlowPipe.P[3], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 189/252 (1): dynamicTwoPhaseFlowPipe.Pb[3] = max($cse4, dynamicTwoPhaseFlowPipe.ptriple) 190/253 (10): $cse22 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[2] + dynamicTwoPhaseFlowPipe.P[3]), dynamicTwoPhaseFlowPipe.hb[2], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 191/263 (1): $cse2 = min(dynamicTwoPhaseFlowPipe.P[2], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 192/264 (1): dynamicTwoPhaseFlowPipe.Pb[2] = max($cse2, dynamicTwoPhaseFlowPipe.ptriple) 193/265 (1): dynamicTwoPhaseFlowPipe.filo[2] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[2] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[2] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[2] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[2] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[2]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[2]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[2] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[2] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[2]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[2])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[2] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[2] * dynamicTwoPhaseFlowPipe.lambdav[2] / (dynamicTwoPhaseFlowPipe.lambdal[2] * dynamicTwoPhaseFlowPipe.rhov2[2]) 194/266 (1): dynamicTwoPhaseFlowPipe.khi[2] = dynamicTwoPhaseFlowPipe.filo[2] * dynamicTwoPhaseFlowPipe.lambdal[2] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 195/267 (1): dynamicTwoPhaseFlowPipe.lambdal[2] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[2] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[2] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 196/268 (1): dynamicTwoPhaseFlowPipe.Rel2[2] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[2] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[2])) 197/269 (1): dynamicTwoPhaseFlowPipe.mul2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[2], dynamicTwoPhaseFlowPipe.T2[2], dynamicTwoPhaseFlowPipe.fluid) 198/270 (1): dynamicTwoPhaseFlowPipe.kl2[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[2], dynamicTwoPhaseFlowPipe.T2[2], 0.5 * (dynamicTwoPhaseFlowPipe.P[2] + dynamicTwoPhaseFlowPipe.P[3]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 199/271 (1): dynamicTwoPhaseFlowPipe.diff_res_e[2] = dynamicTwoPhaseFlowPipe.rho2[2] * dynamicTwoPhaseFlowPipe.cpl2[2] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[2] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[2]) 200/272 (1): dynamicTwoPhaseFlowPipe.cpl2[2] = if noEvent(dynamicTwoPhaseFlowPipe.P[3] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[2] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[2].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[2] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[2].cp else dynamicTwoPhaseFlowPipe.lsat2[2].cp 201/273 (1): dynamicTwoPhaseFlowPipe.muv2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[2], dynamicTwoPhaseFlowPipe.T2[2], dynamicTwoPhaseFlowPipe.fluid) 202/274 (1): dynamicTwoPhaseFlowPipe.Rev2[2] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[2] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[2])) 203/275 (1): dynamicTwoPhaseFlowPipe.lambdav[2] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[2] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[2] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 204/276 (1): dynamicTwoPhaseFlowPipe.rhov2[2] = if noEvent(dynamicTwoPhaseFlowPipe.P[3] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[2] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[2] else min(dynamicTwoPhaseFlowPipe.rho2[2], dynamicTwoPhaseFlowPipe.vsat2[2].rho) 205/277 (1): dynamicTwoPhaseFlowPipe.rhol2[2] = if noEvent(dynamicTwoPhaseFlowPipe.P[3] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[2] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[2] else max(dynamicTwoPhaseFlowPipe.rho2[2], dynamicTwoPhaseFlowPipe.lsat2[2].rho) 206/278 (1): dynamicTwoPhaseFlowPipe.xv2[2] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[2] + dynamicTwoPhaseFlowPipe.P[3]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[2] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[2].x 207/279 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[2], dynamicTwoPhaseFlowPipe.rho2[2], dynamicTwoPhaseFlowPipe.pro2[2].u, dynamicTwoPhaseFlowPipe.pro2[2].s, dynamicTwoPhaseFlowPipe.pro2[2].cp, dynamicTwoPhaseFlowPipe.pro2[2].ddhp, dynamicTwoPhaseFlowPipe.pro2[2].ddph, dynamicTwoPhaseFlowPipe.pro2[2].duph, dynamicTwoPhaseFlowPipe.pro2[2].duhp, dynamicTwoPhaseFlowPipe.pro2[2].x) = $cse22 208/289 (1): dynamicTwoPhaseFlowPipe.dpg[2] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[2] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 209/290 (1): der(dynamicTwoPhaseFlowPipe.Q[2]) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[2] + (-dynamicTwoPhaseFlowPipe.dpf[2]) - dynamicTwoPhaseFlowPipe.P[3] - dynamicTwoPhaseFlowPipe.dpg[2] 210/291 (1): dynamicTwoPhaseFlowPipe.dpf[2] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[2] * dynamicTwoPhaseFlowPipe.Q[2] * abs(dynamicTwoPhaseFlowPipe.Q[2]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[2]) 211/292 (10): $cse21 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (sourceP.P0 + dynamicTwoPhaseFlowPipe.P[2]), dynamicTwoPhaseFlowPipe.hb[1], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 212/302 (1): dynamicTwoPhaseFlowPipe.xv2[1] = if noEvent(0.5 * (sourceP.P0 + dynamicTwoPhaseFlowPipe.P[2]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[1] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[1].x 213/303 (1): dynamicTwoPhaseFlowPipe.cpl2[1] = if noEvent(dynamicTwoPhaseFlowPipe.P[2] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[1] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[1].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[1] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[1].cp else dynamicTwoPhaseFlowPipe.lsat2[1].cp 214/304 (1): dynamicTwoPhaseFlowPipe.rhov2[1] = if noEvent(dynamicTwoPhaseFlowPipe.P[2] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[1] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[1] else min(dynamicTwoPhaseFlowPipe.rho2[1], dynamicTwoPhaseFlowPipe.vsat2[1].rho) 215/305 (1): dynamicTwoPhaseFlowPipe.muv2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[1], dynamicTwoPhaseFlowPipe.T2[1], dynamicTwoPhaseFlowPipe.fluid) 216/306 (1): dynamicTwoPhaseFlowPipe.Rev2[1] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[1] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[1])) 217/307 (1): dynamicTwoPhaseFlowPipe.lambdav[1] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[1] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[1] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 218/308 (1): dynamicTwoPhaseFlowPipe.rhol2[1] = if noEvent(dynamicTwoPhaseFlowPipe.P[2] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[1] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[1] else max(dynamicTwoPhaseFlowPipe.rho2[1], dynamicTwoPhaseFlowPipe.lsat2[1].rho) 219/309 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[1], dynamicTwoPhaseFlowPipe.rho2[1], dynamicTwoPhaseFlowPipe.pro2[1].u, dynamicTwoPhaseFlowPipe.pro2[1].s, dynamicTwoPhaseFlowPipe.pro2[1].cp, dynamicTwoPhaseFlowPipe.pro2[1].ddhp, dynamicTwoPhaseFlowPipe.pro2[1].ddph, dynamicTwoPhaseFlowPipe.pro2[1].duph, dynamicTwoPhaseFlowPipe.pro2[1].duhp, dynamicTwoPhaseFlowPipe.pro2[1].x) = $cse21 220/319 (1): dynamicTwoPhaseFlowPipe.dpg[1] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[1] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 221/320 (1): dynamicTwoPhaseFlowPipe.hb[1] = if dynamicTwoPhaseFlowPipe.Q[1] > 0.0 then dynamicTwoPhaseFlowPipe.h[1] else dynamicTwoPhaseFlowPipe.h[2] 222/321 (1): dynamicTwoPhaseFlowPipe.Je[2] = dynamicTwoPhaseFlowPipe.re[2] * dynamicTwoPhaseFlowPipe.gamma_e[2] * (dynamicTwoPhaseFlowPipe.h[2] - dynamicTwoPhaseFlowPipe.h[3]) 223/322 (1): dynamicTwoPhaseFlowPipe.re[2] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[2] * dynamicTwoPhaseFlowPipe.diff_res_e[2]) ^ 2.0) 224/323 (1): dynamicTwoPhaseFlowPipe.gamma_e[2] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[2] 225/324 (1): dynamicTwoPhaseFlowPipe.gamma_s[1] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[2] 226/325 (1): dynamicTwoPhaseFlowPipe.Js[1] = dynamicTwoPhaseFlowPipe.rs[1] * dynamicTwoPhaseFlowPipe.gamma_s[1] * (dynamicTwoPhaseFlowPipe.h[3] - dynamicTwoPhaseFlowPipe.h[2]) 227/326 (1): dynamicTwoPhaseFlowPipe.re[2] = dynamicTwoPhaseFlowPipe.rs[1] 228/327 (1): dynamicTwoPhaseFlowPipe.hb[2] = if dynamicTwoPhaseFlowPipe.Q[2] > 0.0 then dynamicTwoPhaseFlowPipe.h[2] else dynamicTwoPhaseFlowPipe.h[3] 229/328 (1): dynamicTwoPhaseFlowPipe.hb[3] = if dynamicTwoPhaseFlowPipe.Q[3] > 0.0 then dynamicTwoPhaseFlowPipe.h[3] else dynamicTwoPhaseFlowPipe.h[4] 230/329 (1): dynamicTwoPhaseFlowPipe.Js[2] = dynamicTwoPhaseFlowPipe.rs[2] * dynamicTwoPhaseFlowPipe.gamma_s[2] * (dynamicTwoPhaseFlowPipe.h[4] - dynamicTwoPhaseFlowPipe.h[3]) 231/330 (1): dynamicTwoPhaseFlowPipe.J[2] = dynamicTwoPhaseFlowPipe.Je[2] + dynamicTwoPhaseFlowPipe.Js[2] 232/331 (14): (dynamicTwoPhaseFlowPipe.lsat2[1], dynamicTwoPhaseFlowPipe.vsat2[1]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (sourceP.P0 + dynamicTwoPhaseFlowPipe.P[2]), dynamicTwoPhaseFlowPipe.fluid) 233/345 (14): (dynamicTwoPhaseFlowPipe.lsat2[2], dynamicTwoPhaseFlowPipe.vsat2[2]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[2] + dynamicTwoPhaseFlowPipe.P[3]), dynamicTwoPhaseFlowPipe.fluid) 234/359 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[2] * dynamicTwoPhaseFlowPipe.Q[2] + heatSource.W0[2] + dynamicTwoPhaseFlowPipe.J[2] - dynamicTwoPhaseFlowPipe.hb[3] * dynamicTwoPhaseFlowPipe.Q[3] 235/360 (10): $cse23 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[3] + dynamicTwoPhaseFlowPipe.P[4]), dynamicTwoPhaseFlowPipe.hb[3], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 236/370 (1): dynamicTwoPhaseFlowPipe.muv2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[3], dynamicTwoPhaseFlowPipe.T2[3], dynamicTwoPhaseFlowPipe.fluid) 237/371 (1): dynamicTwoPhaseFlowPipe.Rev2[3] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[3] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[3])) 238/372 (1): dynamicTwoPhaseFlowPipe.lambdav[3] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[3] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[3] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 239/373 (1): dynamicTwoPhaseFlowPipe.rhov2[3] = if noEvent(dynamicTwoPhaseFlowPipe.P[4] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[3] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[3] else min(dynamicTwoPhaseFlowPipe.rho2[3], dynamicTwoPhaseFlowPipe.vsat2[3].rho) 240/374 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[3], dynamicTwoPhaseFlowPipe.rho2[3], dynamicTwoPhaseFlowPipe.pro2[3].u, dynamicTwoPhaseFlowPipe.pro2[3].s, dynamicTwoPhaseFlowPipe.pro2[3].cp, dynamicTwoPhaseFlowPipe.pro2[3].ddhp, dynamicTwoPhaseFlowPipe.pro2[3].ddph, dynamicTwoPhaseFlowPipe.pro2[3].duph, dynamicTwoPhaseFlowPipe.pro2[3].duhp, dynamicTwoPhaseFlowPipe.pro2[3].x) = $cse23 241/384 (1): dynamicTwoPhaseFlowPipe.dpg[3] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[3] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 242/385 (1): $DER.dynamicTwoPhaseFlowPipe.Q[3] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[3] + (-dynamicTwoPhaseFlowPipe.dpf[3]) - dynamicTwoPhaseFlowPipe.P[4] - dynamicTwoPhaseFlowPipe.dpg[3] 243/386 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[3] * dynamicTwoPhaseFlowPipe.Q[3] + heatSource.W0[3] + dynamicTwoPhaseFlowPipe.J[3] - dynamicTwoPhaseFlowPipe.hb[4] * dynamicTwoPhaseFlowPipe.Q[4] 244/387 (14): (dynamicTwoPhaseFlowPipe.lsat2[3], dynamicTwoPhaseFlowPipe.vsat2[3]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[3] + dynamicTwoPhaseFlowPipe.P[4]), dynamicTwoPhaseFlowPipe.fluid) 245/401 (1): dynamicTwoPhaseFlowPipe.gamma_e[3] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[3] 246/402 (1): dynamicTwoPhaseFlowPipe.gamma_s[2] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[3] 247/403 (1): dynamicTwoPhaseFlowPipe.re[3] = dynamicTwoPhaseFlowPipe.rs[2] 248/404 (1): dynamicTwoPhaseFlowPipe.gamma_e[4] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[4] 249/405 (1): dynamicTwoPhaseFlowPipe.gamma_s[3] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[4] 250/406 (1): dynamicTwoPhaseFlowPipe.rhol2[4] = if noEvent(dynamicTwoPhaseFlowPipe.P[5] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[4] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[4] else max(dynamicTwoPhaseFlowPipe.rho2[4], dynamicTwoPhaseFlowPipe.lsat2[4].rho) 251/407 (1): dynamicTwoPhaseFlowPipe.rhov2[4] = if noEvent(dynamicTwoPhaseFlowPipe.P[5] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[4] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[4] else min(dynamicTwoPhaseFlowPipe.rho2[4], dynamicTwoPhaseFlowPipe.vsat2[4].rho) 252/408 (1): dynamicTwoPhaseFlowPipe.muv2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[4], dynamicTwoPhaseFlowPipe.T2[4], dynamicTwoPhaseFlowPipe.fluid) 253/409 (1): dynamicTwoPhaseFlowPipe.Rev2[4] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[4] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[4])) 254/410 (1): dynamicTwoPhaseFlowPipe.lambdav[4] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[4] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[4] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 255/411 (1): dynamicTwoPhaseFlowPipe.xv2[4] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[4] + dynamicTwoPhaseFlowPipe.P[5]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[4] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[4].x 256/412 (1): dynamicTwoPhaseFlowPipe.cpl2[4] = if noEvent(dynamicTwoPhaseFlowPipe.P[5] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[4] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[4].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[4] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[4].cp else dynamicTwoPhaseFlowPipe.lsat2[4].cp 257/413 (10): $cse24 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[4] + dynamicTwoPhaseFlowPipe.P[5]), dynamicTwoPhaseFlowPipe.hb[4], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 258/423 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[4], dynamicTwoPhaseFlowPipe.rho2[4], dynamicTwoPhaseFlowPipe.pro2[4].u, dynamicTwoPhaseFlowPipe.pro2[4].s, dynamicTwoPhaseFlowPipe.pro2[4].cp, dynamicTwoPhaseFlowPipe.pro2[4].ddhp, dynamicTwoPhaseFlowPipe.pro2[4].ddph, dynamicTwoPhaseFlowPipe.pro2[4].duph, dynamicTwoPhaseFlowPipe.pro2[4].duhp, dynamicTwoPhaseFlowPipe.pro2[4].x) = $cse24 259/433 (1): dynamicTwoPhaseFlowPipe.dpg[4] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[4] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 260/434 (1): $DER.dynamicTwoPhaseFlowPipe.Q[4] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[4] + (-dynamicTwoPhaseFlowPipe.dpf[4]) - dynamicTwoPhaseFlowPipe.P[5] - dynamicTwoPhaseFlowPipe.dpg[4] 261/435 (14): (dynamicTwoPhaseFlowPipe.lsat2[4], dynamicTwoPhaseFlowPipe.vsat2[4]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[4] + dynamicTwoPhaseFlowPipe.P[5]), dynamicTwoPhaseFlowPipe.fluid) 262/449 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[4] * dynamicTwoPhaseFlowPipe.Q[4] + heatSource.W0[4] + dynamicTwoPhaseFlowPipe.J[4] - dynamicTwoPhaseFlowPipe.hb[5] * dynamicTwoPhaseFlowPipe.Q[5] 263/450 (1): dynamicTwoPhaseFlowPipe.diff_res_e[5] = dynamicTwoPhaseFlowPipe.rho2[5] * dynamicTwoPhaseFlowPipe.cpl2[5] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[5] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[5]) 264/451 (1): dynamicTwoPhaseFlowPipe.cpl2[5] = if noEvent(dynamicTwoPhaseFlowPipe.P[6] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[5] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[5].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[5] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[5].cp else dynamicTwoPhaseFlowPipe.lsat2[5].cp 265/452 (10): $cse25 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[5] + dynamicTwoPhaseFlowPipe.P[6]), dynamicTwoPhaseFlowPipe.hb[5], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 266/462 (1): dynamicTwoPhaseFlowPipe.xv2[5] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[5] + dynamicTwoPhaseFlowPipe.P[6]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[5] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[5].x 267/463 (1): dynamicTwoPhaseFlowPipe.filo[5] = if noEvent(dynamicTwoPhaseFlowPipe.xv2[5] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe.xv2[5] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe.xv2[5] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[5] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[5]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[5]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe.xv2[5] * dynamicTwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe.a) * dynamicTwoPhaseFlowPipe.xv2[5] * dynamicTwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe.Pb[5]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe.Pb[5])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe.xv2[5] * dynamicTwoPhaseFlowPipe.rgliss) * dynamicTwoPhaseFlowPipe.rhol2[5] * dynamicTwoPhaseFlowPipe.lambdav[5] / (dynamicTwoPhaseFlowPipe.lambdal[5] * dynamicTwoPhaseFlowPipe.rhov2[5]) 268/464 (1): dynamicTwoPhaseFlowPipe.khi[5] = dynamicTwoPhaseFlowPipe.filo[5] * dynamicTwoPhaseFlowPipe.lambdal[5] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 269/465 (1): dynamicTwoPhaseFlowPipe.dpf[5] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[5] * dynamicTwoPhaseFlowPipe.Q[5] * abs(dynamicTwoPhaseFlowPipe.Q[5]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[5]) 270/466 (1): dynamicTwoPhaseFlowPipe.mul2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[5], dynamicTwoPhaseFlowPipe.T2[5], dynamicTwoPhaseFlowPipe.fluid) 271/467 (1): dynamicTwoPhaseFlowPipe.Rel2[5] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[5] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.mul2[5])) 272/468 (1): dynamicTwoPhaseFlowPipe.lambdal[5] = if noEvent(dynamicTwoPhaseFlowPipe.Rel2[5] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rel2[5] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 273/469 (1): dynamicTwoPhaseFlowPipe.kl2[5] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[5], dynamicTwoPhaseFlowPipe.T2[5], 0.5 * (dynamicTwoPhaseFlowPipe.P[5] + dynamicTwoPhaseFlowPipe.P[6]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 274/470 (1): dynamicTwoPhaseFlowPipe.rhol2[5] = if noEvent(dynamicTwoPhaseFlowPipe.P[6] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[5] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[5] else max(dynamicTwoPhaseFlowPipe.rho2[5], dynamicTwoPhaseFlowPipe.lsat2[5].rho) 275/471 (1): $cse8 = min(dynamicTwoPhaseFlowPipe.P[5], dynamicTwoPhaseFlowPipe.pcrit - 1.0) 276/472 (1): dynamicTwoPhaseFlowPipe.Pb[5] = max($cse8, dynamicTwoPhaseFlowPipe.ptriple) 277/473 (14): (dynamicTwoPhaseFlowPipe.lsat2[5], dynamicTwoPhaseFlowPipe.vsat2[5]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[5] + dynamicTwoPhaseFlowPipe.P[6]), dynamicTwoPhaseFlowPipe.fluid) 278/487 (1): $DER.dynamicTwoPhaseFlowPipe.Q[5] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[5] + (-dynamicTwoPhaseFlowPipe.dpf[5]) - dynamicTwoPhaseFlowPipe.P[6] - dynamicTwoPhaseFlowPipe.dpg[5] 279/488 (1): dynamicTwoPhaseFlowPipe.rhov2[5] = if noEvent(dynamicTwoPhaseFlowPipe.P[6] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[5] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[5] else min(dynamicTwoPhaseFlowPipe.rho2[5], dynamicTwoPhaseFlowPipe.vsat2[5].rho) 280/489 (1): dynamicTwoPhaseFlowPipe.muv2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe.rhov2[5], dynamicTwoPhaseFlowPipe.T2[5], dynamicTwoPhaseFlowPipe.fluid) 281/490 (1): dynamicTwoPhaseFlowPipe.Rev2[5] = abs(4.0 * dynamicTwoPhaseFlowPipe.Q[5] / (3.141592653589793 * dynamicTwoPhaseFlowPipe.Di * dynamicTwoPhaseFlowPipe.muv2[5])) 282/491 (1): dynamicTwoPhaseFlowPipe.lambdav[5] = if noEvent(dynamicTwoPhaseFlowPipe.Rev2[5] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe.Rev2[5] + dynamicTwoPhaseFlowPipe.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe.D)) ^ 2.0 else 0.01 283/492 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[5], dynamicTwoPhaseFlowPipe.rho2[5], dynamicTwoPhaseFlowPipe.pro2[5].u, dynamicTwoPhaseFlowPipe.pro2[5].s, dynamicTwoPhaseFlowPipe.pro2[5].cp, dynamicTwoPhaseFlowPipe.pro2[5].ddhp, dynamicTwoPhaseFlowPipe.pro2[5].ddph, dynamicTwoPhaseFlowPipe.pro2[5].duph, dynamicTwoPhaseFlowPipe.pro2[5].duhp, dynamicTwoPhaseFlowPipe.pro2[5].x) = $cse25 284/502 (1): dynamicTwoPhaseFlowPipe.dpg[5] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[5] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 285/503 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[5] * dynamicTwoPhaseFlowPipe.Q[5] + heatSource.W0[5] + dynamicTwoPhaseFlowPipe.J[5] - dynamicTwoPhaseFlowPipe.hb[6] * dynamicTwoPhaseFlowPipe.Q[6] 286/504 (1): dynamicTwoPhaseFlowPipe.gamma_s[4] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[5] 287/505 (1): dynamicTwoPhaseFlowPipe.gamma_e[6] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[6] 288/506 (1): dynamicTwoPhaseFlowPipe.gamma_s[5] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[6] 289/507 (1): dynamicTwoPhaseFlowPipe.cpl2[6] = if noEvent(dynamicTwoPhaseFlowPipe.P[7] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[6] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[6].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[6] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[6].cp else dynamicTwoPhaseFlowPipe.lsat2[6].cp 290/508 (1): dynamicTwoPhaseFlowPipe.xv2[6] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[6] + dynamicTwoPhaseFlowPipe.P[7]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[6] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[6].x 291/509 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[6], dynamicTwoPhaseFlowPipe.rho2[6], dynamicTwoPhaseFlowPipe.pro2[6].u, dynamicTwoPhaseFlowPipe.pro2[6].s, dynamicTwoPhaseFlowPipe.pro2[6].cp, dynamicTwoPhaseFlowPipe.pro2[6].ddhp, dynamicTwoPhaseFlowPipe.pro2[6].ddph, dynamicTwoPhaseFlowPipe.pro2[6].duph, dynamicTwoPhaseFlowPipe.pro2[6].duhp, dynamicTwoPhaseFlowPipe.pro2[6].x) = $cse26 292/519 (14): (dynamicTwoPhaseFlowPipe.lsat2[6], dynamicTwoPhaseFlowPipe.vsat2[6]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[6] + dynamicTwoPhaseFlowPipe.P[7]), dynamicTwoPhaseFlowPipe.fluid) 293/533 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[6] * dynamicTwoPhaseFlowPipe.Q[6] + heatSource.W0[6] + dynamicTwoPhaseFlowPipe.J[6] - dynamicTwoPhaseFlowPipe.hb[7] * dynamicTwoPhaseFlowPipe.Q[7] 294/534 (1): dynamicTwoPhaseFlowPipe.dpg[7] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[7] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 295/535 (1): $DER.dynamicTwoPhaseFlowPipe.Q[7] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[7] + (-dynamicTwoPhaseFlowPipe.dpf[7]) - dynamicTwoPhaseFlowPipe.P[8] - dynamicTwoPhaseFlowPipe.dpg[7] 296/536 (14): (dynamicTwoPhaseFlowPipe.lsat2[7], dynamicTwoPhaseFlowPipe.vsat2[7]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[7] + dynamicTwoPhaseFlowPipe.P[8]), dynamicTwoPhaseFlowPipe.fluid) 297/550 (14): (dynamicTwoPhaseFlowPipe.lsat2[8], dynamicTwoPhaseFlowPipe.vsat2[8]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[8] + dynamicTwoPhaseFlowPipe.P[9]), dynamicTwoPhaseFlowPipe.fluid) 298/564 (1): dynamicTwoPhaseFlowPipe.kl2[8] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe.rhol2[8], dynamicTwoPhaseFlowPipe.T2[8], 0.5 * (dynamicTwoPhaseFlowPipe.P[8] + dynamicTwoPhaseFlowPipe.P[9]), dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 299/565 (1): dynamicTwoPhaseFlowPipe.diff_res_e[8] = dynamicTwoPhaseFlowPipe.rho2[8] * dynamicTwoPhaseFlowPipe.cpl2[8] * dynamicTwoPhaseFlowPipe.dx2 / (dynamicTwoPhaseFlowPipe.rhol2[8] * dynamicTwoPhaseFlowPipe.A * dynamicTwoPhaseFlowPipe.kl2[8]) 300/566 (1): dynamicTwoPhaseFlowPipe.re[8] = exp((-0.033) * (dynamicTwoPhaseFlowPipe.Q[8] * dynamicTwoPhaseFlowPipe.diff_res_e[8]) ^ 2.0) 301/567 (1): dynamicTwoPhaseFlowPipe.re[8] = dynamicTwoPhaseFlowPipe.rs[7] 302/568 (1): dynamicTwoPhaseFlowPipe.gamma_e[8] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[8] 303/569 (1): dynamicTwoPhaseFlowPipe.gamma_s[7] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[8] 304/570 (1): dynamicTwoPhaseFlowPipe.xv2[8] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[8] + dynamicTwoPhaseFlowPipe.P[9]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[8] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[8].x 305/571 (1): dynamicTwoPhaseFlowPipe.cpl2[8] = if noEvent(dynamicTwoPhaseFlowPipe.P[9] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[8] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[8].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[8] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[8].cp else dynamicTwoPhaseFlowPipe.lsat2[8].cp 306/572 (1): $DER.dynamicTwoPhaseFlowPipe.Q[8] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[8] + (-dynamicTwoPhaseFlowPipe.dpf[8]) - dynamicTwoPhaseFlowPipe.P[9] - dynamicTwoPhaseFlowPipe.dpg[8] 307/573 (1): dynamicTwoPhaseFlowPipe.dpf[8] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[8] * dynamicTwoPhaseFlowPipe.Q[8] * abs(dynamicTwoPhaseFlowPipe.Q[8]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[8]) 308/574 (1): dynamicTwoPhaseFlowPipe.khi[8] = dynamicTwoPhaseFlowPipe.filo[8] * dynamicTwoPhaseFlowPipe.lambdal[8] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.D 309/575 (1): dynamicTwoPhaseFlowPipe.rhol2[8] = if noEvent(dynamicTwoPhaseFlowPipe.P[9] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[8] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[8] else max(dynamicTwoPhaseFlowPipe.rho2[8], dynamicTwoPhaseFlowPipe.lsat2[8].rho) 310/576 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[8], dynamicTwoPhaseFlowPipe.rho2[8], dynamicTwoPhaseFlowPipe.pro2[8].u, dynamicTwoPhaseFlowPipe.pro2[8].s, dynamicTwoPhaseFlowPipe.pro2[8].cp, dynamicTwoPhaseFlowPipe.pro2[8].ddhp, dynamicTwoPhaseFlowPipe.pro2[8].ddph, dynamicTwoPhaseFlowPipe.pro2[8].duph, dynamicTwoPhaseFlowPipe.pro2[8].duhp, dynamicTwoPhaseFlowPipe.pro2[8].x) = $cse28 311/586 (1): dynamicTwoPhaseFlowPipe.dpg[8] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[8] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 312/587 (1): 0.0 = dynamicTwoPhaseFlowPipe.hb[8] * dynamicTwoPhaseFlowPipe.Q[8] + heatSource.W0[8] + dynamicTwoPhaseFlowPipe.J[8] - dynamicTwoPhaseFlowPipe.hb[9] * dynamicTwoPhaseFlowPipe.Q[9] 313/588 (1): dynamicTwoPhaseFlowPipe.gamma_e[9] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[9] 314/589 (1): dynamicTwoPhaseFlowPipe.gamma_s[8] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[9] 315/590 (1): dynamicTwoPhaseFlowPipe.cpl2[9] = if noEvent(dynamicTwoPhaseFlowPipe.P[10] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[9] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[9].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[9] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[9].cp else dynamicTwoPhaseFlowPipe.lsat2[9].cp 316/591 (1): dynamicTwoPhaseFlowPipe.rhov2[9] = if noEvent(dynamicTwoPhaseFlowPipe.P[10] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[9] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[9] else min(dynamicTwoPhaseFlowPipe.rho2[9], dynamicTwoPhaseFlowPipe.vsat2[9].rho) 317/592 (1): dynamicTwoPhaseFlowPipe.rhol2[9] = if noEvent(dynamicTwoPhaseFlowPipe.P[10] > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[9] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.rho2[9] else max(dynamicTwoPhaseFlowPipe.rho2[9], dynamicTwoPhaseFlowPipe.lsat2[9].rho) 318/593 (1): dynamicTwoPhaseFlowPipe.dpf[9] = 0.5 * dynamicTwoPhaseFlowPipe.dpfCorr * dynamicTwoPhaseFlowPipe.khi[9] * dynamicTwoPhaseFlowPipe.Q[9] * abs(dynamicTwoPhaseFlowPipe.Q[9]) / (dynamicTwoPhaseFlowPipe.A ^ 2.0 * dynamicTwoPhaseFlowPipe.rhol2[9]) 319/594 (1): dynamicTwoPhaseFlowPipe.xv2[9] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[9] + dynamicTwoPhaseFlowPipe.P[10]) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[9] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[9].x 320/595 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[9], dynamicTwoPhaseFlowPipe.rho2[9], dynamicTwoPhaseFlowPipe.pro2[9].u, dynamicTwoPhaseFlowPipe.pro2[9].s, dynamicTwoPhaseFlowPipe.pro2[9].cp, dynamicTwoPhaseFlowPipe.pro2[9].ddhp, dynamicTwoPhaseFlowPipe.pro2[9].ddph, dynamicTwoPhaseFlowPipe.pro2[9].duph, dynamicTwoPhaseFlowPipe.pro2[9].duhp, dynamicTwoPhaseFlowPipe.pro2[9].x) = $cse29 321/605 (1): dynamicTwoPhaseFlowPipe.dpg[9] = 9.80665 * dynamicTwoPhaseFlowPipe.rho2[9] * (dynamicTwoPhaseFlowPipe.z2 - dynamicTwoPhaseFlowPipe.z1) * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.L 322/606 (1): $DER.dynamicTwoPhaseFlowPipe.Q[9] * dynamicTwoPhaseFlowPipe.dx2 / dynamicTwoPhaseFlowPipe.A = dynamicTwoPhaseFlowPipe.P[9] + (-dynamicTwoPhaseFlowPipe.dpf[9]) - dynamicTwoPhaseFlowPipe.P[10] - dynamicTwoPhaseFlowPipe.dpg[9] 323/607 (14): (dynamicTwoPhaseFlowPipe.lsat2[9], dynamicTwoPhaseFlowPipe.vsat2[9]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[9] + dynamicTwoPhaseFlowPipe.P[10]), dynamicTwoPhaseFlowPipe.fluid) 324/621 (1): dynamicTwoPhaseFlowPipe.gamma_e[10] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[10] 325/622 (1): dynamicTwoPhaseFlowPipe.gamma_s[9] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[10] 326/623 (14): (dynamicTwoPhaseFlowPipe.lsat2[10], dynamicTwoPhaseFlowPipe.vsat2[10]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[10] + dynamicTwoPhaseFlowPipe.P[11]), dynamicTwoPhaseFlowPipe.fluid) 327/637 (10): $cse31 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe.P[11] + sinkP.P0), dynamicTwoPhaseFlowPipe.hb[11], dynamicTwoPhaseFlowPipe.mode, dynamicTwoPhaseFlowPipe.fluid) 328/647 (1): dynamicTwoPhaseFlowPipe.cpl2[11] = if noEvent(sinkP.P0 > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[11] > dynamicTwoPhaseFlowPipe.Tcrit) then dynamicTwoPhaseFlowPipe.pro2[11].cp else if noEvent(dynamicTwoPhaseFlowPipe.xv2[11] <= 0.0) then dynamicTwoPhaseFlowPipe.pro2[11].cp else dynamicTwoPhaseFlowPipe.lsat2[11].cp 329/648 (1): dynamicTwoPhaseFlowPipe.xv2[11] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe.P[11] + sinkP.P0) > dynamicTwoPhaseFlowPipe.pcrit) or noEvent(dynamicTwoPhaseFlowPipe.T2[11] > dynamicTwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe.pro2[11].x 330/649 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe.T2[11], dynamicTwoPhaseFlowPipe.rho2[11], dynamicTwoPhaseFlowPipe.pro2[11].u, dynamicTwoPhaseFlowPipe.pro2[11].s, dynamicTwoPhaseFlowPipe.pro2[11].cp, dynamicTwoPhaseFlowPipe.pro2[11].ddhp, dynamicTwoPhaseFlowPipe.pro2[11].ddph, dynamicTwoPhaseFlowPipe.pro2[11].duph, dynamicTwoPhaseFlowPipe.pro2[11].duhp, dynamicTwoPhaseFlowPipe.pro2[11].x) = $cse31 331/659 (1): dynamicTwoPhaseFlowPipe.hb[11] = if dynamicTwoPhaseFlowPipe.Q[11] > 0.0 then dynamicTwoPhaseFlowPipe.h[11] else dynamicTwoPhaseFlowPipe.h[12] 332/660 (14): (dynamicTwoPhaseFlowPipe.lsat2[11], dynamicTwoPhaseFlowPipe.vsat2[11]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe.P[11] + sinkP.P0), dynamicTwoPhaseFlowPipe.fluid) 333/674 (1): $DER.dynamicTwoPhaseFlowPipe.Q[10] = der(dynamicTwoPhaseFlowPipe.Q[2]) 334/675 (1): $DER.dynamicTwoPhaseFlowPipe.Q[9] = der(dynamicTwoPhaseFlowPipe.Q[2]) 335/676 (1): $DER.dynamicTwoPhaseFlowPipe.Q[8] = der(dynamicTwoPhaseFlowPipe.Q[2]) 336/677 (1): $DER.dynamicTwoPhaseFlowPipe.Q[7] = der(dynamicTwoPhaseFlowPipe.Q[2]) 337/678 (1): $DER.dynamicTwoPhaseFlowPipe.Q[6] = der(dynamicTwoPhaseFlowPipe.Q[2]) 338/679 (1): $DER.dynamicTwoPhaseFlowPipe.Q[5] = der(dynamicTwoPhaseFlowPipe.Q[2]) 339/680 (1): $DER.dynamicTwoPhaseFlowPipe.Q[4] = der(dynamicTwoPhaseFlowPipe.Q[2]) 340/681 (1): $DER.dynamicTwoPhaseFlowPipe.Q[3] = der(dynamicTwoPhaseFlowPipe.Q[2]) 341/682 (1): dynamicTwoPhaseFlowPipe.gamma_e[1] = 1.0 / dynamicTwoPhaseFlowPipe.diff_res_e[1] Variables: 1: dynamicTwoPhaseFlowPipe.gamma_e[1]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 2: $DER.dynamicTwoPhaseFlowPipe.Q[3]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 3: $DER.dynamicTwoPhaseFlowPipe.Q[4]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 4: $DER.dynamicTwoPhaseFlowPipe.Q[5]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 5: $DER.dynamicTwoPhaseFlowPipe.Q[6]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 6: $DER.dynamicTwoPhaseFlowPipe.Q[7]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 7: $DER.dynamicTwoPhaseFlowPipe.Q[8]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 8: $DER.dynamicTwoPhaseFlowPipe.Q[9]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 9: $DER.dynamicTwoPhaseFlowPipe.Q[10]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 10: dynamicTwoPhaseFlowPipe.vsat2[11].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 11: dynamicTwoPhaseFlowPipe.vsat2[11].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 12: dynamicTwoPhaseFlowPipe.vsat2[11].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 13: dynamicTwoPhaseFlowPipe.lsat2[11].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 14: dynamicTwoPhaseFlowPipe.lsat2[11].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 15: dynamicTwoPhaseFlowPipe.h[11]:VARIABLE(start = 256076.18568728055 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 16: dynamicTwoPhaseFlowPipe.pro2[11].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 17: dynamicTwoPhaseFlowPipe.pro2[11].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 18: dynamicTwoPhaseFlowPipe.pro2[11].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 19: $cse31.x:VARIABLE(protected = true ) type: Real unreplaceable 20: dynamicTwoPhaseFlowPipe.pro2[11].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 21: dynamicTwoPhaseFlowPipe.pro2[11].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 22: dynamicTwoPhaseFlowPipe.pro2[11].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 23: dynamicTwoPhaseFlowPipe.pro2[11].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 24: dynamicTwoPhaseFlowPipe.xv2[11]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 25: dynamicTwoPhaseFlowPipe.cpl2[11]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 26: dynamicTwoPhaseFlowPipe.T2[11]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 27: dynamicTwoPhaseFlowPipe.pro2[11].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 28: $cse31.u:VARIABLE(protected = true ) type: Real unreplaceable 29: $cse31.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 30: dynamicTwoPhaseFlowPipe.hb[11]:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 31: $cse31.ddph:VARIABLE(protected = true ) type: Real unreplaceable 32: $cse31.duph:VARIABLE(protected = true ) type: Real unreplaceable 33: $cse31.cp:VARIABLE(protected = true ) type: Real unreplaceable 34: $cse31.s:VARIABLE(protected = true ) type: Real unreplaceable 35: $cse31.duhp:VARIABLE(protected = true ) type: Real unreplaceable 36: $cse31.d:VARIABLE(protected = true ) type: Real unreplaceable 37: $cse31.T:VARIABLE(protected = true ) type: Real unreplaceable 38: dynamicTwoPhaseFlowPipe.lsat2[10].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 39: dynamicTwoPhaseFlowPipe.lsat2[10].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 40: dynamicTwoPhaseFlowPipe.vsat2[10].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 41: dynamicTwoPhaseFlowPipe.lsat2[10].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 42: dynamicTwoPhaseFlowPipe.vsat2[10].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 43: dynamicTwoPhaseFlowPipe.vsat2[10].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 44: dynamicTwoPhaseFlowPipe.vsat2[10].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 45: dynamicTwoPhaseFlowPipe.lsat2[10].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 46: dynamicTwoPhaseFlowPipe.vsat2[10].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 47: dynamicTwoPhaseFlowPipe.lsat2[10].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 48: dynamicTwoPhaseFlowPipe.vsat2[10].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 49: dynamicTwoPhaseFlowPipe.vsat2[10].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 50: dynamicTwoPhaseFlowPipe.lsat2[10].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 51: dynamicTwoPhaseFlowPipe.lsat2[10].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 52: dynamicTwoPhaseFlowPipe.gamma_s[9]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 53: dynamicTwoPhaseFlowPipe.gamma_e[10]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 54: dynamicTwoPhaseFlowPipe.lsat2[9].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 55: dynamicTwoPhaseFlowPipe.vsat2[9].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 56: dynamicTwoPhaseFlowPipe.lsat2[9].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 57: dynamicTwoPhaseFlowPipe.vsat2[9].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 58: dynamicTwoPhaseFlowPipe.vsat2[9].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 59: dynamicTwoPhaseFlowPipe.vsat2[9].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 60: dynamicTwoPhaseFlowPipe.lsat2[9].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 61: dynamicTwoPhaseFlowPipe.vsat2[9].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 62: dynamicTwoPhaseFlowPipe.lsat2[9].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 63: dynamicTwoPhaseFlowPipe.vsat2[9].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 64: dynamicTwoPhaseFlowPipe.lsat2[9].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 65: dynamicTwoPhaseFlowPipe.vsat2[9].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 66: dynamicTwoPhaseFlowPipe.lsat2[9].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 67: dynamicTwoPhaseFlowPipe.lsat2[9].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 68: dynamicTwoPhaseFlowPipe.dpf[9]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 69: dynamicTwoPhaseFlowPipe.dpg[9]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 70: dynamicTwoPhaseFlowPipe.pro2[9].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 71: dynamicTwoPhaseFlowPipe.pro2[9].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 72: dynamicTwoPhaseFlowPipe.pro2[9].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 73: $cse29.x:VARIABLE(protected = true ) type: Real unreplaceable 74: dynamicTwoPhaseFlowPipe.pro2[9].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 75: dynamicTwoPhaseFlowPipe.pro2[9].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 76: dynamicTwoPhaseFlowPipe.pro2[9].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 77: dynamicTwoPhaseFlowPipe.rho2[9]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 78: dynamicTwoPhaseFlowPipe.pro2[9].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 79: dynamicTwoPhaseFlowPipe.pro2[9].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 80: dynamicTwoPhaseFlowPipe.xv2[9]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 81: dynamicTwoPhaseFlowPipe.khi[9]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 82: dynamicTwoPhaseFlowPipe.rhol2[9]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 83: dynamicTwoPhaseFlowPipe.rhov2[9]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 84: dynamicTwoPhaseFlowPipe.cpl2[9]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 85: dynamicTwoPhaseFlowPipe.gamma_s[8]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 86: dynamicTwoPhaseFlowPipe.gamma_e[9]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 87: dynamicTwoPhaseFlowPipe.J[8]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 88: dynamicTwoPhaseFlowPipe.dpg[8]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 89: dynamicTwoPhaseFlowPipe.pro2[8].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 90: dynamicTwoPhaseFlowPipe.pro2[8].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 91: dynamicTwoPhaseFlowPipe.pro2[8].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 92: dynamicTwoPhaseFlowPipe.rho2[8]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 93: dynamicTwoPhaseFlowPipe.pro2[8].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 94: dynamicTwoPhaseFlowPipe.pro2[8].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 95: dynamicTwoPhaseFlowPipe.pro2[8].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 96: dynamicTwoPhaseFlowPipe.rhol2[8]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 97: dynamicTwoPhaseFlowPipe.filo[8]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 98: dynamicTwoPhaseFlowPipe.khi[8]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 99: dynamicTwoPhaseFlowPipe.dpf[8]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 100: dynamicTwoPhaseFlowPipe.cpl2[8]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 101: dynamicTwoPhaseFlowPipe.xv2[8]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 102: dynamicTwoPhaseFlowPipe.gamma_s[7]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 103: dynamicTwoPhaseFlowPipe.gamma_e[8]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 104: dynamicTwoPhaseFlowPipe.rs[7]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 105: dynamicTwoPhaseFlowPipe.re[8]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 106: dynamicTwoPhaseFlowPipe.diff_res_e[8]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 107: dynamicTwoPhaseFlowPipe.kl2[8]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 108: dynamicTwoPhaseFlowPipe.vsat2[8].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 109: dynamicTwoPhaseFlowPipe.lsat2[8].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 110: dynamicTwoPhaseFlowPipe.lsat2[8].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 111: dynamicTwoPhaseFlowPipe.vsat2[8].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 112: dynamicTwoPhaseFlowPipe.vsat2[8].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 113: dynamicTwoPhaseFlowPipe.lsat2[8].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 114: dynamicTwoPhaseFlowPipe.lsat2[7].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 115: dynamicTwoPhaseFlowPipe.lsat2[7].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 116: dynamicTwoPhaseFlowPipe.vsat2[7].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 117: dynamicTwoPhaseFlowPipe.vsat2[7].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 118: dynamicTwoPhaseFlowPipe.vsat2[7].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 119: dynamicTwoPhaseFlowPipe.vsat2[7].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 120: dynamicTwoPhaseFlowPipe.vsat2[7].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 121: dynamicTwoPhaseFlowPipe.vsat2[7].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 122: dynamicTwoPhaseFlowPipe.vsat2[7].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 123: dynamicTwoPhaseFlowPipe.lsat2[7].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 124: dynamicTwoPhaseFlowPipe.lsat2[7].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 125: dynamicTwoPhaseFlowPipe.lsat2[7].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 126: dynamicTwoPhaseFlowPipe.lsat2[7].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 127: dynamicTwoPhaseFlowPipe.lsat2[7].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 128: dynamicTwoPhaseFlowPipe.dpf[7]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 129: dynamicTwoPhaseFlowPipe.dpg[7]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 130: dynamicTwoPhaseFlowPipe.J[6]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 131: dynamicTwoPhaseFlowPipe.vsat2[6].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 132: dynamicTwoPhaseFlowPipe.lsat2[6].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 133: dynamicTwoPhaseFlowPipe.lsat2[6].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 134: dynamicTwoPhaseFlowPipe.lsat2[6].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 135: dynamicTwoPhaseFlowPipe.vsat2[6].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 136: dynamicTwoPhaseFlowPipe.lsat2[6].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 137: dynamicTwoPhaseFlowPipe.vsat2[6].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 138: dynamicTwoPhaseFlowPipe.vsat2[6].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 139: dynamicTwoPhaseFlowPipe.vsat2[6].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 140: dynamicTwoPhaseFlowPipe.lsat2[6].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 141: dynamicTwoPhaseFlowPipe.vsat2[6].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 142: dynamicTwoPhaseFlowPipe.lsat2[6].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 143: dynamicTwoPhaseFlowPipe.lsat2[6].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 144: dynamicTwoPhaseFlowPipe.vsat2[6].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 145: dynamicTwoPhaseFlowPipe.pro2[6].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 146: $cse26.duhp:VARIABLE(protected = true ) type: Real unreplaceable 147: dynamicTwoPhaseFlowPipe.T2[6]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 148: dynamicTwoPhaseFlowPipe.xv2[6]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 149: dynamicTwoPhaseFlowPipe.pro2[6].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 150: dynamicTwoPhaseFlowPipe.pro2[6].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 151: dynamicTwoPhaseFlowPipe.pro2[6].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 152: dynamicTwoPhaseFlowPipe.pro2[6].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 153: dynamicTwoPhaseFlowPipe.cpl2[6]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 154: dynamicTwoPhaseFlowPipe.pro2[6].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 155: dynamicTwoPhaseFlowPipe.pro2[6].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 156: dynamicTwoPhaseFlowPipe.pro2[6].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 157: dynamicTwoPhaseFlowPipe.gamma_s[5]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 158: dynamicTwoPhaseFlowPipe.gamma_e[6]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 159: dynamicTwoPhaseFlowPipe.gamma_s[4]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 160: dynamicTwoPhaseFlowPipe.J[5]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 161: dynamicTwoPhaseFlowPipe.dpg[5]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 162: dynamicTwoPhaseFlowPipe.rho2[5]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 163: dynamicTwoPhaseFlowPipe.pro2[5].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 164: dynamicTwoPhaseFlowPipe.pro2[5].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 165: dynamicTwoPhaseFlowPipe.T2[5]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 166: dynamicTwoPhaseFlowPipe.lambdav[5]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 167: dynamicTwoPhaseFlowPipe.Rev2[5]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 168: dynamicTwoPhaseFlowPipe.muv2[5]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 169: dynamicTwoPhaseFlowPipe.rhov2[5]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 170: dynamicTwoPhaseFlowPipe.dpf[5]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 171: dynamicTwoPhaseFlowPipe.vsat2[5].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 172: dynamicTwoPhaseFlowPipe.vsat2[5].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 173: dynamicTwoPhaseFlowPipe.Pb[5]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 174: $cse8:VARIABLE(protected = true ) type: Real unreplaceable 175: dynamicTwoPhaseFlowPipe.P[5]:VARIABLE(min = 0.0 start = 227647.89301968 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 176: dynamicTwoPhaseFlowPipe.vsat2[5].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 177: dynamicTwoPhaseFlowPipe.lsat2[5].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 178: dynamicTwoPhaseFlowPipe.lsat2[5].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 179: dynamicTwoPhaseFlowPipe.lsat2[5].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 180: dynamicTwoPhaseFlowPipe.vsat2[5].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 181: dynamicTwoPhaseFlowPipe.vsat2[5].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 182: dynamicTwoPhaseFlowPipe.vsat2[5].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 183: dynamicTwoPhaseFlowPipe.vsat2[5].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 184: dynamicTwoPhaseFlowPipe.lsat2[5].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 185: dynamicTwoPhaseFlowPipe.lsat2[5].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 186: dynamicTwoPhaseFlowPipe.lsat2[5].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 187: dynamicTwoPhaseFlowPipe.lsat2[5].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 188: dynamicTwoPhaseFlowPipe.kl2[5]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 189: dynamicTwoPhaseFlowPipe.lambdal[5]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 190: dynamicTwoPhaseFlowPipe.Rel2[5]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 191: dynamicTwoPhaseFlowPipe.mul2[5]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 192: dynamicTwoPhaseFlowPipe.rhol2[5]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 193: dynamicTwoPhaseFlowPipe.khi[5]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 194: dynamicTwoPhaseFlowPipe.filo[5]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 195: dynamicTwoPhaseFlowPipe.xv2[5]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 196: dynamicTwoPhaseFlowPipe.pro2[5].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 197: dynamicTwoPhaseFlowPipe.pro2[5].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 198: dynamicTwoPhaseFlowPipe.pro2[5].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 199: dynamicTwoPhaseFlowPipe.pro2[5].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 200: dynamicTwoPhaseFlowPipe.pro2[5].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 201: $cse25.u:VARIABLE(protected = true ) type: Real unreplaceable 202: $cse25.d:VARIABLE(protected = true ) type: Real unreplaceable 203: $cse25.T:VARIABLE(protected = true ) type: Real unreplaceable 204: $cse25.cp:VARIABLE(protected = true ) type: Real unreplaceable 205: $cse25.duhp:VARIABLE(protected = true ) type: Real unreplaceable 206: $cse25.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 207: dynamicTwoPhaseFlowPipe.hb[5]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 208: $cse25.duph:VARIABLE(protected = true ) type: Real unreplaceable 209: $cse25.x:VARIABLE(protected = true ) type: Real unreplaceable 210: $cse25.ddph:VARIABLE(protected = true ) type: Real unreplaceable 211: $cse25.s:VARIABLE(protected = true ) type: Real unreplaceable 212: dynamicTwoPhaseFlowPipe.pro2[5].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 213: dynamicTwoPhaseFlowPipe.cpl2[5]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 214: dynamicTwoPhaseFlowPipe.J[4]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 215: dynamicTwoPhaseFlowPipe.vsat2[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 216: dynamicTwoPhaseFlowPipe.lsat2[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 217: dynamicTwoPhaseFlowPipe.vsat2[4].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 218: dynamicTwoPhaseFlowPipe.lsat2[4].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 219: dynamicTwoPhaseFlowPipe.lsat2[4].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 220: dynamicTwoPhaseFlowPipe.vsat2[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 221: dynamicTwoPhaseFlowPipe.vsat2[4].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 222: dynamicTwoPhaseFlowPipe.vsat2[4].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 223: dynamicTwoPhaseFlowPipe.lsat2[4].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 224: dynamicTwoPhaseFlowPipe.lsat2[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 225: dynamicTwoPhaseFlowPipe.lsat2[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 226: dynamicTwoPhaseFlowPipe.vsat2[4].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 227: dynamicTwoPhaseFlowPipe.vsat2[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 228: dynamicTwoPhaseFlowPipe.lsat2[4].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 229: dynamicTwoPhaseFlowPipe.dpf[4]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 230: dynamicTwoPhaseFlowPipe.dpg[4]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 231: dynamicTwoPhaseFlowPipe.pro2[4].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 232: dynamicTwoPhaseFlowPipe.pro2[4].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 233: dynamicTwoPhaseFlowPipe.pro2[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 234: dynamicTwoPhaseFlowPipe.pro2[4].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 235: dynamicTwoPhaseFlowPipe.T2[4]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 236: dynamicTwoPhaseFlowPipe.pro2[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 237: $cse24.duhp:VARIABLE(protected = true ) type: Real unreplaceable 238: $cse24.u:VARIABLE(protected = true ) type: Real unreplaceable 239: $cse24.duph:VARIABLE(protected = true ) type: Real unreplaceable 240: $cse24.s:VARIABLE(protected = true ) type: Real unreplaceable 241: $cse24.T:VARIABLE(protected = true ) type: Real unreplaceable 242: $cse24.d:VARIABLE(protected = true ) type: Real unreplaceable 243: $cse24.ddph:VARIABLE(protected = true ) type: Real unreplaceable 244: $cse24.x:VARIABLE(protected = true ) type: Real unreplaceable 245: dynamicTwoPhaseFlowPipe.pro2[4].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 246: dynamicTwoPhaseFlowPipe.cpl2[4]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 247: dynamicTwoPhaseFlowPipe.xv2[4]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 248: dynamicTwoPhaseFlowPipe.pro2[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 249: dynamicTwoPhaseFlowPipe.pro2[4].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 250: dynamicTwoPhaseFlowPipe.lambdav[4]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 251: dynamicTwoPhaseFlowPipe.Rev2[4]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 252: dynamicTwoPhaseFlowPipe.muv2[4]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 253: dynamicTwoPhaseFlowPipe.rhov2[4]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 254: dynamicTwoPhaseFlowPipe.rho2[4]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 255: dynamicTwoPhaseFlowPipe.gamma_s[3]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 256: dynamicTwoPhaseFlowPipe.gamma_e[4]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 257: dynamicTwoPhaseFlowPipe.rs[2]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 258: dynamicTwoPhaseFlowPipe.gamma_s[2]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 259: dynamicTwoPhaseFlowPipe.gamma_e[3]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 260: dynamicTwoPhaseFlowPipe.vsat2[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 261: dynamicTwoPhaseFlowPipe.vsat2[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 262: dynamicTwoPhaseFlowPipe.vsat2[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 263: dynamicTwoPhaseFlowPipe.lsat2[3].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 264: dynamicTwoPhaseFlowPipe.lsat2[3].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 265: dynamicTwoPhaseFlowPipe.vsat2[3].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 266: dynamicTwoPhaseFlowPipe.lsat2[3].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 267: dynamicTwoPhaseFlowPipe.lsat2[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 268: dynamicTwoPhaseFlowPipe.vsat2[3].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 269: dynamicTwoPhaseFlowPipe.J[3]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 270: dynamicTwoPhaseFlowPipe.dpf[3]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 271: dynamicTwoPhaseFlowPipe.dpg[3]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 272: $cse23.duph:VARIABLE(protected = true ) type: Real unreplaceable 273: dynamicTwoPhaseFlowPipe.pro2[3].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 274: dynamicTwoPhaseFlowPipe.pro2[3].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 275: dynamicTwoPhaseFlowPipe.rho2[3]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 276: dynamicTwoPhaseFlowPipe.pro2[3].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 277: dynamicTwoPhaseFlowPipe.rhov2[3]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 278: dynamicTwoPhaseFlowPipe.lambdav[3]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 279: dynamicTwoPhaseFlowPipe.Rev2[3]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 280: dynamicTwoPhaseFlowPipe.muv2[3]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 281: dynamicTwoPhaseFlowPipe.T2[3]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 282: dynamicTwoPhaseFlowPipe.pro2[3].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 283: dynamicTwoPhaseFlowPipe.pro2[3].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 284: dynamicTwoPhaseFlowPipe.pro2[3].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 285: $cse23.ddph:VARIABLE(protected = true ) type: Real unreplaceable 286: $cse23.s:VARIABLE(protected = true ) type: Real unreplaceable 287: $cse23.T:VARIABLE(protected = true ) type: Real unreplaceable 288: $cse23.duhp:VARIABLE(protected = true ) type: Real unreplaceable 289: dynamicTwoPhaseFlowPipe.hb[3]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 290: $cse23.x:VARIABLE(protected = true ) type: Real unreplaceable 291: $cse23.u:VARIABLE(protected = true ) type: Real unreplaceable 292: $cse23.d:VARIABLE(protected = true ) type: Real unreplaceable 293: $cse23.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 294: $cse23.cp:VARIABLE(protected = true ) type: Real unreplaceable 295: dynamicTwoPhaseFlowPipe.J[2]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 296: dynamicTwoPhaseFlowPipe.vsat2[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 297: dynamicTwoPhaseFlowPipe.vsat2[2].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 298: dynamicTwoPhaseFlowPipe.lsat2[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 299: dynamicTwoPhaseFlowPipe.vsat2[2].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 300: dynamicTwoPhaseFlowPipe.vsat2[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 301: dynamicTwoPhaseFlowPipe.vsat2[2].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 302: dynamicTwoPhaseFlowPipe.vsat2[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 303: dynamicTwoPhaseFlowPipe.lsat2[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 304: dynamicTwoPhaseFlowPipe.vsat2[2].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 305: dynamicTwoPhaseFlowPipe.lsat2[2].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 306: dynamicTwoPhaseFlowPipe.lsat2[2].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 307: dynamicTwoPhaseFlowPipe.lsat2[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 308: dynamicTwoPhaseFlowPipe.lsat2[2].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 309: dynamicTwoPhaseFlowPipe.lsat2[2].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 310: dynamicTwoPhaseFlowPipe.vsat2[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 311: dynamicTwoPhaseFlowPipe.lsat2[1].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 312: dynamicTwoPhaseFlowPipe.vsat2[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 313: dynamicTwoPhaseFlowPipe.lsat2[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 314: dynamicTwoPhaseFlowPipe.vsat2[1].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 315: dynamicTwoPhaseFlowPipe.vsat2[1].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 316: dynamicTwoPhaseFlowPipe.vsat2[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 317: dynamicTwoPhaseFlowPipe.lsat2[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 318: dynamicTwoPhaseFlowPipe.vsat2[1].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 319: dynamicTwoPhaseFlowPipe.vsat2[1].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 320: dynamicTwoPhaseFlowPipe.lsat2[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 321: dynamicTwoPhaseFlowPipe.lsat2[1].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 322: dynamicTwoPhaseFlowPipe.lsat2[1].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 323: dynamicTwoPhaseFlowPipe.lsat2[1].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 324: dynamicTwoPhaseFlowPipe.Je[2]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 325: dynamicTwoPhaseFlowPipe.Js[2]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 326: dynamicTwoPhaseFlowPipe.h[4]:VARIABLE(start = 126534.14136650086 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 327: dynamicTwoPhaseFlowPipe.h[3]:VARIABLE(start = 108028.13503495205 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 328: dynamicTwoPhaseFlowPipe.rs[1]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 329: dynamicTwoPhaseFlowPipe.Js[1]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 330: dynamicTwoPhaseFlowPipe.gamma_s[1]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 331: dynamicTwoPhaseFlowPipe.gamma_e[2]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 332: dynamicTwoPhaseFlowPipe.diff_res_e[2]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 333: dynamicTwoPhaseFlowPipe.re[2]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 334: dynamicTwoPhaseFlowPipe.h[2]:VARIABLE(start = 89522.1287033792 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 335: dynamicTwoPhaseFlowPipe.dpg[1]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 336: dynamicTwoPhaseFlowPipe.pro2[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 337: dynamicTwoPhaseFlowPipe.rhol2[1]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 338: dynamicTwoPhaseFlowPipe.lambdav[1]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 339: dynamicTwoPhaseFlowPipe.Rev2[1]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 340: dynamicTwoPhaseFlowPipe.muv2[1]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 341: dynamicTwoPhaseFlowPipe.rhov2[1]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 342: dynamicTwoPhaseFlowPipe.rho2[1]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 343: dynamicTwoPhaseFlowPipe.pro2[1].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 344: dynamicTwoPhaseFlowPipe.pro2[1].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 345: dynamicTwoPhaseFlowPipe.pro2[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 346: dynamicTwoPhaseFlowPipe.pro2[1].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 347: dynamicTwoPhaseFlowPipe.pro2[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 348: dynamicTwoPhaseFlowPipe.pro2[1].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 349: dynamicTwoPhaseFlowPipe.cpl2[1]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 350: dynamicTwoPhaseFlowPipe.xv2[1]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 351: dynamicTwoPhaseFlowPipe.pro2[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 352: $cse21.d:VARIABLE(protected = true ) type: Real unreplaceable 353: $cse21.s:VARIABLE(protected = true ) type: Real unreplaceable 354: $cse21.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 355: $cse21.T:VARIABLE(protected = true ) type: Real unreplaceable 356: $cse21.x:VARIABLE(protected = true ) type: Real unreplaceable 357: $cse21.duph:VARIABLE(protected = true ) type: Real unreplaceable 358: $cse21.u:VARIABLE(protected = true ) type: Real unreplaceable 359: $cse21.duhp:VARIABLE(protected = true ) type: Real unreplaceable 360: dynamicTwoPhaseFlowPipe.hb[1]:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 361: $cse21.ddph:VARIABLE(protected = true ) type: Real unreplaceable 362: $cse21.cp:VARIABLE(protected = true ) type: Real unreplaceable 363: dynamicTwoPhaseFlowPipe.khi[2]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 364: dynamicTwoPhaseFlowPipe.dpf[2]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 365: dynamicTwoPhaseFlowPipe.dpg[2]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 366: dynamicTwoPhaseFlowPipe.pro2[2].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 367: dynamicTwoPhaseFlowPipe.xv2[2]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 368: dynamicTwoPhaseFlowPipe.pro2[2].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 369: dynamicTwoPhaseFlowPipe.pro2[2].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 370: dynamicTwoPhaseFlowPipe.pro2[2].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 371: $cse22.duhp:VARIABLE(protected = true ) type: Real unreplaceable 372: dynamicTwoPhaseFlowPipe.pro2[2].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 373: $cse22.duph:VARIABLE(protected = true ) type: Real unreplaceable 374: dynamicTwoPhaseFlowPipe.pro2[2].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 375: dynamicTwoPhaseFlowPipe.pro2[2].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 376: dynamicTwoPhaseFlowPipe.rho2[2]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 377: dynamicTwoPhaseFlowPipe.rhov2[2]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 378: dynamicTwoPhaseFlowPipe.lambdav[2]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 379: dynamicTwoPhaseFlowPipe.Rev2[2]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 380: dynamicTwoPhaseFlowPipe.muv2[2]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 381: dynamicTwoPhaseFlowPipe.T2[2]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 382: dynamicTwoPhaseFlowPipe.pro2[2].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 383: dynamicTwoPhaseFlowPipe.cpl2[2]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 384: dynamicTwoPhaseFlowPipe.kl2[2]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 385: dynamicTwoPhaseFlowPipe.rhol2[2]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 386: dynamicTwoPhaseFlowPipe.mul2[2]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 387: dynamicTwoPhaseFlowPipe.Rel2[2]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 388: dynamicTwoPhaseFlowPipe.lambdal[2]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 389: dynamicTwoPhaseFlowPipe.filo[2]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 390: dynamicTwoPhaseFlowPipe.Pb[2]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 391: $cse2:VARIABLE(protected = true ) type: Real unreplaceable 392: dynamicTwoPhaseFlowPipe.P[2]:VARIABLE(min = 0.0 start = 281934.94102069 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 393: $cse22.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 394: $cse22.x:VARIABLE(protected = true ) type: Real unreplaceable 395: $cse22.T:VARIABLE(protected = true ) type: Real unreplaceable 396: $cse22.cp:VARIABLE(protected = true ) type: Real unreplaceable 397: $cse22.u:VARIABLE(protected = true ) type: Real unreplaceable 398: dynamicTwoPhaseFlowPipe.hb[2]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 399: $cse22.s:VARIABLE(protected = true ) type: Real unreplaceable 400: $cse22.ddph:VARIABLE(protected = true ) type: Real unreplaceable 401: $cse22.d:VARIABLE(protected = true ) type: Real unreplaceable 402: dynamicTwoPhaseFlowPipe.Pb[3]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 403: $cse4:VARIABLE(protected = true ) type: Real unreplaceable 404: dynamicTwoPhaseFlowPipe.P[3]:VARIABLE(min = 0.0 start = 263857.29519348 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 405: dynamicTwoPhaseFlowPipe.lsat2[3].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 406: dynamicTwoPhaseFlowPipe.vsat2[3].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 407: dynamicTwoPhaseFlowPipe.vsat2[3].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 408: dynamicTwoPhaseFlowPipe.lsat2[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 409: dynamicTwoPhaseFlowPipe.lsat2[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 410: dynamicTwoPhaseFlowPipe.kl2[3]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 411: dynamicTwoPhaseFlowPipe.lambdal[3]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 412: dynamicTwoPhaseFlowPipe.Rel2[3]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 413: dynamicTwoPhaseFlowPipe.mul2[3]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 414: dynamicTwoPhaseFlowPipe.rhol2[3]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 415: dynamicTwoPhaseFlowPipe.khi[3]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 416: dynamicTwoPhaseFlowPipe.filo[3]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 417: dynamicTwoPhaseFlowPipe.xv2[3]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 418: dynamicTwoPhaseFlowPipe.pro2[3].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 419: dynamicTwoPhaseFlowPipe.pro2[3].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 420: dynamicTwoPhaseFlowPipe.cpl2[3]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 421: dynamicTwoPhaseFlowPipe.diff_res_e[3]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 422: dynamicTwoPhaseFlowPipe.re[3]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 423: dynamicTwoPhaseFlowPipe.Je[3]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 424: dynamicTwoPhaseFlowPipe.Js[3]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 425: dynamicTwoPhaseFlowPipe.rs[3]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 426: dynamicTwoPhaseFlowPipe.re[4]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 427: dynamicTwoPhaseFlowPipe.diff_res_e[4]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 428: dynamicTwoPhaseFlowPipe.kl2[4]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 429: dynamicTwoPhaseFlowPipe.lambdal[4]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 430: dynamicTwoPhaseFlowPipe.Rel2[4]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 431: dynamicTwoPhaseFlowPipe.mul2[4]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 432: dynamicTwoPhaseFlowPipe.rhol2[4]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 433: dynamicTwoPhaseFlowPipe.khi[4]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 434: dynamicTwoPhaseFlowPipe.filo[4]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 435: dynamicTwoPhaseFlowPipe.Pb[4]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 436: $cse6:VARIABLE(protected = true ) type: Real unreplaceable 437: dynamicTwoPhaseFlowPipe.P[4]:VARIABLE(min = 0.0 start = 245762.87920492 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 438: $cse24.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 439: $cse24.cp:VARIABLE(protected = true ) type: Real unreplaceable 440: dynamicTwoPhaseFlowPipe.hb[4]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 441: dynamicTwoPhaseFlowPipe.Js[4]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 442: dynamicTwoPhaseFlowPipe.Je[4]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 443: dynamicTwoPhaseFlowPipe.h[6]:VARIABLE(start = 163546.15402957145 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 444: dynamicTwoPhaseFlowPipe.h[5]:VARIABLE(start = 145040.14769798872 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 445: dynamicTwoPhaseFlowPipe.rs[4]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 446: dynamicTwoPhaseFlowPipe.re[5]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 447: dynamicTwoPhaseFlowPipe.diff_res_e[5]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 448: dynamicTwoPhaseFlowPipe.gamma_e[5]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 449: dynamicTwoPhaseFlowPipe.Je[5]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 450: dynamicTwoPhaseFlowPipe.Js[5]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 451: dynamicTwoPhaseFlowPipe.rs[5]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 452: dynamicTwoPhaseFlowPipe.re[6]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 453: dynamicTwoPhaseFlowPipe.diff_res_e[6]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 454: dynamicTwoPhaseFlowPipe.kl2[6]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 455: dynamicTwoPhaseFlowPipe.lambdal[6]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 456: dynamicTwoPhaseFlowPipe.Rel2[6]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 457: dynamicTwoPhaseFlowPipe.mul2[6]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 458: dynamicTwoPhaseFlowPipe.rhol2[6]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 459: dynamicTwoPhaseFlowPipe.lambdav[6]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 460: dynamicTwoPhaseFlowPipe.Rev2[6]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 461: dynamicTwoPhaseFlowPipe.muv2[6]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 462: dynamicTwoPhaseFlowPipe.rhov2[6]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 463: dynamicTwoPhaseFlowPipe.rho2[6]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 464: dynamicTwoPhaseFlowPipe.dpg[6]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 465: dynamicTwoPhaseFlowPipe.dpf[6]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 466: dynamicTwoPhaseFlowPipe.khi[6]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 467: dynamicTwoPhaseFlowPipe.filo[6]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 468: dynamicTwoPhaseFlowPipe.Pb[6]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 469: $cse10:VARIABLE(protected = true ) type: Real unreplaceable 470: dynamicTwoPhaseFlowPipe.P[6]:VARIABLE(min = 0.0 start = 209508.84324089 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 471: $cse26.T:VARIABLE(protected = true ) type: Real unreplaceable 472: $cse26.s:VARIABLE(protected = true ) type: Real unreplaceable 473: $cse26.ddph:VARIABLE(protected = true ) type: Real unreplaceable 474: $cse26.cp:VARIABLE(protected = true ) type: Real unreplaceable 475: $cse26.u:VARIABLE(protected = true ) type: Real unreplaceable 476: $cse26.duph:VARIABLE(protected = true ) type: Real unreplaceable 477: $cse26.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 478: $cse26.d:VARIABLE(protected = true ) type: Real unreplaceable 479: $cse26.x:VARIABLE(protected = true ) type: Real unreplaceable 480: dynamicTwoPhaseFlowPipe.hb[6]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 481: dynamicTwoPhaseFlowPipe.Js[6]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 482: dynamicTwoPhaseFlowPipe.Je[6]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 483: dynamicTwoPhaseFlowPipe.gamma_s[6]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 484: dynamicTwoPhaseFlowPipe.gamma_e[7]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at inlet of thermal node i" type: Real [10] 485: dynamicTwoPhaseFlowPipe.diff_res_e[7]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 486: dynamicTwoPhaseFlowPipe.re[7]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 487: dynamicTwoPhaseFlowPipe.rs[6]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 488: dynamicTwoPhaseFlowPipe.Je[7]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 489: dynamicTwoPhaseFlowPipe.h[7]:VARIABLE(start = 182052.16036112772 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 490: dynamicTwoPhaseFlowPipe.pro2[7].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 491: $cse27.duhp:VARIABLE(protected = true ) type: Real unreplaceable 492: dynamicTwoPhaseFlowPipe.pro2[7].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 493: dynamicTwoPhaseFlowPipe.pro2[7].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 494: dynamicTwoPhaseFlowPipe.cpl2[7]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 495: dynamicTwoPhaseFlowPipe.xv2[7]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 496: dynamicTwoPhaseFlowPipe.pro2[7].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 497: dynamicTwoPhaseFlowPipe.pro2[7].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 498: dynamicTwoPhaseFlowPipe.pro2[7].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 499: $cse27.u:VARIABLE(protected = true ) type: Real unreplaceable 500: $cse27.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 501: dynamicTwoPhaseFlowPipe.hb[7]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 502: $cse27.cp:VARIABLE(protected = true ) type: Real unreplaceable 503: $cse27.s:VARIABLE(protected = true ) type: Real unreplaceable 504: $cse27.ddph:VARIABLE(protected = true ) type: Real unreplaceable 505: $cse27.duph:VARIABLE(protected = true ) type: Real unreplaceable 506: $cse27.d:VARIABLE(protected = true ) type: Real unreplaceable 507: $cse27.x:VARIABLE(protected = true ) type: Real unreplaceable 508: $cse27.T:VARIABLE(protected = true ) type: Real unreplaceable 509: dynamicTwoPhaseFlowPipe.pro2[7].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 510: dynamicTwoPhaseFlowPipe.pro2[7].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 511: dynamicTwoPhaseFlowPipe.filo[7]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 512: dynamicTwoPhaseFlowPipe.khi[7]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 513: dynamicTwoPhaseFlowPipe.rhol2[7]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 514: dynamicTwoPhaseFlowPipe.rhov2[7]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 515: dynamicTwoPhaseFlowPipe.rho2[7]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 516: dynamicTwoPhaseFlowPipe.kl2[7]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 517: dynamicTwoPhaseFlowPipe.lambdav[7]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 518: dynamicTwoPhaseFlowPipe.Rev2[7]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 519: dynamicTwoPhaseFlowPipe.muv2[7]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 520: dynamicTwoPhaseFlowPipe.T2[7]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 521: dynamicTwoPhaseFlowPipe.mul2[7]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 522: dynamicTwoPhaseFlowPipe.Rel2[7]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 523: dynamicTwoPhaseFlowPipe.lambdal[7]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 524: dynamicTwoPhaseFlowPipe.Pb[7]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 525: $cse12:VARIABLE(protected = true ) type: Real unreplaceable 526: dynamicTwoPhaseFlowPipe.P[7]:VARIABLE(min = 0.0 start = 191342.485106 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 527: dynamicTwoPhaseFlowPipe.Pb[8]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 528: $cse14:VARIABLE(protected = true ) type: Real unreplaceable 529: dynamicTwoPhaseFlowPipe.P[8]:VARIABLE(min = 0.0 start = 173145.77779074 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 530: dynamicTwoPhaseFlowPipe.lsat2[8].cp:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant pressure" type: Real [11] 531: dynamicTwoPhaseFlowPipe.lsat2[8].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 532: dynamicTwoPhaseFlowPipe.lsat2[8].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 533: dynamicTwoPhaseFlowPipe.vsat2[8].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 534: dynamicTwoPhaseFlowPipe.lsat2[8].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 535: dynamicTwoPhaseFlowPipe.vsat2[8].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 536: dynamicTwoPhaseFlowPipe.vsat2[8].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 537: dynamicTwoPhaseFlowPipe.vsat2[8].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 538: dynamicTwoPhaseFlowPipe.rhov2[8]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 539: dynamicTwoPhaseFlowPipe.muv2[8]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 540: dynamicTwoPhaseFlowPipe.Rev2[8]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 541: dynamicTwoPhaseFlowPipe.lambdav[8]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 542: dynamicTwoPhaseFlowPipe.lambdal[8]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 543: dynamicTwoPhaseFlowPipe.Rel2[8]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 544: dynamicTwoPhaseFlowPipe.mul2[8]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 545: dynamicTwoPhaseFlowPipe.T2[8]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 546: dynamicTwoPhaseFlowPipe.pro2[8].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 547: dynamicTwoPhaseFlowPipe.pro2[8].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 548: $cse28.cp:VARIABLE(protected = true ) type: Real unreplaceable 549: $cse28.duph:VARIABLE(protected = true ) type: Real unreplaceable 550: $cse28.x:VARIABLE(protected = true ) type: Real unreplaceable 551: $cse28.d:VARIABLE(protected = true ) type: Real unreplaceable 552: $cse28.u:VARIABLE(protected = true ) type: Real unreplaceable 553: $cse28.duhp:VARIABLE(protected = true ) type: Real unreplaceable 554: $cse28.s:VARIABLE(protected = true ) type: Real unreplaceable 555: $cse28.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 556: $cse28.ddph:VARIABLE(protected = true ) type: Real unreplaceable 557: $cse28.T:VARIABLE(protected = true ) type: Real unreplaceable 558: dynamicTwoPhaseFlowPipe.hb[8]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 559: dynamicTwoPhaseFlowPipe.J[7]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 560: dynamicTwoPhaseFlowPipe.Js[7]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 561: dynamicTwoPhaseFlowPipe.J[10]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 562: dynamicTwoPhaseFlowPipe.khi[10]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 563: dynamicTwoPhaseFlowPipe.dpf[10]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 564: dynamicTwoPhaseFlowPipe.dpg[10]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 565: dynamicTwoPhaseFlowPipe.pro2[10].duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11] 566: dynamicTwoPhaseFlowPipe.pro2[10].ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11] 567: dynamicTwoPhaseFlowPipe.pro2[10].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real [11] 568: dynamicTwoPhaseFlowPipe.pro2[10].duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11] 569: dynamicTwoPhaseFlowPipe.pro2[10].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real [11] 570: dynamicTwoPhaseFlowPipe.xv2[10]:VARIABLE() "Vapor mass fraction in hydraulic node i" type: Real [11] 571: dynamicTwoPhaseFlowPipe.pro2[10].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" ) "Vapor mass fraction" type: Real [11] 572: dynamicTwoPhaseFlowPipe.rho2[10]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 573: dynamicTwoPhaseFlowPipe.rhov2[10]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 574: dynamicTwoPhaseFlowPipe.cpl2[10]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 ) "Specific heat capacity in hydraulic node i for the liquid" type: Real [11] 575: dynamicTwoPhaseFlowPipe.lambdav[10]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 576: dynamicTwoPhaseFlowPipe.Rev2[10]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 577: dynamicTwoPhaseFlowPipe.muv2[10]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 578: dynamicTwoPhaseFlowPipe.T2[10]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 579: dynamicTwoPhaseFlowPipe.pro2[10].ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11] 580: $cse30.u:VARIABLE(protected = true ) type: Real unreplaceable 581: dynamicTwoPhaseFlowPipe.pro2[10].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real [11] 582: $cse30.s:VARIABLE(protected = true ) type: Real unreplaceable 583: $cse30.x:VARIABLE(protected = true ) type: Real unreplaceable 584: $cse30.cp:VARIABLE(protected = true ) type: Real unreplaceable 585: $cse30.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 586: dynamicTwoPhaseFlowPipe.hb[10]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 587: dynamicTwoPhaseFlowPipe.h[10]:VARIABLE(start = 237570.17935577242 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 588: dynamicTwoPhaseFlowPipe.h[9]:VARIABLE(start = 219064.17302421754 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 589: dynamicTwoPhaseFlowPipe.h[8]:VARIABLE(start = 200558.16669267463 unit = "J/kg" nominal = 1e6 ) "Fluid specific enthalpy in node i" type: Real [12] 590: dynamicTwoPhaseFlowPipe.Je[8]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 591: dynamicTwoPhaseFlowPipe.Js[8]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 592: dynamicTwoPhaseFlowPipe.rs[8]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 593: dynamicTwoPhaseFlowPipe.Je[9]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 594: dynamicTwoPhaseFlowPipe.re[9]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 595: dynamicTwoPhaseFlowPipe.diff_res_e[9]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 596: dynamicTwoPhaseFlowPipe.kl2[9]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 597: dynamicTwoPhaseFlowPipe.filo[9]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 598: dynamicTwoPhaseFlowPipe.lambdal[9]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 599: dynamicTwoPhaseFlowPipe.Rel2[9]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 600: dynamicTwoPhaseFlowPipe.mul2[9]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 601: dynamicTwoPhaseFlowPipe.T2[9]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 602: dynamicTwoPhaseFlowPipe.muv2[9]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 603: dynamicTwoPhaseFlowPipe.Rev2[9]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 604: dynamicTwoPhaseFlowPipe.lambdav[9]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 605: dynamicTwoPhaseFlowPipe.Pb[9]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 606: $cse16:VARIABLE(protected = true ) type: Real unreplaceable 607: dynamicTwoPhaseFlowPipe.P[9]:VARIABLE(min = 0.0 start = 154915.84935981 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 608: $cse29.u:VARIABLE(protected = true ) type: Real unreplaceable 609: $cse29.cp:VARIABLE(protected = true ) type: Real unreplaceable 610: $cse29.ddhp:VARIABLE(protected = true ) type: Real unreplaceable 611: $cse29.d:VARIABLE(protected = true ) type: Real unreplaceable 612: $cse29.duph:VARIABLE(protected = true ) type: Real unreplaceable 613: $cse29.duhp:VARIABLE(protected = true ) type: Real unreplaceable 614: $cse29.s:VARIABLE(protected = true ) type: Real unreplaceable 615: $cse29.T:VARIABLE(protected = true ) type: Real unreplaceable 616: $cse29.ddph:VARIABLE(protected = true ) type: Real unreplaceable 617: dynamicTwoPhaseFlowPipe.hb[9]:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy at the boundary of node i" type: Real [11] 618: dynamicTwoPhaseFlowPipe.J[9]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] 619: dynamicTwoPhaseFlowPipe.Js[9]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 620: dynamicTwoPhaseFlowPipe.rs[9]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 621: dynamicTwoPhaseFlowPipe.gamma_s[10]:VARIABLE(unit = "kg/s" ) "Diffusion conductance at outlet of thermal node i" type: Real [10] 622: dynamicTwoPhaseFlowPipe.kl2[11]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 623: dynamicTwoPhaseFlowPipe.lambdal[11]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 624: dynamicTwoPhaseFlowPipe.Rel2[11]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 625: dynamicTwoPhaseFlowPipe.mul2[11]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 626: dynamicTwoPhaseFlowPipe.rhol2[11]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 627: dynamicTwoPhaseFlowPipe.diff_res_s[10]:VARIABLE() "Diffusion resistance at outlet of thermal node i" type: Real [10] 628: dynamicTwoPhaseFlowPipe.rs[10]:VARIABLE() "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10] 629: dynamicTwoPhaseFlowPipe.Js[10]:VARIABLE(unit = "W" ) "Thermal power diffusion from outlet of thermal node i" type: Real [10] 630: dynamicTwoPhaseFlowPipe.Je[10]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 631: dynamicTwoPhaseFlowPipe.re[10]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 632: dynamicTwoPhaseFlowPipe.diff_res_e[10]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 633: dynamicTwoPhaseFlowPipe.kl2[10]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 634: dynamicTwoPhaseFlowPipe.rhol2[10]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 ) "Fluid density in hydraulic node i for the liquid" type: Real [11] 635: dynamicTwoPhaseFlowPipe.mul2[10]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 636: dynamicTwoPhaseFlowPipe.Rel2[10]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 637: dynamicTwoPhaseFlowPipe.lambdal[10]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 638: dynamicTwoPhaseFlowPipe.filo[10]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 639: dynamicTwoPhaseFlowPipe.Pb[10]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 640: $cse18:VARIABLE(protected = true ) type: Real unreplaceable 641: dynamicTwoPhaseFlowPipe.P[10]:VARIABLE(min = 0.0 start = 136649.96881108 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 642: $cse30.T:VARIABLE(protected = true ) type: Real unreplaceable 643: $cse30.ddph:VARIABLE(protected = true ) type: Real unreplaceable 644: $cse30.duhp:VARIABLE(protected = true ) type: Real unreplaceable 645: $cse30.duph:VARIABLE(protected = true ) type: Real unreplaceable 646: $cse30.d:VARIABLE(protected = true ) type: Real unreplaceable 647: dynamicTwoPhaseFlowPipe.Pb[11]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Bounded fluid pressure in node i" type: Real [12] 648: $cse20:VARIABLE(protected = true ) type: Real unreplaceable 649: dynamicTwoPhaseFlowPipe.P[11]:VARIABLE(min = 0.0 start = 118345.52340716 unit = "Pa" nominal = 1e5 ) "Fluid pressure in node i" type: Real [12] 650: dynamicTwoPhaseFlowPipe.lsat2[11].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 ) "Temperature" type: Real [11] 651: dynamicTwoPhaseFlowPipe.lsat2[11].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 652: dynamicTwoPhaseFlowPipe.vsat2[11].cv:VARIABLE(unit = "J/(kg.K)" ) "Specific heat capacity at constant volume" type: Real [11] 653: dynamicTwoPhaseFlowPipe.vsat2[11].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 654: dynamicTwoPhaseFlowPipe.lsat2[11].pt:VARIABLE() "Derivative of pressure wrt. temperature" type: Real [11] 655: dynamicTwoPhaseFlowPipe.vsat2[11].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Pressure" type: Real [11] 656: dynamicTwoPhaseFlowPipe.lsat2[11].h:VARIABLE(unit = "J/kg" ) "Specific enthalpy" type: Real [11] 657: dynamicTwoPhaseFlowPipe.vsat2[11].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 658: dynamicTwoPhaseFlowPipe.lsat2[11].rho:VARIABLE(min = 0.0 unit = "kg/m3" ) "Density" type: Real [11] 659: dynamicTwoPhaseFlowPipe.dpf[11]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 660: dynamicTwoPhaseFlowPipe.khi[11]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 661: dynamicTwoPhaseFlowPipe.filo[11]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 662: dynamicTwoPhaseFlowPipe.lambdav[11]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the vapor)" type: Real [11] 663: dynamicTwoPhaseFlowPipe.Rev2[11]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 ) "Reynolds number in hydraulic node i for the vapor" type: Real [11] 664: dynamicTwoPhaseFlowPipe.muv2[11]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 ) "Dynamic viscosity in hydraulic node i for the vapor" type: Real [11] 665: dynamicTwoPhaseFlowPipe.rhov2[11]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i for the vapor" type: Real [11] 666: dynamicTwoPhaseFlowPipe.rho2[11]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 ) "Fluid density in hydraulic node i" type: Real [11] 667: dynamicTwoPhaseFlowPipe.dpg[11]:VARIABLE(unit = "Pa" ) "Gravity pressure loss in node i" type: Real [11] 668: $DER.dynamicTwoPhaseFlowPipe.Q[11]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 669: dynamicTwoPhaseFlowPipe.Q[2]:STATE(1)(start = 378.2555714391421 unit = "kg/s" nominal = 10.0 ) "Mass flow rate in node i" type: Real [11] 670: $DER.dynamicTwoPhaseFlowPipe.Q[1]:DUMMY_DER(fixed = false ) "Mass flow rate in node i" type: Real [11] 671: dynamicTwoPhaseFlowPipe.dpf[1]:VARIABLE(unit = "Pa" ) "Friction pressure loss in node i" type: Real [11] 672: dynamicTwoPhaseFlowPipe.khi[1]:VARIABLE() "Hydraulic pressure loss coefficient in node i" type: Real [11] 673: dynamicTwoPhaseFlowPipe.filo[1]:VARIABLE() "Pressure loss coefficient for two-phase flow" type: Real [11] 674: dynamicTwoPhaseFlowPipe.lambdal[1]:VARIABLE(start = 0.03 nominal = 0.03 ) "Friction pressure loss coefficient in node i for the liquid" type: Real [11] 675: dynamicTwoPhaseFlowPipe.Rel2[1]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 ) "Reynolds number in hydraulic node i for the liquid" type: Real [11] 676: dynamicTwoPhaseFlowPipe.mul2[1]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 ) "Dynamic viscosity in hydraulic node i for the liquid" type: Real [11] 677: dynamicTwoPhaseFlowPipe.T2[1]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 ) "Fluid temperature in hydraulic node i" type: Real [11] 678: dynamicTwoPhaseFlowPipe.kl2[1]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 ) "Thermal conductivity in hydraulic node i for the liquid" type: Real [11] 679: dynamicTwoPhaseFlowPipe.diff_res_e[1]:VARIABLE() "Diffusion resistance at inlet of thermal node i" type: Real [10] 680: dynamicTwoPhaseFlowPipe.re[1]:VARIABLE() "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10] 681: dynamicTwoPhaseFlowPipe.Je[1]:VARIABLE(unit = "W" ) "Thermal power diffusion from inlet of thermal node i" type: Real [10] 682: dynamicTwoPhaseFlowPipe.J[1]:VARIABLE(unit = "W" ) "Total thermal power diffusion of thermal node i" type: Real [10] [/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9805:5-9806:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function: omc_DAEMode_traverserStrongComponents Notification: Performance of postOpt createDAEmodeBDAE (simulation): time 0.07439/5.154, allocations: 230.4 MB / 1.78 GB, free: 50.27 MB / 0.8888 GB Error: post-optimization module createDAEmodeBDAE (simulation) failed. Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicTwoPhaseFlowPipe could not be translated