Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDiffusion_DynamicTwoPhaseFlowPipe.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.TestDiffusion_DynamicTwoPhaseFlowPipe,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDiffusion_DynamicTwoPhaseFlowPipe")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDiffusion_DynamicTwoPhaseFlowPipe,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDiffusion_DynamicTwoPhaseFlowPipe")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.7933/0.7933, allocations: 150.9 MB / 167.2 MB, free: 14.65 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003897/0.0003896, allocations: 17.22 kB / 237.8 MB, free: 1.707 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.06171/0.06213, allocations: 31.35 MB / 269.1 MB, free: 7.035 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.TestDiffusion_DynamicTwoPhaseFlowPipe): time 1.601/1.663, allocations: 300.4 MB / 0.5561 GB, free: 7.434 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5292/2.192, allocations: 195.7 MB / 0.7473 GB, free: 14.77 MB / 0.6075 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001285/2.193, allocations: 34.03 kB / 0.7473 GB, free: 14.77 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/PressureLosses/SwitchValve.mo:36:3-37:55: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/PressureLosses/SwitchValve.mo:38:3-40:35: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/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/SourceQ.mo:62:3-63:65: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 0.001057/2.194, allocations: 472.8 kB / 0.7478 GB, free: 14.77 MB / 0.6075 GB
Notification: Performance of NFTyping.typeBindings: time 0.002621/2.197, allocations: 1.279 MB / 0.749 GB, free: 14.75 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.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Properties/Fluid/derDensity_derP_derh.mo:63:5-63:84:writable] Warning: T 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 0.03282/2.23, allocations: 13.54 MB / 0.7623 GB, free: 13.61 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.01635/2.246, allocations: 20.89 MB / 0.7827 GB, free: 8.84 MB / 0.6075 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.009885/2.256, allocations: 6.892 MB / 0.7894 GB, free: 6.043 MB / 0.6075 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0104/2.267, allocations: 6.738 MB / 0.796 GB, free: 3.23 MB / 0.6075 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.01271/2.279, allocations: 7.872 MB / 0.8036 GB, free: 14.99 MB / 0.6231 GB
Notification: Performance of NFPackage.collectConstants: time 0.004613/2.284, allocations: 1.258 MB / 0.8049 GB, free: 13.73 MB / 0.6231 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.04351/2.328, allocations: 22.75 MB / 0.8271 GB, free: 7.238 MB / 0.6387 GB
Notification: Performance of NFScalarize.scalarize: time 0.007267/2.335, allocations: 4.978 MB / 0.832 GB, free: 2.359 MB / 0.6387 GB
Notification: Performance of NFVerifyModel.verify: time 0.01218/2.347, allocations: 6.361 MB / 0.8382 GB, free: 12.08 MB / 0.6544 GB
Notification: Performance of NFConvertDAE.convert: time 0.04438/2.391, allocations: 26.04 MB / 0.8636 GB, free: 3.121 MB / 0.67 GB
Notification: Performance of FrontEnd - DAE generated: time 6.472e-06/2.391, allocations: 7.938 kB / 0.8636 GB, free: 3.113 MB / 0.67 GB
Notification: Performance of FrontEnd: time 2.284e-06/2.392, allocations: 0 / 0.8636 GB, free: 3.113 MB / 0.67 GB
Notification: Performance of Transformations before backend: time 0.0004493/2.392, allocations: 0 / 0.8636 GB, free: 3.113 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: 3006
 * Number of variables: 3006
Notification: Performance of Generate backend data structure: time 0.06682/2.459, allocations: 16.67 MB / 0.8799 GB, free: 2.352 MB / 0.6856 GB
Notification: Performance of prepare preOptimizeDAE: time 5.379e-05/2.459, allocations: 15.88 kB / 0.8799 GB, free: 2.336 MB / 0.6856 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.005925/2.465, allocations: 1.062 MB / 0.8809 GB, free: 1.262 MB / 0.6856 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.01121/2.476, allocations: 4.177 MB / 0.885 GB, free: 13.03 MB / 0.7012 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.00639/2.482, allocations: 4.372 MB / 0.8893 GB, free: 8 MB / 0.7012 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.004443/2.487, allocations: 0.75 MB / 0.89 GB, free: 7.25 MB / 0.7012 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.06283/2.55, allocations: 21.36 MB / 0.9109 GB, free: 1.816 MB / 0.7169 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0003991/2.55, allocations: 0 / 0.9109 GB, free: 1.816 MB / 0.7169 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.005172/2.555, allocations: 324 kB / 0.9112 GB, free: 1.5 MB / 0.7169 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.0003534/2.556, allocations: 307.8 kB / 0.9115 GB, free: 1.199 MB / 0.7169 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.08228/2.638, allocations: 31.13 MB / 0.9419 GB, free: 2.031 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 0.1518/2.79, allocations: 73.76 MB / 1.014 GB, free: 4.746 MB / 0.8262 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.4837/3.274, allocations: 24.02 MB / 1.037 GB, free: 415.9 MB / 0.8263 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.03486/3.309, allocations: 16.39 MB / 1.053 GB, free: 413.1 MB / 0.8263 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.2729/3.581, allocations: 172.8 MB / 1.222 GB, free: 236.9 MB / 0.8263 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002317/3.582, allocations: 173.6 kB / 1.222 GB, free: 236.8 MB / 0.8263 GB
Notification: Performance of pre-optimization done (n=2307): time 1.639e-05/3.582, allocations: 0 / 1.222 GB, free: 236.8 MB / 0.8263 GB
Notification: Performance of matching and sorting (n=2307): time 0.1358/3.718, allocations: 56.27 MB / 1.277 GB, free: 180.2 MB / 0.8263 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0001136/3.718, allocations: 271.1 kB / 1.278 GB, free: 179.9 MB / 0.8263 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.002217/3.72, allocations: 1.966 MB / 1.279 GB, free: 177.9 MB / 0.8263 GB
Notification: Performance of collectPreVariables (initialization): time 0.003565/3.723, allocations: 241.6 kB / 1.28 GB, free: 177.7 MB / 0.8263 GB
Notification: Performance of collectInitialEqns (initialization): time 0.000739/3.724, allocations: 1.349 MB / 1.281 GB, free: 176.4 MB / 0.8263 GB
Notification: Performance of collectInitialBindings (initialization): time 0.007074/3.731, allocations: 7.538 MB / 1.288 GB, free: 168.9 MB / 0.8263 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.01039/3.742, allocations: 2.87 MB / 1.291 GB, free: 166 MB / 0.8263 GB
Notification: Performance of setup shared object (initialization): time 4.567e-05/3.742, allocations: 305.1 kB / 1.291 GB, free: 165.7 MB / 0.8263 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.03269/3.774, allocations: 13.92 MB / 1.305 GB, free: 151.8 MB / 0.8263 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.03542/3.81, allocations: 15.6 MB / 1.32 GB, free: 135.9 MB / 0.8263 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.06377/3.874, allocations: 29.58 MB / 1.349 GB, free: 105.9 MB / 0.8263 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 6.358e-05/3.874, allocations: 9.625 kB / 1.349 GB, free: 105.9 MB / 0.8263 GB
Notification: Performance of matching and sorting (n=2410) (initialization): time 0.09906/3.973, allocations: 40.18 MB / 1.388 GB, free: 65.6 MB / 0.8263 GB
Notification: Performance of prepare postOptimizeDAE: time 7.182e-05/3.973, allocations: 75.34 kB / 1.389 GB, free: 65.52 MB / 0.8263 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.0001899/3.973, allocations: 60.22 kB / 1.389 GB, free: 65.46 MB / 0.8263 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.1482/4.121, allocations: 60.58 MB / 1.448 GB, free: 4.781 MB / 0.8263 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.01828/4.14, allocations: 3.056 MB / 1.451 GB, free: 1.793 MB / 0.8263 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.2953/4.435, allocations: 61.19 MB / 1.51 GB, free: 376.8 MB / 0.8263 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01948/4.455, allocations: 3.135 MB / 1.514 GB, free: 375.9 MB / 0.8263 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.004648/4.459, allocations: 0.6355 MB / 1.514 GB, free: 375.8 MB / 0.8263 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 95
 * Number of states: 0 ()
 * Number of discrete variables: 17 (sourceP1.C.ftype,dynamicTwoPhaseFlowPipe1.fluid,sinkP1.fluid,sourceP1.fluid1,sourceP.C.ftype,switchValve.C2.diff_on_1,dynamicTwoPhaseFlowPipe.fluid,sinkP.fluid,switchValve.fluid,nONL.yL.signal,echelon.yL.signal,sourceP.fluid1,dynamicTwoPhaseFlowPipe1.C1.diff_on_2,dynamicTwoPhaseFlowPipe1.C2.diff_on_1,dynamicTwoPhaseFlowPipe.C1.diff_on_2,sourceP.C.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 (717):
 * Single equations (assignments): 671
 * Array equations: 0
 * Algorithm blocks: 2
 * Record equations: 22
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 22
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 20 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%), (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
   {(32,313), (33,317)}
Notification: Performance of prepare postOptimizeDAE: time 0.01038/4.47, allocations: 2.597 MB / 1.517 GB, free: 374.7 MB / 0.8263 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.004544/4.474, allocations: 0.8081 MB / 1.517 GB, free: 374.3 MB / 0.8263 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1114/4.586, allocations: 48.9 MB / 1.565 GB, free: 343.7 MB / 0.8263 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0004022/4.586, allocations: 63.75 kB / 1.565 GB, free: 343.6 MB / 0.8263 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.0001512/4.586, allocations: 47.31 kB / 1.565 GB, free: 343.6 MB / 0.8263 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.009876/4.596, allocations: 3.68 MB / 1.569 GB, free: 339.9 MB / 0.8263 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0054/4.602, allocations: 235.8 kB / 1.569 GB, free: 339.7 MB / 0.8263 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.01822/4.62, allocations: 2.143 MB / 1.571 GB, free: 337.5 MB / 0.8263 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.005/4.625, allocations: 0.9309 MB / 1.572 GB, free: 336.6 MB / 0.8263 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 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[1], dynamicTwoPhaseFlowPipe1.rhoc[2], dynamicTwoPhaseFlowPipe1.pro1[1].u, dynamicTwoPhaseFlowPipe1.pro1[1].s, dynamicTwoPhaseFlowPipe1.pro1[1].cp, dynamicTwoPhaseFlowPipe1.pro1[1].ddhp, dynamicTwoPhaseFlowPipe1.pro1[1].ddph, dynamicTwoPhaseFlowPipe1.pro1[1].duph, dynamicTwoPhaseFlowPipe1.pro1[1].duhp, dynamicTwoPhaseFlowPipe1.pro1[1].x) = $cse38

Variables:
1: dynamicTwoPhaseFlowPipe1.pro1[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
2: dynamicTwoPhaseFlowPipe1.pro1[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
3: dynamicTwoPhaseFlowPipe1.T1[1]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
4: dynamicTwoPhaseFlowPipe1.pro1[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
5: dynamicTwoPhaseFlowPipe1.pro1[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
6: dynamicTwoPhaseFlowPipe1.pro1[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
7: dynamicTwoPhaseFlowPipe1.pro1[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
8: dynamicTwoPhaseFlowPipe1.pro1[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
9: dynamicTwoPhaseFlowPipe1.h[1]:VARIABLE(start = 84011.8111671368 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
10: dynamicTwoPhaseFlowPipe1.proc[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [2]
[/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 = dynamicTwoPhaseFlowPipe1.hb[1] * sourceP1.Q0 + heatSource1.W0[1] + dynamicTwoPhaseFlowPipe1.J[1] - dynamicTwoPhaseFlowPipe1.hb[2] * sourceP1.Q0
2/2 (1): dynamicTwoPhaseFlowPipe1.J[1] = dynamicTwoPhaseFlowPipe1.Je[1] + dynamicTwoPhaseFlowPipe1.Js[1]
3/3 (1): dynamicTwoPhaseFlowPipe1.Je[1] = if sourceP1.diffusion then dynamicTwoPhaseFlowPipe1.re[1] * dynamicTwoPhaseFlowPipe1.gamma_e[1] * (dynamicTwoPhaseFlowPipe1.h[1] - dynamicTwoPhaseFlowPipe1.h[2]) else 0.0
4/4 (1): dynamicTwoPhaseFlowPipe1.gamma_e[1] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[1]
5/5 (1): dynamicTwoPhaseFlowPipe1.re[1] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[1]) ^ 2.0)
6/6 (1): dynamicTwoPhaseFlowPipe1.diff_res_t = dynamicTwoPhaseFlowPipe1.diff_res_e[1] + dynamicTwoPhaseFlowPipe1.diff_res_e[2] + dynamicTwoPhaseFlowPipe1.diff_res_e[3] + dynamicTwoPhaseFlowPipe1.diff_res_e[4] + dynamicTwoPhaseFlowPipe1.diff_res_e[5] + dynamicTwoPhaseFlowPipe1.diff_res_e[6] + dynamicTwoPhaseFlowPipe1.diff_res_e[7] + dynamicTwoPhaseFlowPipe1.diff_res_e[8] + dynamicTwoPhaseFlowPipe1.diff_res_e[9] + dynamicTwoPhaseFlowPipe1.diff_res_e[10] + dynamicTwoPhaseFlowPipe1.diff_res_s[10]
7/7 (1): dynamicTwoPhaseFlowPipe1.hb[1] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_t, dynamicTwoPhaseFlowPipe1.h[1], dynamicTwoPhaseFlowPipe1.h[2], 1.0)
8/8 (1): dynamicTwoPhaseFlowPipe1.hb[2] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[2], dynamicTwoPhaseFlowPipe1.h[2], dynamicTwoPhaseFlowPipe1.h[3], 1.0)
9/9 (10): $cse59 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[2] + dynamicTwoPhaseFlowPipe1.P[3]), dynamicTwoPhaseFlowPipe1.hb[2], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
10/19 (10): $cse38 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[2], dynamicTwoPhaseFlowPipe1.h[2], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
11/29 (1): dynamicTwoPhaseFlowPipe1.dpa[2] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[3] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[2]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
12/30 (1): dynamicTwoPhaseFlowPipe1.dpa[3] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[4] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[3]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
13/31 (1): dynamicTwoPhaseFlowPipe1.P[3] + (-dynamicTwoPhaseFlowPipe1.dpg[3]) - dynamicTwoPhaseFlowPipe1.dpa[3] - dynamicTwoPhaseFlowPipe1.dpf[3] - dynamicTwoPhaseFlowPipe1.P[4] = 0.0
14/32 (1): dynamicTwoPhaseFlowPipe1.dpf[3] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[3] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[3])
15/33 (1): dynamicTwoPhaseFlowPipe1.khi[3] = dynamicTwoPhaseFlowPipe1.filo[3] * dynamicTwoPhaseFlowPipe1.lambdal[3] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
16/34 (1): dynamicTwoPhaseFlowPipe1.filo[3] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[3] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[3] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[3] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[3] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[3]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[3]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[3] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[3] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[3]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[3])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[3] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[3] * dynamicTwoPhaseFlowPipe1.lambdav[3] / (dynamicTwoPhaseFlowPipe1.lambdal[3] * dynamicTwoPhaseFlowPipe1.rhov2[3])
17/35 (1): dynamicTwoPhaseFlowPipe1.lambdal[3] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[3] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[3] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
18/36 (1): dynamicTwoPhaseFlowPipe1.Rel2[3] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[3]))
19/37 (1): dynamicTwoPhaseFlowPipe1.mul2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[3], dynamicTwoPhaseFlowPipe1.T2[3], dynamicTwoPhaseFlowPipe1.fluid)
20/38 (1): dynamicTwoPhaseFlowPipe1.kl2[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[3], dynamicTwoPhaseFlowPipe1.T2[3], 0.5 * (dynamicTwoPhaseFlowPipe1.P[3] + dynamicTwoPhaseFlowPipe1.P[4]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
21/39 (1): dynamicTwoPhaseFlowPipe1.muv2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[3], dynamicTwoPhaseFlowPipe1.T2[3], dynamicTwoPhaseFlowPipe1.fluid)
22/40 (1): dynamicTwoPhaseFlowPipe1.Rev2[3] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[3]))
23/41 (1): dynamicTwoPhaseFlowPipe1.lambdav[3] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[3] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[3] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
24/42 (1): dynamicTwoPhaseFlowPipe1.cpl2[3] = if noEvent(dynamicTwoPhaseFlowPipe1.P[4] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[3] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[3].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[3] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[3].cp else dynamicTwoPhaseFlowPipe1.lsat2[3].cp
25/43 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[3] = dynamicTwoPhaseFlowPipe1.rho2[3] * dynamicTwoPhaseFlowPipe1.cpl2[3] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[3] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[3])
26/44 (1): dynamicTwoPhaseFlowPipe1.rhov2[3] = if noEvent(dynamicTwoPhaseFlowPipe1.P[4] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[3] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[3] else min(dynamicTwoPhaseFlowPipe1.rho2[3], dynamicTwoPhaseFlowPipe1.vsat2[3].rho)
27/45 (1): dynamicTwoPhaseFlowPipe1.rhol2[3] = if noEvent(dynamicTwoPhaseFlowPipe1.P[4] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[3] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[3] else max(dynamicTwoPhaseFlowPipe1.rho2[3], dynamicTwoPhaseFlowPipe1.lsat2[3].rho)
28/46 (1): dynamicTwoPhaseFlowPipe1.xv2[3] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[3] + dynamicTwoPhaseFlowPipe1.P[4]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[3] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[3].x
29/47 (1): dynamicTwoPhaseFlowPipe1.hb[3] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[3], dynamicTwoPhaseFlowPipe1.h[3], dynamicTwoPhaseFlowPipe1.h[4], 1.0)
30/48 (1): dynamicTwoPhaseFlowPipe1.gamma[3] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[3]
31/49 (1): dynamicTwoPhaseFlowPipe1.re[3] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[3]) ^ 2.0)
32/50 (1): dynamicTwoPhaseFlowPipe1.Je[3] = dynamicTwoPhaseFlowPipe1.re[3] * dynamicTwoPhaseFlowPipe1.gamma_e[3] * (dynamicTwoPhaseFlowPipe1.h[3] - dynamicTwoPhaseFlowPipe1.h[4])
33/51 (10): $cse40 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[3], dynamicTwoPhaseFlowPipe1.h[3], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
34/61 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[2], dynamicTwoPhaseFlowPipe1.rhoc[3], dynamicTwoPhaseFlowPipe1.pro1[2].u, dynamicTwoPhaseFlowPipe1.pro1[2].s, dynamicTwoPhaseFlowPipe1.pro1[2].cp, dynamicTwoPhaseFlowPipe1.pro1[2].ddhp, dynamicTwoPhaseFlowPipe1.pro1[2].ddph, dynamicTwoPhaseFlowPipe1.pro1[2].duph, dynamicTwoPhaseFlowPipe1.pro1[2].duhp, dynamicTwoPhaseFlowPipe1.pro1[2].x) = $cse40
35/71 (1): $cse41 = min(dynamicTwoPhaseFlowPipe1.P[3], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
36/72 (1): dynamicTwoPhaseFlowPipe1.Pb[3] = max($cse41, dynamicTwoPhaseFlowPipe1.ptriple)
37/73 (14): (dynamicTwoPhaseFlowPipe1.lsat2[2], dynamicTwoPhaseFlowPipe1.vsat2[2]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[2] + dynamicTwoPhaseFlowPipe1.P[3]), dynamicTwoPhaseFlowPipe1.fluid)
38/87 (1): dynamicTwoPhaseFlowPipe1.rhol2[2] = if noEvent(dynamicTwoPhaseFlowPipe1.P[3] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[2] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[2] else max(dynamicTwoPhaseFlowPipe1.rho2[2], dynamicTwoPhaseFlowPipe1.lsat2[2].rho)
39/88 (1): dynamicTwoPhaseFlowPipe1.mul2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[2], dynamicTwoPhaseFlowPipe1.T2[2], dynamicTwoPhaseFlowPipe1.fluid)
40/89 (1): dynamicTwoPhaseFlowPipe1.Rel2[2] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[2]))
41/90 (1): dynamicTwoPhaseFlowPipe1.lambdal[2] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[2] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[2] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
42/91 (1): dynamicTwoPhaseFlowPipe1.filo[2] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[2] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[2] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[2] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[2] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[2]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[2]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[2] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[2] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[2]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[2])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[2] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[2] * dynamicTwoPhaseFlowPipe1.lambdav[2] / (dynamicTwoPhaseFlowPipe1.lambdal[2] * dynamicTwoPhaseFlowPipe1.rhov2[2])
43/92 (1): dynamicTwoPhaseFlowPipe1.khi[2] = dynamicTwoPhaseFlowPipe1.filo[2] * dynamicTwoPhaseFlowPipe1.lambdal[2] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
44/93 (1): dynamicTwoPhaseFlowPipe1.dpf[2] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[2] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[2])
45/94 (1): dynamicTwoPhaseFlowPipe1.P[2] + (-dynamicTwoPhaseFlowPipe1.dpg[2]) - dynamicTwoPhaseFlowPipe1.dpa[2] - dynamicTwoPhaseFlowPipe1.dpf[2] - dynamicTwoPhaseFlowPipe1.P[3] = 0.0
46/95 (1): dynamicTwoPhaseFlowPipe1.kl2[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[2], dynamicTwoPhaseFlowPipe1.T2[2], 0.5 * (dynamicTwoPhaseFlowPipe1.P[2] + dynamicTwoPhaseFlowPipe1.P[3]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
47/96 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[2] = dynamicTwoPhaseFlowPipe1.rho2[2] * dynamicTwoPhaseFlowPipe1.cpl2[2] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[2] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[2])
48/97 (1): dynamicTwoPhaseFlowPipe1.rhov2[2] = if noEvent(dynamicTwoPhaseFlowPipe1.P[3] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[2] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[2] else min(dynamicTwoPhaseFlowPipe1.rho2[2], dynamicTwoPhaseFlowPipe1.vsat2[2].rho)
49/98 (1): dynamicTwoPhaseFlowPipe1.muv2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[2], dynamicTwoPhaseFlowPipe1.T2[2], dynamicTwoPhaseFlowPipe1.fluid)
50/99 (1): dynamicTwoPhaseFlowPipe1.Rev2[2] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[2]))
51/100 (1): dynamicTwoPhaseFlowPipe1.lambdav[2] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[2] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[2] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
52/101 (1): dynamicTwoPhaseFlowPipe1.xv2[2] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[2] + dynamicTwoPhaseFlowPipe1.P[3]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[2] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[2].x
53/102 (1): dynamicTwoPhaseFlowPipe1.cpl2[2] = if noEvent(dynamicTwoPhaseFlowPipe1.P[3] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[2] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[2].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[2] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[2].cp else dynamicTwoPhaseFlowPipe1.lsat2[2].cp
54/103 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[2], dynamicTwoPhaseFlowPipe1.rho2[2], dynamicTwoPhaseFlowPipe1.pro2[2].u, dynamicTwoPhaseFlowPipe1.pro2[2].s, dynamicTwoPhaseFlowPipe1.pro2[2].cp, dynamicTwoPhaseFlowPipe1.pro2[2].ddhp, dynamicTwoPhaseFlowPipe1.pro2[2].ddph, dynamicTwoPhaseFlowPipe1.pro2[2].duph, dynamicTwoPhaseFlowPipe1.pro2[2].duhp, dynamicTwoPhaseFlowPipe1.pro2[2].x) = $cse59
55/113 (1): dynamicTwoPhaseFlowPipe1.dpg[2] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[2] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
56/114 (1): dynamicTwoPhaseFlowPipe1.hb[4] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[4], dynamicTwoPhaseFlowPipe1.h[4], dynamicTwoPhaseFlowPipe1.h[5], 1.0)
57/115 (1): dynamicTwoPhaseFlowPipe1.gamma[4] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[4]
58/116 (1): dynamicTwoPhaseFlowPipe1.re[4] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[4]) ^ 2.0)
59/117 (1): dynamicTwoPhaseFlowPipe1.Je[4] = dynamicTwoPhaseFlowPipe1.re[4] * dynamicTwoPhaseFlowPipe1.gamma_e[4] * (dynamicTwoPhaseFlowPipe1.h[4] - dynamicTwoPhaseFlowPipe1.h[5])
60/118 (1): dynamicTwoPhaseFlowPipe1.J[4] = dynamicTwoPhaseFlowPipe1.Je[4] + dynamicTwoPhaseFlowPipe1.Js[4]
61/119 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[4] * sourceP1.Q0 + heatSource1.W0[4] + dynamicTwoPhaseFlowPipe1.J[4] - dynamicTwoPhaseFlowPipe1.hb[5] * sourceP1.Q0
62/120 (10): $cse61 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[4] + dynamicTwoPhaseFlowPipe1.P[5]), dynamicTwoPhaseFlowPipe1.hb[4], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
63/130 (1): dynamicTwoPhaseFlowPipe1.mul2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[4], dynamicTwoPhaseFlowPipe1.T2[4], dynamicTwoPhaseFlowPipe1.fluid)
64/131 (1): dynamicTwoPhaseFlowPipe1.Rel2[4] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[4]))
65/132 (1): dynamicTwoPhaseFlowPipe1.lambdal[4] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[4] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[4] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
66/133 (1): dynamicTwoPhaseFlowPipe1.filo[4] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[4] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[4] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[4] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[4] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[4]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[4]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[4] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[4] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[4]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[4])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[4] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[4] * dynamicTwoPhaseFlowPipe1.lambdav[4] / (dynamicTwoPhaseFlowPipe1.lambdal[4] * dynamicTwoPhaseFlowPipe1.rhov2[4])
67/134 (1): dynamicTwoPhaseFlowPipe1.khi[4] = dynamicTwoPhaseFlowPipe1.filo[4] * dynamicTwoPhaseFlowPipe1.lambdal[4] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
68/135 (1): dynamicTwoPhaseFlowPipe1.dpf[4] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[4] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[4])
69/136 (1): dynamicTwoPhaseFlowPipe1.P[4] + (-dynamicTwoPhaseFlowPipe1.dpg[4]) - dynamicTwoPhaseFlowPipe1.dpa[4] - dynamicTwoPhaseFlowPipe1.dpf[4] - dynamicTwoPhaseFlowPipe1.P[5] = 0.0
70/137 (1): dynamicTwoPhaseFlowPipe1.dpa[4] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[5] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[4]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
71/138 (10): $cse42 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[4], dynamicTwoPhaseFlowPipe1.h[4], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
72/148 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[3], dynamicTwoPhaseFlowPipe1.rhoc[4], dynamicTwoPhaseFlowPipe1.pro1[3].u, dynamicTwoPhaseFlowPipe1.pro1[3].s, dynamicTwoPhaseFlowPipe1.pro1[3].cp, dynamicTwoPhaseFlowPipe1.pro1[3].ddhp, dynamicTwoPhaseFlowPipe1.pro1[3].ddph, dynamicTwoPhaseFlowPipe1.pro1[3].duph, dynamicTwoPhaseFlowPipe1.pro1[3].duhp, dynamicTwoPhaseFlowPipe1.pro1[3].x) = $cse42
73/158 (1): dynamicTwoPhaseFlowPipe1.muv2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[4], dynamicTwoPhaseFlowPipe1.T2[4], dynamicTwoPhaseFlowPipe1.fluid)
74/159 (1): dynamicTwoPhaseFlowPipe1.Rev2[4] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[4]))
75/160 (1): dynamicTwoPhaseFlowPipe1.lambdav[4] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[4] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[4] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
76/161 (1): dynamicTwoPhaseFlowPipe1.kl2[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[4], dynamicTwoPhaseFlowPipe1.T2[4], 0.5 * (dynamicTwoPhaseFlowPipe1.P[4] + dynamicTwoPhaseFlowPipe1.P[5]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
77/162 (10): $cse44 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[5], dynamicTwoPhaseFlowPipe1.h[5], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
78/172 (1): dynamicTwoPhaseFlowPipe1.dpa[5] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[6] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[5]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
79/173 (1): dynamicTwoPhaseFlowPipe1.P[5] + (-dynamicTwoPhaseFlowPipe1.dpg[5]) - dynamicTwoPhaseFlowPipe1.dpa[5] - dynamicTwoPhaseFlowPipe1.dpf[5] - dynamicTwoPhaseFlowPipe1.P[6] = 0.0
80/174 (1): dynamicTwoPhaseFlowPipe1.dpf[5] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[5] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[5])
81/175 (1): dynamicTwoPhaseFlowPipe1.khi[5] = dynamicTwoPhaseFlowPipe1.filo[5] * dynamicTwoPhaseFlowPipe1.lambdal[5] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
82/176 (1): dynamicTwoPhaseFlowPipe1.filo[5] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[5] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[5] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[5] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[5] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[5]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[5]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[5] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[5] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[5]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[5])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[5] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[5] * dynamicTwoPhaseFlowPipe1.lambdav[5] / (dynamicTwoPhaseFlowPipe1.lambdal[5] * dynamicTwoPhaseFlowPipe1.rhov2[5])
83/177 (1): dynamicTwoPhaseFlowPipe1.lambdal[5] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[5] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[5] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
84/178 (1): dynamicTwoPhaseFlowPipe1.Rel2[5] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[5]))
85/179 (1): dynamicTwoPhaseFlowPipe1.mul2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[5], dynamicTwoPhaseFlowPipe1.T2[5], dynamicTwoPhaseFlowPipe1.fluid)
86/180 (1): dynamicTwoPhaseFlowPipe1.kl2[5] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[5], dynamicTwoPhaseFlowPipe1.T2[5], 0.5 * (dynamicTwoPhaseFlowPipe1.P[5] + dynamicTwoPhaseFlowPipe1.P[6]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
87/181 (1): dynamicTwoPhaseFlowPipe1.muv2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[5], dynamicTwoPhaseFlowPipe1.T2[5], dynamicTwoPhaseFlowPipe1.fluid)
88/182 (1): dynamicTwoPhaseFlowPipe1.Rev2[5] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[5]))
89/183 (1): dynamicTwoPhaseFlowPipe1.lambdav[5] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[5] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[5] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
90/184 (1): dynamicTwoPhaseFlowPipe1.cpl2[5] = if noEvent(dynamicTwoPhaseFlowPipe1.P[6] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[5] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[5].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[5] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[5].cp else dynamicTwoPhaseFlowPipe1.lsat2[5].cp
91/185 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[5] = dynamicTwoPhaseFlowPipe1.rho2[5] * dynamicTwoPhaseFlowPipe1.cpl2[5] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[5] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[5])
92/186 (1): dynamicTwoPhaseFlowPipe1.rhov2[5] = if noEvent(dynamicTwoPhaseFlowPipe1.P[6] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[5] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[5] else min(dynamicTwoPhaseFlowPipe1.rho2[5], dynamicTwoPhaseFlowPipe1.vsat2[5].rho)
93/187 (1): dynamicTwoPhaseFlowPipe1.rhol2[5] = if noEvent(dynamicTwoPhaseFlowPipe1.P[6] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[5] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[5] else max(dynamicTwoPhaseFlowPipe1.rho2[5], dynamicTwoPhaseFlowPipe1.lsat2[5].rho)
94/188 (10): $cse46 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[6], dynamicTwoPhaseFlowPipe1.h[6], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
95/198 (1): dynamicTwoPhaseFlowPipe1.dpa[6] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[7] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[6]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
96/199 (1): dynamicTwoPhaseFlowPipe1.P[6] + (-dynamicTwoPhaseFlowPipe1.dpg[6]) - dynamicTwoPhaseFlowPipe1.dpa[6] - dynamicTwoPhaseFlowPipe1.dpf[6] - dynamicTwoPhaseFlowPipe1.P[7] = 0.0
97/200 (1): dynamicTwoPhaseFlowPipe1.dpf[6] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[6] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[6])
98/201 (1): dynamicTwoPhaseFlowPipe1.khi[6] = dynamicTwoPhaseFlowPipe1.filo[6] * dynamicTwoPhaseFlowPipe1.lambdal[6] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
99/202 (1): dynamicTwoPhaseFlowPipe1.filo[6] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[6] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[6] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[6] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[6] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[6]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[6]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[6] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[6] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[6]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[6])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[6] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[6] * dynamicTwoPhaseFlowPipe1.lambdav[6] / (dynamicTwoPhaseFlowPipe1.lambdal[6] * dynamicTwoPhaseFlowPipe1.rhov2[6])
100/203 (1): dynamicTwoPhaseFlowPipe1.cpl2[6] = if noEvent(dynamicTwoPhaseFlowPipe1.P[7] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[6] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[6].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[6] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[6].cp else dynamicTwoPhaseFlowPipe1.lsat2[6].cp
101/204 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[6] = dynamicTwoPhaseFlowPipe1.rho2[6] * dynamicTwoPhaseFlowPipe1.cpl2[6] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[6] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[6])
102/205 (1): dynamicTwoPhaseFlowPipe1.mul2[6] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[6], dynamicTwoPhaseFlowPipe1.T2[6], dynamicTwoPhaseFlowPipe1.fluid)
103/206 (1): dynamicTwoPhaseFlowPipe1.Rel2[6] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[6]))
104/207 (1): dynamicTwoPhaseFlowPipe1.lambdal[6] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[6] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[6] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
105/208 (1): dynamicTwoPhaseFlowPipe1.kl2[6] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[6], dynamicTwoPhaseFlowPipe1.T2[6], 0.5 * (dynamicTwoPhaseFlowPipe1.P[6] + dynamicTwoPhaseFlowPipe1.P[7]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
106/209 (1): dynamicTwoPhaseFlowPipe1.rhol2[6] = if noEvent(dynamicTwoPhaseFlowPipe1.P[7] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[6] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[6] else max(dynamicTwoPhaseFlowPipe1.rho2[6], dynamicTwoPhaseFlowPipe1.lsat2[6].rho)
107/210 (1): dynamicTwoPhaseFlowPipe1.rhov2[6] = if noEvent(dynamicTwoPhaseFlowPipe1.P[7] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[6] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[6] else min(dynamicTwoPhaseFlowPipe1.rho2[6], dynamicTwoPhaseFlowPipe1.vsat2[6].rho)
108/211 (1): dynamicTwoPhaseFlowPipe1.muv2[6] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[6], dynamicTwoPhaseFlowPipe1.T2[6], dynamicTwoPhaseFlowPipe1.fluid)
109/212 (1): dynamicTwoPhaseFlowPipe1.Rev2[6] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[6]))
110/213 (1): dynamicTwoPhaseFlowPipe1.lambdav[6] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[6] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[6] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
111/214 (10): $cse48 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[7], dynamicTwoPhaseFlowPipe1.h[7], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
112/224 (1): dynamicTwoPhaseFlowPipe1.dpa[7] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[8] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[7]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
113/225 (1): dynamicTwoPhaseFlowPipe1.P[7] + (-dynamicTwoPhaseFlowPipe1.dpg[7]) - dynamicTwoPhaseFlowPipe1.dpa[7] - dynamicTwoPhaseFlowPipe1.dpf[7] - dynamicTwoPhaseFlowPipe1.P[8] = 0.0
114/226 (1): dynamicTwoPhaseFlowPipe1.dpf[7] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[7] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[7])
115/227 (1): dynamicTwoPhaseFlowPipe1.khi[7] = dynamicTwoPhaseFlowPipe1.filo[7] * dynamicTwoPhaseFlowPipe1.lambdal[7] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
116/228 (1): dynamicTwoPhaseFlowPipe1.filo[7] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[7] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[7] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[7] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[7] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[7]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[7]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[7] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[7] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[7]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[7])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[7] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[7] * dynamicTwoPhaseFlowPipe1.lambdav[7] / (dynamicTwoPhaseFlowPipe1.lambdal[7] * dynamicTwoPhaseFlowPipe1.rhov2[7])
117/229 (1): dynamicTwoPhaseFlowPipe1.lambdav[7] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[7] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[7] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
118/230 (1): dynamicTwoPhaseFlowPipe1.Rev2[7] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[7]))
119/231 (1): dynamicTwoPhaseFlowPipe1.muv2[7] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[7], dynamicTwoPhaseFlowPipe1.T2[7], dynamicTwoPhaseFlowPipe1.fluid)
120/232 (1): dynamicTwoPhaseFlowPipe1.mul2[7] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[7], dynamicTwoPhaseFlowPipe1.T2[7], dynamicTwoPhaseFlowPipe1.fluid)
121/233 (1): dynamicTwoPhaseFlowPipe1.Rel2[7] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[7]))
122/234 (1): dynamicTwoPhaseFlowPipe1.lambdal[7] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[7] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[7] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
123/235 (1): dynamicTwoPhaseFlowPipe1.kl2[7] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[7], dynamicTwoPhaseFlowPipe1.T2[7], 0.5 * (dynamicTwoPhaseFlowPipe1.P[7] + dynamicTwoPhaseFlowPipe1.P[8]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
124/236 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[7] = dynamicTwoPhaseFlowPipe1.rho2[7] * dynamicTwoPhaseFlowPipe1.cpl2[7] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[7] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[7])
125/237 (1): dynamicTwoPhaseFlowPipe1.rhol2[7] = if noEvent(dynamicTwoPhaseFlowPipe1.P[8] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[7] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[7] else max(dynamicTwoPhaseFlowPipe1.rho2[7], dynamicTwoPhaseFlowPipe1.lsat2[7].rho)
126/238 (1): dynamicTwoPhaseFlowPipe1.hb[7] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[7], dynamicTwoPhaseFlowPipe1.h[7], dynamicTwoPhaseFlowPipe1.h[8], 1.0)
127/239 (1): dynamicTwoPhaseFlowPipe1.hb[6] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[6], dynamicTwoPhaseFlowPipe1.h[6], dynamicTwoPhaseFlowPipe1.h[7], 1.0)
128/240 (1): dynamicTwoPhaseFlowPipe1.gamma[6] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[6]
129/241 (1): dynamicTwoPhaseFlowPipe1.re[6] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[6]) ^ 2.0)
130/242 (1): dynamicTwoPhaseFlowPipe1.Je[6] = dynamicTwoPhaseFlowPipe1.re[6] * dynamicTwoPhaseFlowPipe1.gamma_e[6] * (dynamicTwoPhaseFlowPipe1.h[6] - dynamicTwoPhaseFlowPipe1.h[7])
131/243 (1): dynamicTwoPhaseFlowPipe1.hb[5] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[5], dynamicTwoPhaseFlowPipe1.h[5], dynamicTwoPhaseFlowPipe1.h[6], 1.0)
132/244 (1): dynamicTwoPhaseFlowPipe1.gamma[5] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[5]
133/245 (1): dynamicTwoPhaseFlowPipe1.re[5] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[5]) ^ 2.0)
134/246 (1): dynamicTwoPhaseFlowPipe1.Je[5] = dynamicTwoPhaseFlowPipe1.re[5] * dynamicTwoPhaseFlowPipe1.gamma_e[5] * (dynamicTwoPhaseFlowPipe1.h[5] - dynamicTwoPhaseFlowPipe1.h[6])
135/247 (1): dynamicTwoPhaseFlowPipe1.Js[4] = dynamicTwoPhaseFlowPipe1.rs[4] * dynamicTwoPhaseFlowPipe1.gamma_s[4] * (dynamicTwoPhaseFlowPipe1.h[6] - dynamicTwoPhaseFlowPipe1.h[5])
136/248 (1): dynamicTwoPhaseFlowPipe1.Js[3] = dynamicTwoPhaseFlowPipe1.rs[3] * dynamicTwoPhaseFlowPipe1.gamma_s[3] * (dynamicTwoPhaseFlowPipe1.h[5] - dynamicTwoPhaseFlowPipe1.h[4])
137/249 (1): dynamicTwoPhaseFlowPipe1.J[3] = dynamicTwoPhaseFlowPipe1.Je[3] + dynamicTwoPhaseFlowPipe1.Js[3]
138/250 (1): dynamicTwoPhaseFlowPipe1.rs[4] = dynamicTwoPhaseFlowPipe1.re[5]
139/251 (1): dynamicTwoPhaseFlowPipe1.gamma_e[5] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[5]
140/252 (1): dynamicTwoPhaseFlowPipe1.gamma_s[4] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[5]
141/253 (1): dynamicTwoPhaseFlowPipe1.Js[5] = dynamicTwoPhaseFlowPipe1.rs[5] * dynamicTwoPhaseFlowPipe1.gamma_s[5] * (dynamicTwoPhaseFlowPipe1.h[7] - dynamicTwoPhaseFlowPipe1.h[6])
142/254 (1): dynamicTwoPhaseFlowPipe1.J[5] = dynamicTwoPhaseFlowPipe1.Je[5] + dynamicTwoPhaseFlowPipe1.Js[5]
143/255 (1): dynamicTwoPhaseFlowPipe1.rs[5] = dynamicTwoPhaseFlowPipe1.re[6]
144/256 (1): dynamicTwoPhaseFlowPipe1.gamma_e[6] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[6]
145/257 (1): dynamicTwoPhaseFlowPipe1.gamma_s[5] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[6]
146/258 (1): dynamicTwoPhaseFlowPipe1.Je[7] = dynamicTwoPhaseFlowPipe1.re[7] * dynamicTwoPhaseFlowPipe1.gamma_e[7] * (dynamicTwoPhaseFlowPipe1.h[7] - dynamicTwoPhaseFlowPipe1.h[8])
147/259 (1): dynamicTwoPhaseFlowPipe1.re[7] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[7]) ^ 2.0)
148/260 (1): dynamicTwoPhaseFlowPipe1.gamma[7] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[7]
149/261 (1): dynamicTwoPhaseFlowPipe1.gamma_e[7] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[7]
150/262 (1): dynamicTwoPhaseFlowPipe1.gamma_s[6] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[7]
151/263 (1): dynamicTwoPhaseFlowPipe1.Js[6] = dynamicTwoPhaseFlowPipe1.rs[6] * dynamicTwoPhaseFlowPipe1.gamma_s[6] * (dynamicTwoPhaseFlowPipe1.h[8] - dynamicTwoPhaseFlowPipe1.h[7])
152/264 (1): dynamicTwoPhaseFlowPipe1.J[6] = dynamicTwoPhaseFlowPipe1.Je[6] + dynamicTwoPhaseFlowPipe1.Js[6]
153/265 (1): dynamicTwoPhaseFlowPipe1.rs[6] = dynamicTwoPhaseFlowPipe1.re[7]
154/266 (1): dynamicTwoPhaseFlowPipe1.hb[8] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[8], dynamicTwoPhaseFlowPipe1.h[8], dynamicTwoPhaseFlowPipe1.h[9], 1.0)
155/267 (1): dynamicTwoPhaseFlowPipe1.gamma[8] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[8]
156/268 (1): dynamicTwoPhaseFlowPipe1.re[8] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[8]) ^ 2.0)
157/269 (1): dynamicTwoPhaseFlowPipe1.Je[8] = dynamicTwoPhaseFlowPipe1.re[8] * dynamicTwoPhaseFlowPipe1.gamma_e[8] * (dynamicTwoPhaseFlowPipe1.h[8] - dynamicTwoPhaseFlowPipe1.h[9])
158/270 (1): dynamicTwoPhaseFlowPipe1.J[8] = dynamicTwoPhaseFlowPipe1.Je[8] + dynamicTwoPhaseFlowPipe1.Js[8]
159/271 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[8] * sourceP1.Q0 + heatSource1.W0[8] + dynamicTwoPhaseFlowPipe1.J[8] - dynamicTwoPhaseFlowPipe1.hb[9] * sourceP1.Q0
160/272 (10): $cse65 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[8] + dynamicTwoPhaseFlowPipe1.P[9]), dynamicTwoPhaseFlowPipe1.hb[8], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
161/282 (1): dynamicTwoPhaseFlowPipe1.rhov2[8] = if noEvent(dynamicTwoPhaseFlowPipe1.P[9] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[8] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[8] else min(dynamicTwoPhaseFlowPipe1.rho2[8], dynamicTwoPhaseFlowPipe1.vsat2[8].rho)
162/283 (1): dynamicTwoPhaseFlowPipe1.muv2[8] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[8], dynamicTwoPhaseFlowPipe1.T2[8], dynamicTwoPhaseFlowPipe1.fluid)
163/284 (1): dynamicTwoPhaseFlowPipe1.Rev2[8] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[8]))
164/285 (1): dynamicTwoPhaseFlowPipe1.lambdav[8] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[8] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[8] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
165/286 (1): dynamicTwoPhaseFlowPipe1.filo[8] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[8] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[8] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[8] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[8] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[8]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[8]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[8] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[8] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[8]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[8])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[8] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[8] * dynamicTwoPhaseFlowPipe1.lambdav[8] / (dynamicTwoPhaseFlowPipe1.lambdal[8] * dynamicTwoPhaseFlowPipe1.rhov2[8])
166/287 (1): dynamicTwoPhaseFlowPipe1.khi[8] = dynamicTwoPhaseFlowPipe1.filo[8] * dynamicTwoPhaseFlowPipe1.lambdal[8] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
167/288 (1): dynamicTwoPhaseFlowPipe1.dpf[8] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[8] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[8])
168/289 (1): dynamicTwoPhaseFlowPipe1.P[8] + (-dynamicTwoPhaseFlowPipe1.dpg[8]) - dynamicTwoPhaseFlowPipe1.dpa[8] - dynamicTwoPhaseFlowPipe1.dpf[8] - dynamicTwoPhaseFlowPipe1.P[9] = 0.0
169/290 (1): dynamicTwoPhaseFlowPipe1.dpa[8] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[9] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[8]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
170/291 (10): $cse50 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[8], dynamicTwoPhaseFlowPipe1.h[8], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
171/301 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[7], dynamicTwoPhaseFlowPipe1.rhoc[8], dynamicTwoPhaseFlowPipe1.pro1[7].u, dynamicTwoPhaseFlowPipe1.pro1[7].s, dynamicTwoPhaseFlowPipe1.pro1[7].cp, dynamicTwoPhaseFlowPipe1.pro1[7].ddhp, dynamicTwoPhaseFlowPipe1.pro1[7].ddph, dynamicTwoPhaseFlowPipe1.pro1[7].duph, dynamicTwoPhaseFlowPipe1.pro1[7].duhp, dynamicTwoPhaseFlowPipe1.pro1[7].x) = $cse50
172/311 (1): dynamicTwoPhaseFlowPipe1.rhol2[8] = if noEvent(dynamicTwoPhaseFlowPipe1.P[9] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[8] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[8] else max(dynamicTwoPhaseFlowPipe1.rho2[8], dynamicTwoPhaseFlowPipe1.lsat2[8].rho)
173/312 (1): dynamicTwoPhaseFlowPipe1.mul2[8] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[8], dynamicTwoPhaseFlowPipe1.T2[8], dynamicTwoPhaseFlowPipe1.fluid)
174/313 (1): dynamicTwoPhaseFlowPipe1.Rel2[8] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[8]))
175/314 (1): dynamicTwoPhaseFlowPipe1.lambdal[8] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[8] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[8] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
176/315 (1): dynamicTwoPhaseFlowPipe1.kl2[8] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[8], dynamicTwoPhaseFlowPipe1.T2[8], 0.5 * (dynamicTwoPhaseFlowPipe1.P[8] + dynamicTwoPhaseFlowPipe1.P[9]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
177/316 (1): dynamicTwoPhaseFlowPipe1.hb[9] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[9], dynamicTwoPhaseFlowPipe1.h[9], dynamicTwoPhaseFlowPipe1.h[10], 1.0)
178/317 (10): $cse66 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[9] + dynamicTwoPhaseFlowPipe1.P[10]), dynamicTwoPhaseFlowPipe1.hb[9], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
179/327 (1): dynamicTwoPhaseFlowPipe1.cpl2[9] = if noEvent(dynamicTwoPhaseFlowPipe1.P[10] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[9] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[9].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[9] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[9].cp else dynamicTwoPhaseFlowPipe1.lsat2[9].cp
180/328 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[9] = dynamicTwoPhaseFlowPipe1.rho2[9] * dynamicTwoPhaseFlowPipe1.cpl2[9] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[9] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[9])
181/329 (1): dynamicTwoPhaseFlowPipe1.kl2[9] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[9], dynamicTwoPhaseFlowPipe1.T2[9], 0.5 * (dynamicTwoPhaseFlowPipe1.P[9] + dynamicTwoPhaseFlowPipe1.P[10]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
182/330 (1): dynamicTwoPhaseFlowPipe1.mul2[9] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[9], dynamicTwoPhaseFlowPipe1.T2[9], dynamicTwoPhaseFlowPipe1.fluid)
183/331 (1): dynamicTwoPhaseFlowPipe1.Rel2[9] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[9]))
184/332 (1): dynamicTwoPhaseFlowPipe1.lambdal[9] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[9] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[9] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
185/333 (1): dynamicTwoPhaseFlowPipe1.filo[9] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[9] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[9] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[9] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[9] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[9]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[9]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[9] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[9] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[9]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[9])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[9] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[9] * dynamicTwoPhaseFlowPipe1.lambdav[9] / (dynamicTwoPhaseFlowPipe1.lambdal[9] * dynamicTwoPhaseFlowPipe1.rhov2[9])
186/334 (1): dynamicTwoPhaseFlowPipe1.khi[9] = dynamicTwoPhaseFlowPipe1.filo[9] * dynamicTwoPhaseFlowPipe1.lambdal[9] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
187/335 (1): dynamicTwoPhaseFlowPipe1.dpf[9] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[9] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[9])
188/336 (1): dynamicTwoPhaseFlowPipe1.P[9] + (-dynamicTwoPhaseFlowPipe1.dpg[9]) - dynamicTwoPhaseFlowPipe1.dpa[9] - dynamicTwoPhaseFlowPipe1.dpf[9] - dynamicTwoPhaseFlowPipe1.P[10] = 0.0
189/337 (1): dynamicTwoPhaseFlowPipe1.dpa[9] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[10] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[9]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
190/338 (10): $cse52 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[9], dynamicTwoPhaseFlowPipe1.h[9], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
191/348 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[8], dynamicTwoPhaseFlowPipe1.rhoc[9], dynamicTwoPhaseFlowPipe1.pro1[8].u, dynamicTwoPhaseFlowPipe1.pro1[8].s, dynamicTwoPhaseFlowPipe1.pro1[8].cp, dynamicTwoPhaseFlowPipe1.pro1[8].ddhp, dynamicTwoPhaseFlowPipe1.pro1[8].ddph, dynamicTwoPhaseFlowPipe1.pro1[8].duph, dynamicTwoPhaseFlowPipe1.pro1[8].duhp, dynamicTwoPhaseFlowPipe1.pro1[8].x) = $cse52
192/358 (1): dynamicTwoPhaseFlowPipe1.rhol2[9] = if noEvent(dynamicTwoPhaseFlowPipe1.P[10] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[9] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[9] else max(dynamicTwoPhaseFlowPipe1.rho2[9], dynamicTwoPhaseFlowPipe1.lsat2[9].rho)
193/359 (10): $cse54 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[10], dynamicTwoPhaseFlowPipe1.h[10], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
194/369 (1): dynamicTwoPhaseFlowPipe1.dpa[10] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[11] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[10]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
195/370 (1): dynamicTwoPhaseFlowPipe1.P[10] + (-dynamicTwoPhaseFlowPipe1.dpg[10]) - dynamicTwoPhaseFlowPipe1.dpa[10] - dynamicTwoPhaseFlowPipe1.dpf[10] - dynamicTwoPhaseFlowPipe1.P[11] = 0.0
196/371 (1): dynamicTwoPhaseFlowPipe1.dpf[10] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[10] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[10])
197/372 (1): dynamicTwoPhaseFlowPipe1.khi[10] = dynamicTwoPhaseFlowPipe1.filo[10] * dynamicTwoPhaseFlowPipe1.lambdal[10] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
198/373 (1): dynamicTwoPhaseFlowPipe1.filo[10] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[10] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[10] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[10] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[10] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[10]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[10]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[10] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[10] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[10]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[10])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[10] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[10] * dynamicTwoPhaseFlowPipe1.lambdav[10] / (dynamicTwoPhaseFlowPipe1.lambdal[10] * dynamicTwoPhaseFlowPipe1.rhov2[10])
199/374 (1): dynamicTwoPhaseFlowPipe1.lambdav[10] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[10] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[10] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
200/375 (1): dynamicTwoPhaseFlowPipe1.Rev2[10] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[10]))
201/376 (1): dynamicTwoPhaseFlowPipe1.muv2[10] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[10], dynamicTwoPhaseFlowPipe1.T2[10], dynamicTwoPhaseFlowPipe1.fluid)
202/377 (1): dynamicTwoPhaseFlowPipe1.mul2[10] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[10], dynamicTwoPhaseFlowPipe1.T2[10], dynamicTwoPhaseFlowPipe1.fluid)
203/378 (1): dynamicTwoPhaseFlowPipe1.Rel2[10] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[10]))
204/379 (1): dynamicTwoPhaseFlowPipe1.lambdal[10] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[10] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[10] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
205/380 (1): dynamicTwoPhaseFlowPipe1.kl2[10] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[10], dynamicTwoPhaseFlowPipe1.T2[10], 0.5 * (dynamicTwoPhaseFlowPipe1.P[10] + dynamicTwoPhaseFlowPipe1.P[11]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
206/381 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[10] = dynamicTwoPhaseFlowPipe1.rho2[10] * dynamicTwoPhaseFlowPipe1.cpl2[10] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[10] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[10])
207/382 (1): dynamicTwoPhaseFlowPipe1.cpl2[10] = if noEvent(dynamicTwoPhaseFlowPipe1.P[11] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[10] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[10].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[10] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[10].cp else dynamicTwoPhaseFlowPipe1.lsat2[10].cp
208/383 (1): dynamicTwoPhaseFlowPipe1.hb[10] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[10], dynamicTwoPhaseFlowPipe1.h[10], dynamicTwoPhaseFlowPipe1.h[11], 1.0)
209/384 (1): dynamicTwoPhaseFlowPipe1.gamma[10] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[10]
210/385 (1): dynamicTwoPhaseFlowPipe1.re[10] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[10]) ^ 2.0)
211/386 (1): dynamicTwoPhaseFlowPipe1.Je[10] = dynamicTwoPhaseFlowPipe1.re[10] * dynamicTwoPhaseFlowPipe1.gamma_e[10] * (dynamicTwoPhaseFlowPipe1.h[10] - dynamicTwoPhaseFlowPipe1.h[11])
212/387 (1): dynamicTwoPhaseFlowPipe1.Js[9] = dynamicTwoPhaseFlowPipe1.rs[9] * dynamicTwoPhaseFlowPipe1.gamma_s[9] * (dynamicTwoPhaseFlowPipe1.h[11] - dynamicTwoPhaseFlowPipe1.h[10])
213/388 (1): dynamicTwoPhaseFlowPipe1.J[9] = dynamicTwoPhaseFlowPipe1.Je[9] + dynamicTwoPhaseFlowPipe1.Js[9]
214/389 (1): dynamicTwoPhaseFlowPipe1.Je[9] = dynamicTwoPhaseFlowPipe1.re[9] * dynamicTwoPhaseFlowPipe1.gamma_e[9] * (dynamicTwoPhaseFlowPipe1.h[9] - dynamicTwoPhaseFlowPipe1.h[10])
215/390 (1): dynamicTwoPhaseFlowPipe1.re[9] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[9]) ^ 2.0)
216/391 (1): dynamicTwoPhaseFlowPipe1.gamma[9] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[9]
217/392 (1): dynamicTwoPhaseFlowPipe1.gamma_e[9] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[9]
218/393 (1): dynamicTwoPhaseFlowPipe1.gamma_s[8] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[9]
219/394 (1): dynamicTwoPhaseFlowPipe1.Js[8] = dynamicTwoPhaseFlowPipe1.rs[8] * dynamicTwoPhaseFlowPipe1.gamma_s[8] * (dynamicTwoPhaseFlowPipe1.h[10] - dynamicTwoPhaseFlowPipe1.h[9])
220/395 (1): dynamicTwoPhaseFlowPipe1.rs[8] = dynamicTwoPhaseFlowPipe1.re[9]
221/396 (1): dynamicTwoPhaseFlowPipe1.rs[9] = dynamicTwoPhaseFlowPipe1.re[10]
222/397 (1): dynamicTwoPhaseFlowPipe1.gamma_e[10] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[10]
223/398 (1): dynamicTwoPhaseFlowPipe1.gamma_s[9] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[10]
224/399 (1): dynamicTwoPhaseFlowPipe1.hb[11] = ThermoSysPro.Functions.SmoothCond(sourceP1.Q0 / dynamicTwoPhaseFlowPipe1.gamma[11], dynamicTwoPhaseFlowPipe1.h[11], dynamicTwoPhaseFlowPipe1.h[12], 1.0)
225/400 (1): dynamicTwoPhaseFlowPipe1.gamma[11] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_s[10]
226/401 (1): dynamicTwoPhaseFlowPipe1.rs[10] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_s[10]) ^ 2.0)
227/402 (1): dynamicTwoPhaseFlowPipe1.Js[10] = if sinkP1.diffusion then dynamicTwoPhaseFlowPipe1.rs[10] * dynamicTwoPhaseFlowPipe1.gamma_s[10] * (dynamicTwoPhaseFlowPipe1.h[12] - dynamicTwoPhaseFlowPipe1.h[11]) else 0.0
228/403 (1): dynamicTwoPhaseFlowPipe1.J[10] = dynamicTwoPhaseFlowPipe1.Je[10] + dynamicTwoPhaseFlowPipe1.Js[10]
229/404 (1): dynamicTwoPhaseFlowPipe1.diff_res_s[10] = dynamicTwoPhaseFlowPipe1.rho2[11] * dynamicTwoPhaseFlowPipe1.cpl2[11] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[11] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[11])
230/405 (1): dynamicTwoPhaseFlowPipe1.mul2[11] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[11], dynamicTwoPhaseFlowPipe1.T2[11], dynamicTwoPhaseFlowPipe1.fluid)
231/406 (1): dynamicTwoPhaseFlowPipe1.Rel2[11] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[11]))
232/407 (1): dynamicTwoPhaseFlowPipe1.lambdal[11] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[11] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[11] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
233/408 (1): dynamicTwoPhaseFlowPipe1.filo[11] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[11] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[11] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[11] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[11] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[11]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[11]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[11] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[11] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[11]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[11])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[11] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[11] * dynamicTwoPhaseFlowPipe1.lambdav[11] / (dynamicTwoPhaseFlowPipe1.lambdal[11] * dynamicTwoPhaseFlowPipe1.rhov2[11])
234/409 (1): dynamicTwoPhaseFlowPipe1.khi[11] = dynamicTwoPhaseFlowPipe1.filo[11] * dynamicTwoPhaseFlowPipe1.lambdal[11] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
235/410 (1): dynamicTwoPhaseFlowPipe1.dpf[11] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[11] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[11])
236/411 (1): dynamicTwoPhaseFlowPipe1.P[11] + (-dynamicTwoPhaseFlowPipe1.dpf[11]) - sinkP1.P0 - dynamicTwoPhaseFlowPipe1.dpa[11] - dynamicTwoPhaseFlowPipe1.dpg[11] = 0.0
237/412 (1): dynamicTwoPhaseFlowPipe1.dpa[11] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[12] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[11]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
238/413 (10): $cse56 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[11], dynamicTwoPhaseFlowPipe1.h[11], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
239/423 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[10], dynamicTwoPhaseFlowPipe1.rhoc[11], dynamicTwoPhaseFlowPipe1.pro1[10].u, dynamicTwoPhaseFlowPipe1.pro1[10].s, dynamicTwoPhaseFlowPipe1.pro1[10].cp, dynamicTwoPhaseFlowPipe1.pro1[10].ddhp, dynamicTwoPhaseFlowPipe1.pro1[10].ddph, dynamicTwoPhaseFlowPipe1.pro1[10].duph, dynamicTwoPhaseFlowPipe1.pro1[10].duhp, dynamicTwoPhaseFlowPipe1.pro1[10].x) = $cse56
240/433 (1): dynamicTwoPhaseFlowPipe1.kl2[11] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[11], dynamicTwoPhaseFlowPipe1.T2[11], 0.5 * (dynamicTwoPhaseFlowPipe1.P[11] + sinkP1.P0), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
241/434 (1): dynamicTwoPhaseFlowPipe1.rhol2[11] = if noEvent(sinkP1.P0 > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[11] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[11] else max(dynamicTwoPhaseFlowPipe1.rho2[11], dynamicTwoPhaseFlowPipe1.lsat2[11].rho)
242/435 (1): dynamicTwoPhaseFlowPipe1.rhov2[11] = if noEvent(sinkP1.P0 > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[11] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[11] else min(dynamicTwoPhaseFlowPipe1.rho2[11], dynamicTwoPhaseFlowPipe1.vsat2[11].rho)
243/436 (1): dynamicTwoPhaseFlowPipe1.muv2[11] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[11], dynamicTwoPhaseFlowPipe1.T2[11], dynamicTwoPhaseFlowPipe1.fluid)
244/437 (1): dynamicTwoPhaseFlowPipe1.Rev2[11] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[11]))
245/438 (1): dynamicTwoPhaseFlowPipe1.lambdav[11] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[11] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[11] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
246/439 (10): $cse68 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[11] + sinkP1.P0), dynamicTwoPhaseFlowPipe1.hb[11], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
247/449 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[10] * sourceP1.Q0 + heatSource1.W0[10] + dynamicTwoPhaseFlowPipe1.J[10] - dynamicTwoPhaseFlowPipe1.hb[11] * sourceP1.Q0
248/450 (1): dynamicTwoPhaseFlowPipe1.cpl2[11] = if noEvent(sinkP1.P0 > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[11] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[11].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[11] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[11].cp else dynamicTwoPhaseFlowPipe1.lsat2[11].cp
249/451 (1): dynamicTwoPhaseFlowPipe1.xv2[11] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[11] + sinkP1.P0) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[11] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[11].x
250/452 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[11], dynamicTwoPhaseFlowPipe1.rho2[11], dynamicTwoPhaseFlowPipe1.pro2[11].u, dynamicTwoPhaseFlowPipe1.pro2[11].s, dynamicTwoPhaseFlowPipe1.pro2[11].cp, dynamicTwoPhaseFlowPipe1.pro2[11].ddhp, dynamicTwoPhaseFlowPipe1.pro2[11].ddph, dynamicTwoPhaseFlowPipe1.pro2[11].duph, dynamicTwoPhaseFlowPipe1.pro2[11].duhp, dynamicTwoPhaseFlowPipe1.pro2[11].x) = $cse68
251/462 (1): dynamicTwoPhaseFlowPipe1.dpg[11] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[11] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
252/463 (1): dynamicTwoPhaseFlowPipe1.gamma_s[10] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_s[10]
253/464 (1): $cse57 = min(dynamicTwoPhaseFlowPipe1.P[11], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
254/465 (1): dynamicTwoPhaseFlowPipe1.Pb[11] = max($cse57, dynamicTwoPhaseFlowPipe1.ptriple)
255/466 (10): $cse67 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[10] + dynamicTwoPhaseFlowPipe1.P[11]), dynamicTwoPhaseFlowPipe1.hb[10], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
256/476 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[9] * sourceP1.Q0 + heatSource1.W0[9] + dynamicTwoPhaseFlowPipe1.J[9] - dynamicTwoPhaseFlowPipe1.hb[10] * sourceP1.Q0
257/477 (1): dynamicTwoPhaseFlowPipe1.xv2[10] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[10] + dynamicTwoPhaseFlowPipe1.P[11]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[10] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[10].x
258/478 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[10], dynamicTwoPhaseFlowPipe1.rho2[10], dynamicTwoPhaseFlowPipe1.pro2[10].u, dynamicTwoPhaseFlowPipe1.pro2[10].s, dynamicTwoPhaseFlowPipe1.pro2[10].cp, dynamicTwoPhaseFlowPipe1.pro2[10].ddhp, dynamicTwoPhaseFlowPipe1.pro2[10].ddph, dynamicTwoPhaseFlowPipe1.pro2[10].duph, dynamicTwoPhaseFlowPipe1.pro2[10].duhp, dynamicTwoPhaseFlowPipe1.pro2[10].x) = $cse67
259/488 (1): dynamicTwoPhaseFlowPipe1.rhov2[10] = if noEvent(dynamicTwoPhaseFlowPipe1.P[11] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[10] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[10] else min(dynamicTwoPhaseFlowPipe1.rho2[10], dynamicTwoPhaseFlowPipe1.vsat2[10].rho)
260/489 (1): dynamicTwoPhaseFlowPipe1.rhol2[10] = if noEvent(dynamicTwoPhaseFlowPipe1.P[11] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[10] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[10] else max(dynamicTwoPhaseFlowPipe1.rho2[10], dynamicTwoPhaseFlowPipe1.lsat2[10].rho)
261/490 (1): dynamicTwoPhaseFlowPipe1.dpg[10] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[10] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
262/491 (14): (dynamicTwoPhaseFlowPipe1.lsat2[10], dynamicTwoPhaseFlowPipe1.vsat2[10]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[10] + dynamicTwoPhaseFlowPipe1.P[11]), dynamicTwoPhaseFlowPipe1.fluid)
263/505 (14): (dynamicTwoPhaseFlowPipe1.lsat2[11], dynamicTwoPhaseFlowPipe1.vsat2[11]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[11] + sinkP1.P0), dynamicTwoPhaseFlowPipe1.fluid)
264/519 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[9], dynamicTwoPhaseFlowPipe1.rhoc[10], dynamicTwoPhaseFlowPipe1.pro1[9].u, dynamicTwoPhaseFlowPipe1.pro1[9].s, dynamicTwoPhaseFlowPipe1.pro1[9].cp, dynamicTwoPhaseFlowPipe1.pro1[9].ddhp, dynamicTwoPhaseFlowPipe1.pro1[9].ddph, dynamicTwoPhaseFlowPipe1.pro1[9].duph, dynamicTwoPhaseFlowPipe1.pro1[9].duhp, dynamicTwoPhaseFlowPipe1.pro1[9].x) = $cse54
265/529 (1): $cse55 = min(dynamicTwoPhaseFlowPipe1.P[10], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
266/530 (1): dynamicTwoPhaseFlowPipe1.Pb[10] = max($cse55, dynamicTwoPhaseFlowPipe1.ptriple)
267/531 (14): (dynamicTwoPhaseFlowPipe1.lsat2[9], dynamicTwoPhaseFlowPipe1.vsat2[9]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[9] + dynamicTwoPhaseFlowPipe1.P[10]), dynamicTwoPhaseFlowPipe1.fluid)
268/545 (1): dynamicTwoPhaseFlowPipe1.rhov2[9] = if noEvent(dynamicTwoPhaseFlowPipe1.P[10] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[9] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[9] else min(dynamicTwoPhaseFlowPipe1.rho2[9], dynamicTwoPhaseFlowPipe1.vsat2[9].rho)
269/546 (1): dynamicTwoPhaseFlowPipe1.muv2[9] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[9], dynamicTwoPhaseFlowPipe1.T2[9], dynamicTwoPhaseFlowPipe1.fluid)
270/547 (1): dynamicTwoPhaseFlowPipe1.Rev2[9] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[9]))
271/548 (1): dynamicTwoPhaseFlowPipe1.lambdav[9] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[9] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[9] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
272/549 (1): dynamicTwoPhaseFlowPipe1.xv2[9] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[9] + dynamicTwoPhaseFlowPipe1.P[10]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[9] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[9].x
273/550 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[9], dynamicTwoPhaseFlowPipe1.rho2[9], dynamicTwoPhaseFlowPipe1.pro2[9].u, dynamicTwoPhaseFlowPipe1.pro2[9].s, dynamicTwoPhaseFlowPipe1.pro2[9].cp, dynamicTwoPhaseFlowPipe1.pro2[9].ddhp, dynamicTwoPhaseFlowPipe1.pro2[9].ddph, dynamicTwoPhaseFlowPipe1.pro2[9].duph, dynamicTwoPhaseFlowPipe1.pro2[9].duhp, dynamicTwoPhaseFlowPipe1.pro2[9].x) = $cse66
274/560 (1): dynamicTwoPhaseFlowPipe1.dpg[9] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[9] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
275/561 (1): dynamicTwoPhaseFlowPipe1.Js[7] = dynamicTwoPhaseFlowPipe1.rs[7] * dynamicTwoPhaseFlowPipe1.gamma_s[7] * (dynamicTwoPhaseFlowPipe1.h[9] - dynamicTwoPhaseFlowPipe1.h[8])
276/562 (1): dynamicTwoPhaseFlowPipe1.J[7] = dynamicTwoPhaseFlowPipe1.Je[7] + dynamicTwoPhaseFlowPipe1.Js[7]
277/563 (1): $cse53 = min(dynamicTwoPhaseFlowPipe1.P[9], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
278/564 (1): dynamicTwoPhaseFlowPipe1.Pb[9] = max($cse53, dynamicTwoPhaseFlowPipe1.ptriple)
279/565 (14): (dynamicTwoPhaseFlowPipe1.lsat2[8], dynamicTwoPhaseFlowPipe1.vsat2[8]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[8] + dynamicTwoPhaseFlowPipe1.P[9]), dynamicTwoPhaseFlowPipe1.fluid)
280/579 (1): dynamicTwoPhaseFlowPipe1.cpl2[8] = if noEvent(dynamicTwoPhaseFlowPipe1.P[9] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[8] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[8].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[8] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[8].cp else dynamicTwoPhaseFlowPipe1.lsat2[8].cp
281/580 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[8] = dynamicTwoPhaseFlowPipe1.rho2[8] * dynamicTwoPhaseFlowPipe1.cpl2[8] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[8] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[8])
282/581 (1): dynamicTwoPhaseFlowPipe1.xv2[8] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[8] + dynamicTwoPhaseFlowPipe1.P[9]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[8] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[8].x
283/582 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[8], dynamicTwoPhaseFlowPipe1.rho2[8], dynamicTwoPhaseFlowPipe1.pro2[8].u, dynamicTwoPhaseFlowPipe1.pro2[8].s, dynamicTwoPhaseFlowPipe1.pro2[8].cp, dynamicTwoPhaseFlowPipe1.pro2[8].ddhp, dynamicTwoPhaseFlowPipe1.pro2[8].ddph, dynamicTwoPhaseFlowPipe1.pro2[8].duph, dynamicTwoPhaseFlowPipe1.pro2[8].duhp, dynamicTwoPhaseFlowPipe1.pro2[8].x) = $cse65
284/592 (1): dynamicTwoPhaseFlowPipe1.dpg[8] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[8] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
285/593 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[7] * sourceP1.Q0 + heatSource1.W0[7] + dynamicTwoPhaseFlowPipe1.J[7] - dynamicTwoPhaseFlowPipe1.hb[8] * sourceP1.Q0
286/594 (1): dynamicTwoPhaseFlowPipe1.rs[7] = dynamicTwoPhaseFlowPipe1.re[8]
287/595 (1): dynamicTwoPhaseFlowPipe1.gamma_e[8] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[8]
288/596 (1): dynamicTwoPhaseFlowPipe1.gamma_s[7] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[8]
289/597 (1): $cse51 = min(dynamicTwoPhaseFlowPipe1.P[8], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
290/598 (1): dynamicTwoPhaseFlowPipe1.Pb[8] = max($cse51, dynamicTwoPhaseFlowPipe1.ptriple)
291/599 (10): $cse64 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[7] + dynamicTwoPhaseFlowPipe1.P[8]), dynamicTwoPhaseFlowPipe1.hb[7], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
292/609 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[6] * sourceP1.Q0 + heatSource1.W0[6] + dynamicTwoPhaseFlowPipe1.J[6] - dynamicTwoPhaseFlowPipe1.hb[7] * sourceP1.Q0
293/610 (1): dynamicTwoPhaseFlowPipe1.rhov2[7] = if noEvent(dynamicTwoPhaseFlowPipe1.P[8] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[7] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[7] else min(dynamicTwoPhaseFlowPipe1.rho2[7], dynamicTwoPhaseFlowPipe1.vsat2[7].rho)
294/611 (1): dynamicTwoPhaseFlowPipe1.xv2[7] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[7] + dynamicTwoPhaseFlowPipe1.P[8]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[7] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[7].x
295/612 (1): dynamicTwoPhaseFlowPipe1.cpl2[7] = if noEvent(dynamicTwoPhaseFlowPipe1.P[8] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[7] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[7].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[7] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[7].cp else dynamicTwoPhaseFlowPipe1.lsat2[7].cp
296/613 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[7], dynamicTwoPhaseFlowPipe1.rho2[7], dynamicTwoPhaseFlowPipe1.pro2[7].u, dynamicTwoPhaseFlowPipe1.pro2[7].s, dynamicTwoPhaseFlowPipe1.pro2[7].cp, dynamicTwoPhaseFlowPipe1.pro2[7].ddhp, dynamicTwoPhaseFlowPipe1.pro2[7].ddph, dynamicTwoPhaseFlowPipe1.pro2[7].duph, dynamicTwoPhaseFlowPipe1.pro2[7].duhp, dynamicTwoPhaseFlowPipe1.pro2[7].x) = $cse64
297/623 (1): dynamicTwoPhaseFlowPipe1.dpg[7] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[7] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
298/624 (14): (dynamicTwoPhaseFlowPipe1.lsat2[7], dynamicTwoPhaseFlowPipe1.vsat2[7]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[7] + dynamicTwoPhaseFlowPipe1.P[8]), dynamicTwoPhaseFlowPipe1.fluid)
299/638 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[6], dynamicTwoPhaseFlowPipe1.rhoc[7], dynamicTwoPhaseFlowPipe1.pro1[6].u, dynamicTwoPhaseFlowPipe1.pro1[6].s, dynamicTwoPhaseFlowPipe1.pro1[6].cp, dynamicTwoPhaseFlowPipe1.pro1[6].ddhp, dynamicTwoPhaseFlowPipe1.pro1[6].ddph, dynamicTwoPhaseFlowPipe1.pro1[6].duph, dynamicTwoPhaseFlowPipe1.pro1[6].duhp, dynamicTwoPhaseFlowPipe1.pro1[6].x) = $cse48
300/648 (1): $cse49 = min(dynamicTwoPhaseFlowPipe1.P[7], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
301/649 (1): dynamicTwoPhaseFlowPipe1.Pb[7] = max($cse49, dynamicTwoPhaseFlowPipe1.ptriple)
302/650 (10): $cse63 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[6] + dynamicTwoPhaseFlowPipe1.P[7]), dynamicTwoPhaseFlowPipe1.hb[6], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
303/660 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[5] * sourceP1.Q0 + heatSource1.W0[5] + dynamicTwoPhaseFlowPipe1.J[5] - dynamicTwoPhaseFlowPipe1.hb[6] * sourceP1.Q0
304/661 (1): dynamicTwoPhaseFlowPipe1.xv2[6] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[6] + dynamicTwoPhaseFlowPipe1.P[7]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[6] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[6].x
305/662 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[6], dynamicTwoPhaseFlowPipe1.rho2[6], dynamicTwoPhaseFlowPipe1.pro2[6].u, dynamicTwoPhaseFlowPipe1.pro2[6].s, dynamicTwoPhaseFlowPipe1.pro2[6].cp, dynamicTwoPhaseFlowPipe1.pro2[6].ddhp, dynamicTwoPhaseFlowPipe1.pro2[6].ddph, dynamicTwoPhaseFlowPipe1.pro2[6].duph, dynamicTwoPhaseFlowPipe1.pro2[6].duhp, dynamicTwoPhaseFlowPipe1.pro2[6].x) = $cse63
306/672 (14): (dynamicTwoPhaseFlowPipe1.lsat2[6], dynamicTwoPhaseFlowPipe1.vsat2[6]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[6] + dynamicTwoPhaseFlowPipe1.P[7]), dynamicTwoPhaseFlowPipe1.fluid)
307/686 (1): dynamicTwoPhaseFlowPipe1.dpg[6] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[6] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
308/687 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[5], dynamicTwoPhaseFlowPipe1.rhoc[6], dynamicTwoPhaseFlowPipe1.pro1[5].u, dynamicTwoPhaseFlowPipe1.pro1[5].s, dynamicTwoPhaseFlowPipe1.pro1[5].cp, dynamicTwoPhaseFlowPipe1.pro1[5].ddhp, dynamicTwoPhaseFlowPipe1.pro1[5].ddph, dynamicTwoPhaseFlowPipe1.pro1[5].duph, dynamicTwoPhaseFlowPipe1.pro1[5].duhp, dynamicTwoPhaseFlowPipe1.pro1[5].x) = $cse46
309/697 (1): $cse47 = min(dynamicTwoPhaseFlowPipe1.P[6], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
310/698 (1): dynamicTwoPhaseFlowPipe1.Pb[6] = max($cse47, dynamicTwoPhaseFlowPipe1.ptriple)
311/699 (10): $cse62 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[5] + dynamicTwoPhaseFlowPipe1.P[6]), dynamicTwoPhaseFlowPipe1.hb[5], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
312/709 (1): dynamicTwoPhaseFlowPipe1.xv2[5] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[5] + dynamicTwoPhaseFlowPipe1.P[6]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[5] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[5].x
313/710 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[5], dynamicTwoPhaseFlowPipe1.rho2[5], dynamicTwoPhaseFlowPipe1.pro2[5].u, dynamicTwoPhaseFlowPipe1.pro2[5].s, dynamicTwoPhaseFlowPipe1.pro2[5].cp, dynamicTwoPhaseFlowPipe1.pro2[5].ddhp, dynamicTwoPhaseFlowPipe1.pro2[5].ddph, dynamicTwoPhaseFlowPipe1.pro2[5].duph, dynamicTwoPhaseFlowPipe1.pro2[5].duhp, dynamicTwoPhaseFlowPipe1.pro2[5].x) = $cse62
314/720 (1): dynamicTwoPhaseFlowPipe1.dpg[5] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[5] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
315/721 (14): (dynamicTwoPhaseFlowPipe1.lsat2[5], dynamicTwoPhaseFlowPipe1.vsat2[5]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[5] + dynamicTwoPhaseFlowPipe1.P[6]), dynamicTwoPhaseFlowPipe1.fluid)
316/735 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[4], dynamicTwoPhaseFlowPipe1.rhoc[5], dynamicTwoPhaseFlowPipe1.pro1[4].u, dynamicTwoPhaseFlowPipe1.pro1[4].s, dynamicTwoPhaseFlowPipe1.pro1[4].cp, dynamicTwoPhaseFlowPipe1.pro1[4].ddhp, dynamicTwoPhaseFlowPipe1.pro1[4].ddph, dynamicTwoPhaseFlowPipe1.pro1[4].duph, dynamicTwoPhaseFlowPipe1.pro1[4].duhp, dynamicTwoPhaseFlowPipe1.pro1[4].x) = $cse44
317/745 (1): $cse45 = min(dynamicTwoPhaseFlowPipe1.P[5], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
318/746 (1): dynamicTwoPhaseFlowPipe1.Pb[5] = max($cse45, dynamicTwoPhaseFlowPipe1.ptriple)
319/747 (14): (dynamicTwoPhaseFlowPipe1.lsat2[4], dynamicTwoPhaseFlowPipe1.vsat2[4]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[4] + dynamicTwoPhaseFlowPipe1.P[5]), dynamicTwoPhaseFlowPipe1.fluid)
320/761 (1): dynamicTwoPhaseFlowPipe1.rhol2[4] = if noEvent(dynamicTwoPhaseFlowPipe1.P[5] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[4] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[4] else max(dynamicTwoPhaseFlowPipe1.rho2[4], dynamicTwoPhaseFlowPipe1.lsat2[4].rho)
321/762 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[4] = dynamicTwoPhaseFlowPipe1.rho2[4] * dynamicTwoPhaseFlowPipe1.cpl2[4] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[4] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[4])
322/763 (1): dynamicTwoPhaseFlowPipe1.rhov2[4] = if noEvent(dynamicTwoPhaseFlowPipe1.P[5] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[4] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[4] else min(dynamicTwoPhaseFlowPipe1.rho2[4], dynamicTwoPhaseFlowPipe1.vsat2[4].rho)
323/764 (1): dynamicTwoPhaseFlowPipe1.cpl2[4] = if noEvent(dynamicTwoPhaseFlowPipe1.P[5] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[4] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[4].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[4] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[4].cp else dynamicTwoPhaseFlowPipe1.lsat2[4].cp
324/765 (1): dynamicTwoPhaseFlowPipe1.xv2[4] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[4] + dynamicTwoPhaseFlowPipe1.P[5]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[4] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[4].x
325/766 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[4], dynamicTwoPhaseFlowPipe1.rho2[4], dynamicTwoPhaseFlowPipe1.pro2[4].u, dynamicTwoPhaseFlowPipe1.pro2[4].s, dynamicTwoPhaseFlowPipe1.pro2[4].cp, dynamicTwoPhaseFlowPipe1.pro2[4].ddhp, dynamicTwoPhaseFlowPipe1.pro2[4].ddph, dynamicTwoPhaseFlowPipe1.pro2[4].duph, dynamicTwoPhaseFlowPipe1.pro2[4].duhp, dynamicTwoPhaseFlowPipe1.pro2[4].x) = $cse61
326/776 (1): dynamicTwoPhaseFlowPipe1.dpg[4] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[4] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
327/777 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[3] * sourceP1.Q0 + heatSource1.W0[3] + dynamicTwoPhaseFlowPipe1.J[3] - dynamicTwoPhaseFlowPipe1.hb[4] * sourceP1.Q0
328/778 (1): dynamicTwoPhaseFlowPipe1.rs[3] = dynamicTwoPhaseFlowPipe1.re[4]
329/779 (1): dynamicTwoPhaseFlowPipe1.gamma_e[4] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[4]
330/780 (1): dynamicTwoPhaseFlowPipe1.gamma_s[3] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[4]
331/781 (1): dynamicTwoPhaseFlowPipe1.Js[2] = dynamicTwoPhaseFlowPipe1.rs[2] * dynamicTwoPhaseFlowPipe1.gamma_s[2] * (dynamicTwoPhaseFlowPipe1.h[4] - dynamicTwoPhaseFlowPipe1.h[3])
332/782 (1): dynamicTwoPhaseFlowPipe1.J[2] = dynamicTwoPhaseFlowPipe1.Je[2] + dynamicTwoPhaseFlowPipe1.Js[2]
333/783 (1): dynamicTwoPhaseFlowPipe1.Je[2] = dynamicTwoPhaseFlowPipe1.re[2] * dynamicTwoPhaseFlowPipe1.gamma_e[2] * (dynamicTwoPhaseFlowPipe1.h[2] - dynamicTwoPhaseFlowPipe1.h[3])
334/784 (1): dynamicTwoPhaseFlowPipe1.gamma_e[2] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[2]
335/785 (1): dynamicTwoPhaseFlowPipe1.re[2] = exp((-0.033) * (sourceP1.Q0 * dynamicTwoPhaseFlowPipe1.diff_res_e[2]) ^ 2.0)
336/786 (1): dynamicTwoPhaseFlowPipe1.rs[1] = dynamicTwoPhaseFlowPipe1.re[2]
337/787 (1): dynamicTwoPhaseFlowPipe1.Js[1] = dynamicTwoPhaseFlowPipe1.rs[1] * dynamicTwoPhaseFlowPipe1.gamma_s[1] * (dynamicTwoPhaseFlowPipe1.h[3] - dynamicTwoPhaseFlowPipe1.h[2])
338/788 (1): dynamicTwoPhaseFlowPipe1.gamma[2] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[2]
339/789 (1): dynamicTwoPhaseFlowPipe1.gamma_s[1] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[2]
340/790 (1): $cse43 = min(dynamicTwoPhaseFlowPipe1.P[4], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
341/791 (1): dynamicTwoPhaseFlowPipe1.Pb[4] = max($cse43, dynamicTwoPhaseFlowPipe1.ptriple)
342/792 (10): $cse60 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[3] + dynamicTwoPhaseFlowPipe1.P[4]), dynamicTwoPhaseFlowPipe1.hb[3], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
343/802 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[3], dynamicTwoPhaseFlowPipe1.rho2[3], dynamicTwoPhaseFlowPipe1.pro2[3].u, dynamicTwoPhaseFlowPipe1.pro2[3].s, dynamicTwoPhaseFlowPipe1.pro2[3].cp, dynamicTwoPhaseFlowPipe1.pro2[3].ddhp, dynamicTwoPhaseFlowPipe1.pro2[3].ddph, dynamicTwoPhaseFlowPipe1.pro2[3].duph, dynamicTwoPhaseFlowPipe1.pro2[3].duhp, dynamicTwoPhaseFlowPipe1.pro2[3].x) = $cse60
344/812 (14): (dynamicTwoPhaseFlowPipe1.lsat2[3], dynamicTwoPhaseFlowPipe1.vsat2[3]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[3] + dynamicTwoPhaseFlowPipe1.P[4]), dynamicTwoPhaseFlowPipe1.fluid)
345/826 (1): dynamicTwoPhaseFlowPipe1.rs[2] = dynamicTwoPhaseFlowPipe1.re[3]
346/827 (1): dynamicTwoPhaseFlowPipe1.gamma_e[3] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[3]
347/828 (1): dynamicTwoPhaseFlowPipe1.gamma_s[2] = 1.0 / dynamicTwoPhaseFlowPipe1.diff_res_e[3]
348/829 (1): 0.0 = dynamicTwoPhaseFlowPipe1.hb[2] * sourceP1.Q0 + heatSource1.W0[2] + dynamicTwoPhaseFlowPipe1.J[2] - dynamicTwoPhaseFlowPipe1.hb[3] * sourceP1.Q0
349/830 (1): dynamicTwoPhaseFlowPipe1.dpg[3] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[3] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
350/831 (1): dynamicTwoPhaseFlowPipe1.dpa[1] = sourceP1.Q0 ^ 2.0 * (1.0 / dynamicTwoPhaseFlowPipe1.rhoc[2] + (-1.0) / dynamicTwoPhaseFlowPipe1.rhoc[1]) / dynamicTwoPhaseFlowPipe1.A ^ 2.0
351/832 (1): dynamicTwoPhaseFlowPipe1.P[1] + (-dynamicTwoPhaseFlowPipe1.dpg[1]) - dynamicTwoPhaseFlowPipe1.dpa[1] - dynamicTwoPhaseFlowPipe1.dpf[1] - dynamicTwoPhaseFlowPipe1.P[2] = 0.0
352/833 (1): $cse37 = min(dynamicTwoPhaseFlowPipe1.P[1], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
353/834 (1): dynamicTwoPhaseFlowPipe1.Pb[1] = max($cse37, dynamicTwoPhaseFlowPipe1.ptriple)
354/835 (1): dynamicTwoPhaseFlowPipe1.filo[1] = if noEvent(dynamicTwoPhaseFlowPipe1.xv2[1] < 0.0) then 1.0 else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[1] >= 0.0) and noEvent(dynamicTwoPhaseFlowPipe1.xv2[1] < 0.8) then 1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[1] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[1]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[1]) else (5.0 + (-5.0) * dynamicTwoPhaseFlowPipe1.xv2[1] * dynamicTwoPhaseFlowPipe1.rgliss) * (1.0 + /*Real*/(dynamicTwoPhaseFlowPipe1.a) * dynamicTwoPhaseFlowPipe1.xv2[1] * dynamicTwoPhaseFlowPipe1.rgliss * exp((-1.1904761904761906e-7) * dynamicTwoPhaseFlowPipe1.Pb[1]) / (19.0 + 1e-5 * dynamicTwoPhaseFlowPipe1.Pb[1])) + (-4.0 + 5.0 * dynamicTwoPhaseFlowPipe1.xv2[1] * dynamicTwoPhaseFlowPipe1.rgliss) * dynamicTwoPhaseFlowPipe1.rhol2[1] * dynamicTwoPhaseFlowPipe1.lambdav[1] / (dynamicTwoPhaseFlowPipe1.lambdal[1] * dynamicTwoPhaseFlowPipe1.rhov2[1])
355/836 (1): dynamicTwoPhaseFlowPipe1.khi[1] = dynamicTwoPhaseFlowPipe1.filo[1] * dynamicTwoPhaseFlowPipe1.lambdal[1] * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.D
356/837 (1): dynamicTwoPhaseFlowPipe1.dpf[1] = 0.5 * dynamicTwoPhaseFlowPipe1.dpfCorr * dynamicTwoPhaseFlowPipe1.khi[1] * sourceP1.Q0 * abs(sourceP1.Q0) / (dynamicTwoPhaseFlowPipe1.A ^ 2.0 * dynamicTwoPhaseFlowPipe1.rhol2[1])
357/838 (10): $cse58 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicTwoPhaseFlowPipe1.P[1] + dynamicTwoPhaseFlowPipe1.P[2]), dynamicTwoPhaseFlowPipe1.hb[1], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
358/848 (1): dynamicTwoPhaseFlowPipe1.mul2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[1], dynamicTwoPhaseFlowPipe1.T2[1], dynamicTwoPhaseFlowPipe1.fluid)
359/849 (1): dynamicTwoPhaseFlowPipe1.Rel2[1] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.mul2[1]))
360/850 (1): dynamicTwoPhaseFlowPipe1.lambdal[1] = if noEvent(dynamicTwoPhaseFlowPipe1.Rel2[1] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rel2[1] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
361/851 (1): dynamicTwoPhaseFlowPipe1.muv2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicTwoPhaseFlowPipe1.rhov2[1], dynamicTwoPhaseFlowPipe1.T2[1], dynamicTwoPhaseFlowPipe1.fluid)
362/852 (1): dynamicTwoPhaseFlowPipe1.Rev2[1] = abs(4.0 * sourceP1.Q0 / (3.141592653589793 * dynamicTwoPhaseFlowPipe1.Di * dynamicTwoPhaseFlowPipe1.muv2[1]))
363/853 (1): dynamicTwoPhaseFlowPipe1.lambdav[1] = if noEvent(dynamicTwoPhaseFlowPipe1.Rev2[1] > 1.0) then 0.25 / log10(13.0 / dynamicTwoPhaseFlowPipe1.Rev2[1] + dynamicTwoPhaseFlowPipe1.rugosrel / (3.7 * dynamicTwoPhaseFlowPipe1.D)) ^ 2.0 else 0.01
364/854 (1): dynamicTwoPhaseFlowPipe1.kl2[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicTwoPhaseFlowPipe1.rhol2[1], dynamicTwoPhaseFlowPipe1.T2[1], 0.5 * (dynamicTwoPhaseFlowPipe1.P[1] + dynamicTwoPhaseFlowPipe1.P[2]), dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
365/855 (1): dynamicTwoPhaseFlowPipe1.rhol2[1] = if noEvent(dynamicTwoPhaseFlowPipe1.P[2] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[1] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[1] else max(dynamicTwoPhaseFlowPipe1.rho2[1], dynamicTwoPhaseFlowPipe1.lsat2[1].rho)
366/856 (1): dynamicTwoPhaseFlowPipe1.rhov2[1] = if noEvent(dynamicTwoPhaseFlowPipe1.P[2] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[1] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.rho2[1] else min(dynamicTwoPhaseFlowPipe1.rho2[1], dynamicTwoPhaseFlowPipe1.vsat2[1].rho)
367/857 (1): dynamicTwoPhaseFlowPipe1.cpl2[1] = if noEvent(dynamicTwoPhaseFlowPipe1.P[2] > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[1] > dynamicTwoPhaseFlowPipe1.Tcrit) then dynamicTwoPhaseFlowPipe1.pro2[1].cp else if noEvent(dynamicTwoPhaseFlowPipe1.xv2[1] <= 0.0) then dynamicTwoPhaseFlowPipe1.pro2[1].cp else dynamicTwoPhaseFlowPipe1.lsat2[1].cp
368/858 (1): dynamicTwoPhaseFlowPipe1.diff_res_e[1] = dynamicTwoPhaseFlowPipe1.rho2[1] * dynamicTwoPhaseFlowPipe1.cpl2[1] * dynamicTwoPhaseFlowPipe1.dx2 / (dynamicTwoPhaseFlowPipe1.rhol2[1] * dynamicTwoPhaseFlowPipe1.A * dynamicTwoPhaseFlowPipe1.kl2[1])
369/859 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T2[1], dynamicTwoPhaseFlowPipe1.rho2[1], dynamicTwoPhaseFlowPipe1.pro2[1].u, dynamicTwoPhaseFlowPipe1.pro2[1].s, dynamicTwoPhaseFlowPipe1.pro2[1].cp, dynamicTwoPhaseFlowPipe1.pro2[1].ddhp, dynamicTwoPhaseFlowPipe1.pro2[1].ddph, dynamicTwoPhaseFlowPipe1.pro2[1].duph, dynamicTwoPhaseFlowPipe1.pro2[1].duhp, dynamicTwoPhaseFlowPipe1.pro2[1].x) = $cse58
370/869 (1): dynamicTwoPhaseFlowPipe1.xv2[1] = if noEvent(0.5 * (dynamicTwoPhaseFlowPipe1.P[1] + dynamicTwoPhaseFlowPipe1.P[2]) > dynamicTwoPhaseFlowPipe1.pcrit) or noEvent(dynamicTwoPhaseFlowPipe1.T2[1] > dynamicTwoPhaseFlowPipe1.Tcrit) then 1.0 else dynamicTwoPhaseFlowPipe1.pro2[1].x
371/870 (1): dynamicTwoPhaseFlowPipe1.dpg[1] = 9.80665 * dynamicTwoPhaseFlowPipe1.rho2[1] * (dynamicTwoPhaseFlowPipe1.z2 - dynamicTwoPhaseFlowPipe1.z1) * dynamicTwoPhaseFlowPipe1.dx2 / dynamicTwoPhaseFlowPipe1.L
372/871 (14): (dynamicTwoPhaseFlowPipe1.lsat2[1], dynamicTwoPhaseFlowPipe1.vsat2[1]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicTwoPhaseFlowPipe1.P[1] + dynamicTwoPhaseFlowPipe1.P[2]), dynamicTwoPhaseFlowPipe1.fluid)
373/885 (10): $cse69 = ThermoSysPro.Properties.Fluid.Ph(dynamicTwoPhaseFlowPipe1.P[1], dynamicTwoPhaseFlowPipe1.h[1], dynamicTwoPhaseFlowPipe1.mode, dynamicTwoPhaseFlowPipe1.fluid)
374/895 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.proc[1].T, dynamicTwoPhaseFlowPipe1.rhoc[1], dynamicTwoPhaseFlowPipe1.proc[1].u, dynamicTwoPhaseFlowPipe1.proc[1].s, dynamicTwoPhaseFlowPipe1.proc[1].cp, dynamicTwoPhaseFlowPipe1.proc[1].ddhp, dynamicTwoPhaseFlowPipe1.proc[1].ddph, dynamicTwoPhaseFlowPipe1.proc[1].duph, dynamicTwoPhaseFlowPipe1.proc[1].duhp, dynamicTwoPhaseFlowPipe1.proc[1].x) = $cse69
375/905 (1): dynamicTwoPhaseFlowPipe1.h[1] = ThermoSysPro.Properties.Fluid.SpecificEnthalpy_PT(dynamicTwoPhaseFlowPipe1.P[1], 293.15, 1, sourceP1.mode, 0.01, 0.05, 0.22, 0.0)
376/906 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicTwoPhaseFlowPipe1.T1[1], dynamicTwoPhaseFlowPipe1.rhoc[2], dynamicTwoPhaseFlowPipe1.pro1[1].u, dynamicTwoPhaseFlowPipe1.pro1[1].s, dynamicTwoPhaseFlowPipe1.pro1[1].cp, dynamicTwoPhaseFlowPipe1.pro1[1].ddhp, dynamicTwoPhaseFlowPipe1.pro1[1].ddph, dynamicTwoPhaseFlowPipe1.pro1[1].duph, dynamicTwoPhaseFlowPipe1.pro1[1].duhp, dynamicTwoPhaseFlowPipe1.pro1[1].x) = $cse38
377/916 (1): $cse39 = min(dynamicTwoPhaseFlowPipe1.P[2], dynamicTwoPhaseFlowPipe1.pcrit - 1.0)
378/917 (1): dynamicTwoPhaseFlowPipe1.Pb[2] = max($cse39, dynamicTwoPhaseFlowPipe1.ptriple)

Variables:
1: dynamicTwoPhaseFlowPipe1.Pb[2]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
2: $cse39:VARIABLE(protected = true )  type: Real unreplaceable
3: dynamicTwoPhaseFlowPipe1.pro1[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
4: dynamicTwoPhaseFlowPipe1.pro1[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
5: dynamicTwoPhaseFlowPipe1.T1[1]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
6: dynamicTwoPhaseFlowPipe1.pro1[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
7: dynamicTwoPhaseFlowPipe1.pro1[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
8: dynamicTwoPhaseFlowPipe1.pro1[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
9: dynamicTwoPhaseFlowPipe1.pro1[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
10: dynamicTwoPhaseFlowPipe1.pro1[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
11: dynamicTwoPhaseFlowPipe1.h[1]:VARIABLE(start = 84011.8111671368 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
12: dynamicTwoPhaseFlowPipe1.proc[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [2]
13: dynamicTwoPhaseFlowPipe1.proc[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [2]
14: dynamicTwoPhaseFlowPipe1.proc[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [2]
15: dynamicTwoPhaseFlowPipe1.proc[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [2]
16: dynamicTwoPhaseFlowPipe1.proc[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [2]
17: dynamicTwoPhaseFlowPipe1.proc[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [2]
18: dynamicTwoPhaseFlowPipe1.proc[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [2]
19: dynamicTwoPhaseFlowPipe1.rhoc[1]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
20: dynamicTwoPhaseFlowPipe1.proc[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [2]
21: dynamicTwoPhaseFlowPipe1.proc[1].T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 )  "Temperature" type: Real [2]
22: $cse69.cp:VARIABLE(protected = true )  type: Real unreplaceable
23: $cse69.ddph:VARIABLE(protected = true )  type: Real unreplaceable
24: $cse69.x:VARIABLE(protected = true )  type: Real unreplaceable
25: $cse69.d:VARIABLE(protected = true )  type: Real unreplaceable
26: $cse69.u:VARIABLE(protected = true )  type: Real unreplaceable
27: $cse69.s:VARIABLE(protected = true )  type: Real unreplaceable
28: $cse69.duhp:VARIABLE(protected = true )  type: Real unreplaceable
29: $cse69.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
30: $cse69.duph:VARIABLE(protected = true )  type: Real unreplaceable
31: $cse69.T:VARIABLE(protected = true )  type: Real unreplaceable
32: dynamicTwoPhaseFlowPipe1.lsat2[1].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
33: dynamicTwoPhaseFlowPipe1.lsat2[1].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
34: dynamicTwoPhaseFlowPipe1.vsat2[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
35: dynamicTwoPhaseFlowPipe1.lsat2[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
36: dynamicTwoPhaseFlowPipe1.lsat2[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
37: dynamicTwoPhaseFlowPipe1.lsat2[1].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
38: dynamicTwoPhaseFlowPipe1.lsat2[1].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
39: dynamicTwoPhaseFlowPipe1.vsat2[1].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
40: dynamicTwoPhaseFlowPipe1.lsat2[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
41: dynamicTwoPhaseFlowPipe1.vsat2[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
42: dynamicTwoPhaseFlowPipe1.vsat2[1].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
43: dynamicTwoPhaseFlowPipe1.vsat2[1].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
44: dynamicTwoPhaseFlowPipe1.vsat2[1].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
45: dynamicTwoPhaseFlowPipe1.vsat2[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
46: dynamicTwoPhaseFlowPipe1.dpg[1]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
47: dynamicTwoPhaseFlowPipe1.xv2[1]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
48: dynamicTwoPhaseFlowPipe1.pro2[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
49: $cse58.x:VARIABLE(protected = true )  type: Real unreplaceable
50: dynamicTwoPhaseFlowPipe1.kl2[1]:VARIABLE(start = 0.5995743350581909 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
51: dynamicTwoPhaseFlowPipe1.cpl2[1]:VARIABLE(start = 4183.8461052314415 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
52: dynamicTwoPhaseFlowPipe1.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]
53: dynamicTwoPhaseFlowPipe1.pro2[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
54: dynamicTwoPhaseFlowPipe1.pro2[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
55: dynamicTwoPhaseFlowPipe1.pro2[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
56: dynamicTwoPhaseFlowPipe1.pro2[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
57: dynamicTwoPhaseFlowPipe1.pro2[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
58: dynamicTwoPhaseFlowPipe1.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]
59: dynamicTwoPhaseFlowPipe1.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]
60: dynamicTwoPhaseFlowPipe1.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]
61: dynamicTwoPhaseFlowPipe1.lambdav[1]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
62: dynamicTwoPhaseFlowPipe1.Rev2[1]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
63: dynamicTwoPhaseFlowPipe1.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]
64: dynamicTwoPhaseFlowPipe1.lambdal[1]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
65: dynamicTwoPhaseFlowPipe1.Rel2[1]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
66: dynamicTwoPhaseFlowPipe1.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]
67: dynamicTwoPhaseFlowPipe1.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]
68: dynamicTwoPhaseFlowPipe1.pro2[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
69: $cse58.T:VARIABLE(protected = true )  type: Real unreplaceable
70: $cse58.u:VARIABLE(protected = true )  type: Real unreplaceable
71: $cse58.ddph:VARIABLE(protected = true )  type: Real unreplaceable
72: $cse58.cp:VARIABLE(protected = true )  type: Real unreplaceable
73: $cse58.s:VARIABLE(protected = true )  type: Real unreplaceable
74: $cse58.duph:VARIABLE(protected = true )  type: Real unreplaceable
75: dynamicTwoPhaseFlowPipe1.hb[1]:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
76: $cse58.d:VARIABLE(protected = true )  type: Real unreplaceable
77: $cse58.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
78: $cse58.duhp:VARIABLE(protected = true )  type: Real unreplaceable
79: dynamicTwoPhaseFlowPipe1.dpf[1]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
80: dynamicTwoPhaseFlowPipe1.khi[1]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
81: dynamicTwoPhaseFlowPipe1.filo[1]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
82: dynamicTwoPhaseFlowPipe1.Pb[1]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
83: $cse37:VARIABLE(protected = true )  type: Real unreplaceable
84: dynamicTwoPhaseFlowPipe1.P[1]:VARIABLE(min = 0.0 start = 99999.999999976 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
85: dynamicTwoPhaseFlowPipe1.dpa[1]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
86: dynamicTwoPhaseFlowPipe1.dpg[3]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
87: dynamicTwoPhaseFlowPipe1.J[2]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
88: dynamicTwoPhaseFlowPipe1.gamma_s[2]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
89: dynamicTwoPhaseFlowPipe1.gamma_e[3]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
90: dynamicTwoPhaseFlowPipe1.rs[2]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
91: dynamicTwoPhaseFlowPipe1.lsat2[3].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
92: dynamicTwoPhaseFlowPipe1.lsat2[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
93: dynamicTwoPhaseFlowPipe1.lsat2[3].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
94: dynamicTwoPhaseFlowPipe1.lsat2[3].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
95: dynamicTwoPhaseFlowPipe1.vsat2[3].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
96: dynamicTwoPhaseFlowPipe1.lsat2[3].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
97: dynamicTwoPhaseFlowPipe1.vsat2[3].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
98: dynamicTwoPhaseFlowPipe1.vsat2[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
99: dynamicTwoPhaseFlowPipe1.lsat2[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
100: dynamicTwoPhaseFlowPipe1.vsat2[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
101: dynamicTwoPhaseFlowPipe1.vsat2[3].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
102: dynamicTwoPhaseFlowPipe1.lsat2[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
103: dynamicTwoPhaseFlowPipe1.vsat2[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
104: dynamicTwoPhaseFlowPipe1.vsat2[3].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
105: dynamicTwoPhaseFlowPipe1.pro2[3].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
106: dynamicTwoPhaseFlowPipe1.pro2[3].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
107: dynamicTwoPhaseFlowPipe1.pro2[3].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
108: $cse60.s:VARIABLE(protected = true )  type: Real unreplaceable
109: dynamicTwoPhaseFlowPipe1.pro2[3].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
110: dynamicTwoPhaseFlowPipe1.pro2[3].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
111: dynamicTwoPhaseFlowPipe1.pro2[3].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
112: $cse60.x:VARIABLE(protected = true )  type: Real unreplaceable
113: $cse60.cp:VARIABLE(protected = true )  type: Real unreplaceable
114: $cse60.duhp:VARIABLE(protected = true )  type: Real unreplaceable
115: $cse60.T:VARIABLE(protected = true )  type: Real unreplaceable
116: $cse60.u:VARIABLE(protected = true )  type: Real unreplaceable
117: $cse60.ddph:VARIABLE(protected = true )  type: Real unreplaceable
118: dynamicTwoPhaseFlowPipe1.Pb[4]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
119: $cse43:VARIABLE(protected = true )  type: Real unreplaceable
120: dynamicTwoPhaseFlowPipe1.gamma_s[1]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
121: dynamicTwoPhaseFlowPipe1.gamma[2]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
122: dynamicTwoPhaseFlowPipe1.Js[1]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
123: dynamicTwoPhaseFlowPipe1.rs[1]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
124: dynamicTwoPhaseFlowPipe1.re[2]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
125: dynamicTwoPhaseFlowPipe1.diff_res_e[2]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
126: dynamicTwoPhaseFlowPipe1.gamma_e[2]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
127: dynamicTwoPhaseFlowPipe1.Je[2]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
128: dynamicTwoPhaseFlowPipe1.Js[2]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
129: dynamicTwoPhaseFlowPipe1.gamma_s[3]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
130: dynamicTwoPhaseFlowPipe1.gamma_e[4]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
131: dynamicTwoPhaseFlowPipe1.rs[3]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
132: dynamicTwoPhaseFlowPipe1.J[3]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
133: dynamicTwoPhaseFlowPipe1.dpg[4]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
134: dynamicTwoPhaseFlowPipe1.pro2[4].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
135: dynamicTwoPhaseFlowPipe1.pro2[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
136: dynamicTwoPhaseFlowPipe1.pro2[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
137: dynamicTwoPhaseFlowPipe1.pro2[4].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
138: dynamicTwoPhaseFlowPipe1.pro2[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
139: dynamicTwoPhaseFlowPipe1.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]
140: dynamicTwoPhaseFlowPipe1.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]
141: dynamicTwoPhaseFlowPipe1.xv2[4]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
142: dynamicTwoPhaseFlowPipe1.cpl2[4]:VARIABLE(start = 4180.086463719214 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
143: dynamicTwoPhaseFlowPipe1.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]
144: dynamicTwoPhaseFlowPipe1.kl2[4]:VARIABLE(start = 0.5995743350562764 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
145: dynamicTwoPhaseFlowPipe1.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]
146: dynamicTwoPhaseFlowPipe1.lsat2[4].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
147: dynamicTwoPhaseFlowPipe1.lsat2[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
148: dynamicTwoPhaseFlowPipe1.lsat2[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
149: dynamicTwoPhaseFlowPipe1.vsat2[4].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
150: dynamicTwoPhaseFlowPipe1.vsat2[4].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
151: dynamicTwoPhaseFlowPipe1.vsat2[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
152: dynamicTwoPhaseFlowPipe1.vsat2[4].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
153: dynamicTwoPhaseFlowPipe1.vsat2[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
154: dynamicTwoPhaseFlowPipe1.vsat2[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
155: dynamicTwoPhaseFlowPipe1.lsat2[4].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
156: dynamicTwoPhaseFlowPipe1.lsat2[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
157: dynamicTwoPhaseFlowPipe1.lsat2[4].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
158: dynamicTwoPhaseFlowPipe1.lsat2[4].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
159: dynamicTwoPhaseFlowPipe1.vsat2[4].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
160: dynamicTwoPhaseFlowPipe1.Pb[5]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
161: $cse45:VARIABLE(protected = true )  type: Real unreplaceable
162: dynamicTwoPhaseFlowPipe1.T1[4]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
163: dynamicTwoPhaseFlowPipe1.pro1[4].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
164: dynamicTwoPhaseFlowPipe1.pro1[4].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
165: dynamicTwoPhaseFlowPipe1.pro1[4].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
166: dynamicTwoPhaseFlowPipe1.pro1[4].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
167: dynamicTwoPhaseFlowPipe1.pro1[4].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
168: dynamicTwoPhaseFlowPipe1.pro1[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
169: dynamicTwoPhaseFlowPipe1.vsat2[5].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
170: dynamicTwoPhaseFlowPipe1.vsat2[5].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
171: dynamicTwoPhaseFlowPipe1.vsat2[5].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
172: dynamicTwoPhaseFlowPipe1.lsat2[5].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
173: dynamicTwoPhaseFlowPipe1.vsat2[5].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
174: dynamicTwoPhaseFlowPipe1.vsat2[5].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
175: dynamicTwoPhaseFlowPipe1.lsat2[5].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
176: dynamicTwoPhaseFlowPipe1.lsat2[5].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
177: dynamicTwoPhaseFlowPipe1.vsat2[5].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
178: dynamicTwoPhaseFlowPipe1.lsat2[5].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
179: dynamicTwoPhaseFlowPipe1.vsat2[5].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
180: dynamicTwoPhaseFlowPipe1.dpg[5]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
181: $cse62.duhp:VARIABLE(protected = true )  type: Real unreplaceable
182: dynamicTwoPhaseFlowPipe1.pro2[5].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
183: dynamicTwoPhaseFlowPipe1.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]
184: dynamicTwoPhaseFlowPipe1.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]
185: dynamicTwoPhaseFlowPipe1.xv2[5]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
186: dynamicTwoPhaseFlowPipe1.pro2[5].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
187: dynamicTwoPhaseFlowPipe1.pro2[5].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
188: dynamicTwoPhaseFlowPipe1.pro2[5].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
189: dynamicTwoPhaseFlowPipe1.pro2[5].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
190: dynamicTwoPhaseFlowPipe1.pro2[5].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
191: dynamicTwoPhaseFlowPipe1.pro2[5].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
192: dynamicTwoPhaseFlowPipe1.hb[5]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
193: $cse62.duph:VARIABLE(protected = true )  type: Real unreplaceable
194: $cse62.s:VARIABLE(protected = true )  type: Real unreplaceable
195: $cse62.u:VARIABLE(protected = true )  type: Real unreplaceable
196: $cse62.ddph:VARIABLE(protected = true )  type: Real unreplaceable
197: $cse62.cp:VARIABLE(protected = true )  type: Real unreplaceable
198: $cse62.d:VARIABLE(protected = true )  type: Real unreplaceable
199: $cse62.x:VARIABLE(protected = true )  type: Real unreplaceable
200: $cse62.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
201: $cse62.T:VARIABLE(protected = true )  type: Real unreplaceable
202: dynamicTwoPhaseFlowPipe1.Pb[6]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
203: $cse47:VARIABLE(protected = true )  type: Real unreplaceable
204: dynamicTwoPhaseFlowPipe1.pro1[5].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
205: dynamicTwoPhaseFlowPipe1.pro1[5].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
206: dynamicTwoPhaseFlowPipe1.dpg[6]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
207: dynamicTwoPhaseFlowPipe1.lsat2[6].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
208: dynamicTwoPhaseFlowPipe1.vsat2[6].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
209: dynamicTwoPhaseFlowPipe1.lsat2[6].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
210: dynamicTwoPhaseFlowPipe1.vsat2[6].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
211: dynamicTwoPhaseFlowPipe1.vsat2[6].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
212: dynamicTwoPhaseFlowPipe1.lsat2[6].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
213: dynamicTwoPhaseFlowPipe1.lsat2[6].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
214: dynamicTwoPhaseFlowPipe1.vsat2[6].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
215: dynamicTwoPhaseFlowPipe1.vsat2[6].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
216: dynamicTwoPhaseFlowPipe1.vsat2[6].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
217: dynamicTwoPhaseFlowPipe1.lsat2[6].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
218: dynamicTwoPhaseFlowPipe1.lsat2[6].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
219: dynamicTwoPhaseFlowPipe1.lsat2[6].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
220: dynamicTwoPhaseFlowPipe1.vsat2[6].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
221: $cse63.ddph:VARIABLE(protected = true )  type: Real unreplaceable
222: dynamicTwoPhaseFlowPipe1.pro2[6].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
223: dynamicTwoPhaseFlowPipe1.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]
224: dynamicTwoPhaseFlowPipe1.pro2[6].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
225: dynamicTwoPhaseFlowPipe1.pro2[6].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
226: dynamicTwoPhaseFlowPipe1.J[5]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
227: dynamicTwoPhaseFlowPipe1.hb[6]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
228: $cse63.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
229: $cse63.s:VARIABLE(protected = true )  type: Real unreplaceable
230: dynamicTwoPhaseFlowPipe1.Pb[7]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
231: $cse49:VARIABLE(protected = true )  type: Real unreplaceable
232: dynamicTwoPhaseFlowPipe1.T1[6]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
233: dynamicTwoPhaseFlowPipe1.pro1[6].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
234: dynamicTwoPhaseFlowPipe1.pro1[6].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
235: dynamicTwoPhaseFlowPipe1.pro1[6].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
236: dynamicTwoPhaseFlowPipe1.pro1[6].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
237: dynamicTwoPhaseFlowPipe1.pro1[6].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
238: dynamicTwoPhaseFlowPipe1.pro1[6].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
239: dynamicTwoPhaseFlowPipe1.vsat2[7].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
240: dynamicTwoPhaseFlowPipe1.vsat2[7].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
241: dynamicTwoPhaseFlowPipe1.vsat2[7].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
242: dynamicTwoPhaseFlowPipe1.dpg[7]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
243: $cse64.d:VARIABLE(protected = true )  type: Real unreplaceable
244: dynamicTwoPhaseFlowPipe1.pro2[7].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
245: dynamicTwoPhaseFlowPipe1.pro2[7].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
246: dynamicTwoPhaseFlowPipe1.pro2[7].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
247: dynamicTwoPhaseFlowPipe1.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]
248: dynamicTwoPhaseFlowPipe1.cpl2[7]:VARIABLE(start = 4178.639109839789 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
249: dynamicTwoPhaseFlowPipe1.xv2[7]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
250: dynamicTwoPhaseFlowPipe1.pro2[7].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
251: dynamicTwoPhaseFlowPipe1.pro2[7].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
252: dynamicTwoPhaseFlowPipe1.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]
253: dynamicTwoPhaseFlowPipe1.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]
254: dynamicTwoPhaseFlowPipe1.pro2[7].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
255: dynamicTwoPhaseFlowPipe1.pro2[7].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
256: dynamicTwoPhaseFlowPipe1.J[6]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
257: dynamicTwoPhaseFlowPipe1.hb[7]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
258: $cse64.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
259: $cse64.ddph:VARIABLE(protected = true )  type: Real unreplaceable
260: $cse64.s:VARIABLE(protected = true )  type: Real unreplaceable
261: $cse64.cp:VARIABLE(protected = true )  type: Real unreplaceable
262: $cse64.u:VARIABLE(protected = true )  type: Real unreplaceable
263: $cse64.duhp:VARIABLE(protected = true )  type: Real unreplaceable
264: $cse64.x:VARIABLE(protected = true )  type: Real unreplaceable
265: $cse64.duph:VARIABLE(protected = true )  type: Real unreplaceable
266: $cse64.T:VARIABLE(protected = true )  type: Real unreplaceable
267: dynamicTwoPhaseFlowPipe1.Pb[8]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
268: $cse51:VARIABLE(protected = true )  type: Real unreplaceable
269: dynamicTwoPhaseFlowPipe1.gamma_s[7]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
270: dynamicTwoPhaseFlowPipe1.gamma_e[8]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
271: dynamicTwoPhaseFlowPipe1.rs[7]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
272: dynamicTwoPhaseFlowPipe1.J[7]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
273: dynamicTwoPhaseFlowPipe1.dpg[8]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
274: dynamicTwoPhaseFlowPipe1.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]
275: dynamicTwoPhaseFlowPipe1.pro2[8].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
276: dynamicTwoPhaseFlowPipe1.pro2[8].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
277: dynamicTwoPhaseFlowPipe1.pro2[8].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
278: dynamicTwoPhaseFlowPipe1.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]
279: dynamicTwoPhaseFlowPipe1.pro2[8].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
280: dynamicTwoPhaseFlowPipe1.pro2[8].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
281: dynamicTwoPhaseFlowPipe1.xv2[8]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
282: dynamicTwoPhaseFlowPipe1.kl2[8]:VARIABLE(start = 0.5995743350539415 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
283: dynamicTwoPhaseFlowPipe1.cpl2[8]:VARIABLE(start = 4178.550383980675 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
284: dynamicTwoPhaseFlowPipe1.vsat2[8].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
285: dynamicTwoPhaseFlowPipe1.lsat2[8].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
286: dynamicTwoPhaseFlowPipe1.vsat2[8].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
287: dynamicTwoPhaseFlowPipe1.vsat2[8].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
288: dynamicTwoPhaseFlowPipe1.vsat2[8].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
289: dynamicTwoPhaseFlowPipe1.lsat2[8].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
290: dynamicTwoPhaseFlowPipe1.lsat2[8].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
291: dynamicTwoPhaseFlowPipe1.vsat2[8].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
292: dynamicTwoPhaseFlowPipe1.lsat2[8].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
293: dynamicTwoPhaseFlowPipe1.vsat2[8].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
294: dynamicTwoPhaseFlowPipe1.lsat2[8].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
295: dynamicTwoPhaseFlowPipe1.lsat2[8].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
296: dynamicTwoPhaseFlowPipe1.lsat2[8].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
297: dynamicTwoPhaseFlowPipe1.vsat2[8].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
298: dynamicTwoPhaseFlowPipe1.Pb[9]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
299: $cse53:VARIABLE(protected = true )  type: Real unreplaceable
300: dynamicTwoPhaseFlowPipe1.Je[7]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
301: dynamicTwoPhaseFlowPipe1.Js[7]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
302: dynamicTwoPhaseFlowPipe1.dpg[9]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
303: dynamicTwoPhaseFlowPipe1.pro2[9].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
304: dynamicTwoPhaseFlowPipe1.pro2[9].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
305: dynamicTwoPhaseFlowPipe1.pro2[9].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
306: dynamicTwoPhaseFlowPipe1.pro2[9].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
307: dynamicTwoPhaseFlowPipe1.pro2[9].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
308: dynamicTwoPhaseFlowPipe1.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]
309: dynamicTwoPhaseFlowPipe1.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]
310: dynamicTwoPhaseFlowPipe1.pro2[9].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
311: dynamicTwoPhaseFlowPipe1.pro2[9].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
312: dynamicTwoPhaseFlowPipe1.xv2[9]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
313: dynamicTwoPhaseFlowPipe1.lambdav[9]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
314: dynamicTwoPhaseFlowPipe1.Rev2[9]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
315: dynamicTwoPhaseFlowPipe1.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]
316: dynamicTwoPhaseFlowPipe1.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]
317: dynamicTwoPhaseFlowPipe1.vsat2[9].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
318: dynamicTwoPhaseFlowPipe1.lsat2[9].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
319: dynamicTwoPhaseFlowPipe1.lsat2[9].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
320: dynamicTwoPhaseFlowPipe1.vsat2[9].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
321: dynamicTwoPhaseFlowPipe1.vsat2[9].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
322: dynamicTwoPhaseFlowPipe1.lsat2[9].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
323: dynamicTwoPhaseFlowPipe1.lsat2[9].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
324: dynamicTwoPhaseFlowPipe1.vsat2[9].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
325: dynamicTwoPhaseFlowPipe1.vsat2[9].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
326: dynamicTwoPhaseFlowPipe1.vsat2[9].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
327: dynamicTwoPhaseFlowPipe1.Pb[10]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
328: $cse55:VARIABLE(protected = true )  type: Real unreplaceable
329: dynamicTwoPhaseFlowPipe1.pro1[9].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
330: dynamicTwoPhaseFlowPipe1.pro1[9].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
331: dynamicTwoPhaseFlowPipe1.T1[9]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
332: dynamicTwoPhaseFlowPipe1.pro1[9].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
333: dynamicTwoPhaseFlowPipe1.pro1[9].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
334: dynamicTwoPhaseFlowPipe1.pro1[9].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
335: dynamicTwoPhaseFlowPipe1.pro1[9].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
336: dynamicTwoPhaseFlowPipe1.pro1[9].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
337: dynamicTwoPhaseFlowPipe1.lsat2[11].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
338: dynamicTwoPhaseFlowPipe1.lsat2[11].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
339: dynamicTwoPhaseFlowPipe1.vsat2[11].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
340: dynamicTwoPhaseFlowPipe1.vsat2[11].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
341: dynamicTwoPhaseFlowPipe1.lsat2[11].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
342: dynamicTwoPhaseFlowPipe1.vsat2[11].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
343: dynamicTwoPhaseFlowPipe1.vsat2[11].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
344: dynamicTwoPhaseFlowPipe1.lsat2[11].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
345: dynamicTwoPhaseFlowPipe1.lsat2[11].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
346: dynamicTwoPhaseFlowPipe1.lsat2[11].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
347: dynamicTwoPhaseFlowPipe1.vsat2[11].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
348: dynamicTwoPhaseFlowPipe1.vsat2[11].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
349: dynamicTwoPhaseFlowPipe1.lsat2[11].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
350: dynamicTwoPhaseFlowPipe1.vsat2[11].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
351: dynamicTwoPhaseFlowPipe1.vsat2[10].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
352: dynamicTwoPhaseFlowPipe1.vsat2[10].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
353: dynamicTwoPhaseFlowPipe1.lsat2[10].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
354: dynamicTwoPhaseFlowPipe1.lsat2[10].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
355: dynamicTwoPhaseFlowPipe1.lsat2[10].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
356: dynamicTwoPhaseFlowPipe1.lsat2[10].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
357: dynamicTwoPhaseFlowPipe1.lsat2[10].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
358: dynamicTwoPhaseFlowPipe1.lsat2[10].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
359: dynamicTwoPhaseFlowPipe1.vsat2[10].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
360: dynamicTwoPhaseFlowPipe1.vsat2[10].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
361: dynamicTwoPhaseFlowPipe1.dpg[10]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
362: dynamicTwoPhaseFlowPipe1.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]
363: dynamicTwoPhaseFlowPipe1.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]
364: dynamicTwoPhaseFlowPipe1.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]
365: dynamicTwoPhaseFlowPipe1.pro2[10].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
366: $cse67.duhp:VARIABLE(protected = true )  type: Real unreplaceable
367: dynamicTwoPhaseFlowPipe1.pro2[10].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
368: dynamicTwoPhaseFlowPipe1.pro2[10].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
369: dynamicTwoPhaseFlowPipe1.pro2[10].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
370: dynamicTwoPhaseFlowPipe1.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]
371: dynamicTwoPhaseFlowPipe1.pro2[10].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
372: dynamicTwoPhaseFlowPipe1.xv2[10]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
373: dynamicTwoPhaseFlowPipe1.pro2[10].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
374: dynamicTwoPhaseFlowPipe1.pro2[10].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
375: dynamicTwoPhaseFlowPipe1.J[9]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
376: dynamicTwoPhaseFlowPipe1.hb[10]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
377: $cse67.u:VARIABLE(protected = true )  type: Real unreplaceable
378: $cse67.d:VARIABLE(protected = true )  type: Real unreplaceable
379: $cse67.duph:VARIABLE(protected = true )  type: Real unreplaceable
380: $cse67.ddph:VARIABLE(protected = true )  type: Real unreplaceable
381: $cse67.x:VARIABLE(protected = true )  type: Real unreplaceable
382: $cse67.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
383: $cse67.cp:VARIABLE(protected = true )  type: Real unreplaceable
384: $cse67.s:VARIABLE(protected = true )  type: Real unreplaceable
385: $cse67.T:VARIABLE(protected = true )  type: Real unreplaceable
386: dynamicTwoPhaseFlowPipe1.Pb[11]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
387: $cse57:VARIABLE(protected = true )  type: Real unreplaceable
388: dynamicTwoPhaseFlowPipe1.gamma_s[10]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
389: dynamicTwoPhaseFlowPipe1.dpg[11]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
390: dynamicTwoPhaseFlowPipe1.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]
391: dynamicTwoPhaseFlowPipe1.pro2[11].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
392: dynamicTwoPhaseFlowPipe1.xv2[11]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
393: dynamicTwoPhaseFlowPipe1.pro2[11].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
394: dynamicTwoPhaseFlowPipe1.pro2[11].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
395: dynamicTwoPhaseFlowPipe1.cpl2[11]:VARIABLE(start = 4179.2962820044995 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
396: dynamicTwoPhaseFlowPipe1.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]
397: dynamicTwoPhaseFlowPipe1.J[10]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
398: dynamicTwoPhaseFlowPipe1.hb[11]:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
399: $cse68.u:VARIABLE(protected = true )  type: Real unreplaceable
400: $cse68.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
401: $cse68.d:VARIABLE(protected = true )  type: Real unreplaceable
402: $cse68.ddph:VARIABLE(protected = true )  type: Real unreplaceable
403: $cse68.cp:VARIABLE(protected = true )  type: Real unreplaceable
404: $cse68.duph:VARIABLE(protected = true )  type: Real unreplaceable
405: $cse68.s:VARIABLE(protected = true )  type: Real unreplaceable
406: $cse68.x:VARIABLE(protected = true )  type: Real unreplaceable
407: $cse68.T:VARIABLE(protected = true )  type: Real unreplaceable
408: $cse68.duhp:VARIABLE(protected = true )  type: Real unreplaceable
409: dynamicTwoPhaseFlowPipe1.pro2[11].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
410: dynamicTwoPhaseFlowPipe1.pro2[11].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
411: dynamicTwoPhaseFlowPipe1.pro2[11].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
412: dynamicTwoPhaseFlowPipe1.pro2[11].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
413: dynamicTwoPhaseFlowPipe1.lambdav[11]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
414: dynamicTwoPhaseFlowPipe1.Rev2[11]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
415: dynamicTwoPhaseFlowPipe1.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]
416: dynamicTwoPhaseFlowPipe1.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]
417: dynamicTwoPhaseFlowPipe1.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]
418: dynamicTwoPhaseFlowPipe1.kl2[11]:VARIABLE(start = 0.5995743403506435 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
419: dynamicTwoPhaseFlowPipe1.pro1[10].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
420: dynamicTwoPhaseFlowPipe1.pro1[10].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
421: dynamicTwoPhaseFlowPipe1.pro1[10].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
422: dynamicTwoPhaseFlowPipe1.pro1[10].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
423: $cse56.x:VARIABLE(protected = true )  type: Real unreplaceable
424: $cse56.duph:VARIABLE(protected = true )  type: Real unreplaceable
425: $cse56.s:VARIABLE(protected = true )  type: Real unreplaceable
426: $cse56.T:VARIABLE(protected = true )  type: Real unreplaceable
427: $cse56.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
428: $cse56.cp:VARIABLE(protected = true )  type: Real unreplaceable
429: $cse56.u:VARIABLE(protected = true )  type: Real unreplaceable
430: dynamicTwoPhaseFlowPipe1.pro1[10].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
431: dynamicTwoPhaseFlowPipe1.pro1[10].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
432: dynamicTwoPhaseFlowPipe1.T1[10]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
433: dynamicTwoPhaseFlowPipe1.pro1[10].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
434: dynamicTwoPhaseFlowPipe1.pro1[10].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
435: dynamicTwoPhaseFlowPipe1.rhoc[11]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
436: dynamicTwoPhaseFlowPipe1.dpa[11]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
437: dynamicTwoPhaseFlowPipe1.dpf[11]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
438: dynamicTwoPhaseFlowPipe1.khi[11]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
439: dynamicTwoPhaseFlowPipe1.filo[11]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
440: dynamicTwoPhaseFlowPipe1.lambdal[11]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
441: dynamicTwoPhaseFlowPipe1.Rel2[11]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
442: dynamicTwoPhaseFlowPipe1.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]
443: dynamicTwoPhaseFlowPipe1.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]
444: dynamicTwoPhaseFlowPipe1.Je[10]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
445: dynamicTwoPhaseFlowPipe1.Js[10]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
446: dynamicTwoPhaseFlowPipe1.rs[10]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
447: dynamicTwoPhaseFlowPipe1.diff_res_s[10]:VARIABLE()  "Diffusion resistance at outlet of thermal node i" type: Real [10]
448: dynamicTwoPhaseFlowPipe1.gamma[11]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
449: dynamicTwoPhaseFlowPipe1.gamma_s[9]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
450: dynamicTwoPhaseFlowPipe1.gamma_e[10]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
451: dynamicTwoPhaseFlowPipe1.rs[9]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
452: dynamicTwoPhaseFlowPipe1.rs[8]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
453: dynamicTwoPhaseFlowPipe1.Js[8]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
454: dynamicTwoPhaseFlowPipe1.gamma_s[8]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
455: dynamicTwoPhaseFlowPipe1.gamma_e[9]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
456: dynamicTwoPhaseFlowPipe1.gamma[9]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
457: dynamicTwoPhaseFlowPipe1.diff_res_e[9]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
458: dynamicTwoPhaseFlowPipe1.re[9]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
459: dynamicTwoPhaseFlowPipe1.Je[9]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
460: dynamicTwoPhaseFlowPipe1.Js[9]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
461: dynamicTwoPhaseFlowPipe1.h[10]:VARIABLE(start = 187192.78587129858 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
462: dynamicTwoPhaseFlowPipe1.re[10]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
463: dynamicTwoPhaseFlowPipe1.diff_res_e[10]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
464: dynamicTwoPhaseFlowPipe1.gamma[10]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
465: dynamicTwoPhaseFlowPipe1.h[11]:VARIABLE(start = 198328.3807233511 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
466: $cse56.duhp:VARIABLE(protected = true )  type: Real unreplaceable
467: $cse56.d:VARIABLE(protected = true )  type: Real unreplaceable
468: $cse56.ddph:VARIABLE(protected = true )  type: Real unreplaceable
469: dynamicTwoPhaseFlowPipe1.P[11]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
470: dynamicTwoPhaseFlowPipe1.vsat2[10].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
471: dynamicTwoPhaseFlowPipe1.vsat2[10].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
472: dynamicTwoPhaseFlowPipe1.vsat2[10].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
473: dynamicTwoPhaseFlowPipe1.lsat2[10].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
474: dynamicTwoPhaseFlowPipe1.cpl2[10]:VARIABLE(start = 4178.886733579299 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
475: dynamicTwoPhaseFlowPipe1.kl2[10]:VARIABLE(start = 0.599574335053346 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
476: dynamicTwoPhaseFlowPipe1.lambdal[10]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
477: dynamicTwoPhaseFlowPipe1.Rel2[10]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
478: dynamicTwoPhaseFlowPipe1.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]
479: dynamicTwoPhaseFlowPipe1.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]
480: dynamicTwoPhaseFlowPipe1.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]
481: dynamicTwoPhaseFlowPipe1.Rev2[10]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
482: dynamicTwoPhaseFlowPipe1.lambdav[10]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
483: dynamicTwoPhaseFlowPipe1.filo[10]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
484: dynamicTwoPhaseFlowPipe1.khi[10]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
485: dynamicTwoPhaseFlowPipe1.dpf[10]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
486: dynamicTwoPhaseFlowPipe1.dpa[10]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
487: dynamicTwoPhaseFlowPipe1.rhoc[10]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
488: dynamicTwoPhaseFlowPipe1.pro1[9].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
489: $cse54.duhp:VARIABLE(protected = true )  type: Real unreplaceable
490: $cse54.u:VARIABLE(protected = true )  type: Real unreplaceable
491: $cse54.T:VARIABLE(protected = true )  type: Real unreplaceable
492: $cse54.cp:VARIABLE(protected = true )  type: Real unreplaceable
493: $cse54.d:VARIABLE(protected = true )  type: Real unreplaceable
494: $cse54.ddph:VARIABLE(protected = true )  type: Real unreplaceable
495: $cse54.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
496: $cse54.duph:VARIABLE(protected = true )  type: Real unreplaceable
497: $cse54.s:VARIABLE(protected = true )  type: Real unreplaceable
498: $cse54.x:VARIABLE(protected = true )  type: Real unreplaceable
499: dynamicTwoPhaseFlowPipe1.P[10]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
500: dynamicTwoPhaseFlowPipe1.vsat2[9].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
501: dynamicTwoPhaseFlowPipe1.lsat2[9].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
502: dynamicTwoPhaseFlowPipe1.lsat2[9].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
503: dynamicTwoPhaseFlowPipe1.lsat2[9].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
504: dynamicTwoPhaseFlowPipe1.pro1[8].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
505: dynamicTwoPhaseFlowPipe1.pro1[8].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
506: dynamicTwoPhaseFlowPipe1.pro1[8].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
507: dynamicTwoPhaseFlowPipe1.T1[8]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
508: dynamicTwoPhaseFlowPipe1.pro1[8].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
509: dynamicTwoPhaseFlowPipe1.pro1[8].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
510: dynamicTwoPhaseFlowPipe1.pro1[8].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
511: dynamicTwoPhaseFlowPipe1.pro1[8].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
512: $cse52.ddph:VARIABLE(protected = true )  type: Real unreplaceable
513: $cse52.s:VARIABLE(protected = true )  type: Real unreplaceable
514: $cse52.duhp:VARIABLE(protected = true )  type: Real unreplaceable
515: $cse52.d:VARIABLE(protected = true )  type: Real unreplaceable
516: $cse52.T:VARIABLE(protected = true )  type: Real unreplaceable
517: $cse52.u:VARIABLE(protected = true )  type: Real unreplaceable
518: $cse52.cp:VARIABLE(protected = true )  type: Real unreplaceable
519: $cse52.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
520: $cse52.duph:VARIABLE(protected = true )  type: Real unreplaceable
521: $cse52.x:VARIABLE(protected = true )  type: Real unreplaceable
522: dynamicTwoPhaseFlowPipe1.pro1[8].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
523: dynamicTwoPhaseFlowPipe1.rhoc[9]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
524: dynamicTwoPhaseFlowPipe1.dpa[9]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
525: dynamicTwoPhaseFlowPipe1.dpf[9]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
526: dynamicTwoPhaseFlowPipe1.khi[9]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
527: dynamicTwoPhaseFlowPipe1.filo[9]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
528: dynamicTwoPhaseFlowPipe1.lambdal[9]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
529: dynamicTwoPhaseFlowPipe1.Rel2[9]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
530: dynamicTwoPhaseFlowPipe1.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]
531: dynamicTwoPhaseFlowPipe1.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]
532: dynamicTwoPhaseFlowPipe1.kl2[9]:VARIABLE(start = 0.5995743350536991 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
533: dynamicTwoPhaseFlowPipe1.cpl2[9]:VARIABLE(start = 4178.6358456341095 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
534: dynamicTwoPhaseFlowPipe1.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]
535: $cse66.d:VARIABLE(protected = true )  type: Real unreplaceable
536: $cse66.duhp:VARIABLE(protected = true )  type: Real unreplaceable
537: $cse66.duph:VARIABLE(protected = true )  type: Real unreplaceable
538: $cse66.ddph:VARIABLE(protected = true )  type: Real unreplaceable
539: $cse66.cp:VARIABLE(protected = true )  type: Real unreplaceable
540: $cse66.u:VARIABLE(protected = true )  type: Real unreplaceable
541: $cse66.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
542: $cse66.s:VARIABLE(protected = true )  type: Real unreplaceable
543: $cse66.T:VARIABLE(protected = true )  type: Real unreplaceable
544: $cse66.x:VARIABLE(protected = true )  type: Real unreplaceable
545: dynamicTwoPhaseFlowPipe1.hb[9]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
546: dynamicTwoPhaseFlowPipe1.h[9]:VARIABLE(start = 176001.7618457063 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
547: dynamicTwoPhaseFlowPipe1.P[9]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
548: dynamicTwoPhaseFlowPipe1.lambdal[8]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
549: dynamicTwoPhaseFlowPipe1.Rel2[8]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
550: dynamicTwoPhaseFlowPipe1.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]
551: dynamicTwoPhaseFlowPipe1.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]
552: dynamicTwoPhaseFlowPipe1.pro1[7].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
553: dynamicTwoPhaseFlowPipe1.T1[7]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
554: $cse50.duhp:VARIABLE(protected = true )  type: Real unreplaceable
555: $cse50.cp:VARIABLE(protected = true )  type: Real unreplaceable
556: $cse50.d:VARIABLE(protected = true )  type: Real unreplaceable
557: $cse50.duph:VARIABLE(protected = true )  type: Real unreplaceable
558: $cse50.s:VARIABLE(protected = true )  type: Real unreplaceable
559: $cse50.x:VARIABLE(protected = true )  type: Real unreplaceable
560: $cse50.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
561: $cse50.ddph:VARIABLE(protected = true )  type: Real unreplaceable
562: $cse50.T:VARIABLE(protected = true )  type: Real unreplaceable
563: $cse50.u:VARIABLE(protected = true )  type: Real unreplaceable
564: dynamicTwoPhaseFlowPipe1.pro1[7].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
565: dynamicTwoPhaseFlowPipe1.pro1[7].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
566: dynamicTwoPhaseFlowPipe1.pro1[7].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
567: dynamicTwoPhaseFlowPipe1.pro1[7].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
568: dynamicTwoPhaseFlowPipe1.pro1[7].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
569: dynamicTwoPhaseFlowPipe1.pro1[7].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
570: dynamicTwoPhaseFlowPipe1.pro1[7].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
571: dynamicTwoPhaseFlowPipe1.rhoc[8]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
572: dynamicTwoPhaseFlowPipe1.dpa[8]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
573: dynamicTwoPhaseFlowPipe1.dpf[8]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
574: dynamicTwoPhaseFlowPipe1.khi[8]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
575: dynamicTwoPhaseFlowPipe1.filo[8]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
576: dynamicTwoPhaseFlowPipe1.lambdav[8]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
577: dynamicTwoPhaseFlowPipe1.Rev2[8]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
578: dynamicTwoPhaseFlowPipe1.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]
579: dynamicTwoPhaseFlowPipe1.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]
580: dynamicTwoPhaseFlowPipe1.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]
581: dynamicTwoPhaseFlowPipe1.pro2[8].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
582: dynamicTwoPhaseFlowPipe1.pro2[8].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
583: $cse65.cp:VARIABLE(protected = true )  type: Real unreplaceable
584: $cse65.duph:VARIABLE(protected = true )  type: Real unreplaceable
585: $cse65.x:VARIABLE(protected = true )  type: Real unreplaceable
586: $cse65.ddph:VARIABLE(protected = true )  type: Real unreplaceable
587: $cse65.duhp:VARIABLE(protected = true )  type: Real unreplaceable
588: $cse65.T:VARIABLE(protected = true )  type: Real unreplaceable
589: $cse65.d:VARIABLE(protected = true )  type: Real unreplaceable
590: $cse65.u:VARIABLE(protected = true )  type: Real unreplaceable
591: $cse65.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
592: $cse65.s:VARIABLE(protected = true )  type: Real unreplaceable
593: dynamicTwoPhaseFlowPipe1.hb[8]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
594: dynamicTwoPhaseFlowPipe1.J[8]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
595: dynamicTwoPhaseFlowPipe1.Je[8]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
596: dynamicTwoPhaseFlowPipe1.re[8]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
597: dynamicTwoPhaseFlowPipe1.diff_res_e[8]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
598: dynamicTwoPhaseFlowPipe1.gamma[8]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
599: dynamicTwoPhaseFlowPipe1.rs[6]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
600: dynamicTwoPhaseFlowPipe1.Je[6]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
601: dynamicTwoPhaseFlowPipe1.Js[6]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
602: dynamicTwoPhaseFlowPipe1.gamma_s[6]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
603: dynamicTwoPhaseFlowPipe1.gamma_e[7]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
604: dynamicTwoPhaseFlowPipe1.gamma[7]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
605: dynamicTwoPhaseFlowPipe1.diff_res_e[7]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
606: dynamicTwoPhaseFlowPipe1.re[7]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
607: dynamicTwoPhaseFlowPipe1.gamma_s[5]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
608: dynamicTwoPhaseFlowPipe1.gamma_e[6]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
609: dynamicTwoPhaseFlowPipe1.rs[5]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
610: dynamicTwoPhaseFlowPipe1.Je[5]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
611: dynamicTwoPhaseFlowPipe1.Js[5]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
612: dynamicTwoPhaseFlowPipe1.gamma_s[4]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [10]
613: dynamicTwoPhaseFlowPipe1.gamma_e[5]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
614: dynamicTwoPhaseFlowPipe1.rs[4]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [10]
615: dynamicTwoPhaseFlowPipe1.Je[3]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
616: dynamicTwoPhaseFlowPipe1.Js[3]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
617: dynamicTwoPhaseFlowPipe1.Js[4]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [10]
618: dynamicTwoPhaseFlowPipe1.h[5]:VARIABLE(start = 130611.17116650468 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
619: dynamicTwoPhaseFlowPipe1.re[5]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
620: dynamicTwoPhaseFlowPipe1.diff_res_e[5]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
621: dynamicTwoPhaseFlowPipe1.gamma[5]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
622: dynamicTwoPhaseFlowPipe1.h[6]:VARIABLE(start = 142060.60442474802 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
623: dynamicTwoPhaseFlowPipe1.re[6]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
624: dynamicTwoPhaseFlowPipe1.diff_res_e[6]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
625: dynamicTwoPhaseFlowPipe1.gamma[6]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
626: dynamicTwoPhaseFlowPipe1.h[7]:VARIABLE(start = 153439.44619534744 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
627: dynamicTwoPhaseFlowPipe1.h[8]:VARIABLE(start = 164751.8668430315 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
628: dynamicTwoPhaseFlowPipe1.P[8]:VARIABLE(min = 0.0 start = 99999.999999992 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
629: dynamicTwoPhaseFlowPipe1.lsat2[7].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
630: dynamicTwoPhaseFlowPipe1.lsat2[7].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
631: dynamicTwoPhaseFlowPipe1.vsat2[7].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
632: dynamicTwoPhaseFlowPipe1.vsat2[7].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
633: dynamicTwoPhaseFlowPipe1.lsat2[7].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
634: dynamicTwoPhaseFlowPipe1.vsat2[7].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
635: dynamicTwoPhaseFlowPipe1.lsat2[7].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
636: dynamicTwoPhaseFlowPipe1.vsat2[7].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
637: dynamicTwoPhaseFlowPipe1.lsat2[7].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
638: dynamicTwoPhaseFlowPipe1.lsat2[7].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
639: dynamicTwoPhaseFlowPipe1.lsat2[7].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
640: dynamicTwoPhaseFlowPipe1.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]
641: dynamicTwoPhaseFlowPipe1.kl2[7]:VARIABLE(start = 0.5995743350543319 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
642: dynamicTwoPhaseFlowPipe1.lambdal[7]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
643: dynamicTwoPhaseFlowPipe1.Rel2[7]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
644: dynamicTwoPhaseFlowPipe1.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]
645: dynamicTwoPhaseFlowPipe1.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]
646: dynamicTwoPhaseFlowPipe1.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]
647: dynamicTwoPhaseFlowPipe1.Rev2[7]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
648: dynamicTwoPhaseFlowPipe1.lambdav[7]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
649: dynamicTwoPhaseFlowPipe1.filo[7]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
650: dynamicTwoPhaseFlowPipe1.khi[7]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
651: dynamicTwoPhaseFlowPipe1.dpf[7]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
652: dynamicTwoPhaseFlowPipe1.dpa[7]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
653: dynamicTwoPhaseFlowPipe1.rhoc[7]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
654: dynamicTwoPhaseFlowPipe1.pro1[6].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
655: dynamicTwoPhaseFlowPipe1.pro1[6].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
656: $cse48.cp:VARIABLE(protected = true )  type: Real unreplaceable
657: $cse48.duhp:VARIABLE(protected = true )  type: Real unreplaceable
658: $cse48.u:VARIABLE(protected = true )  type: Real unreplaceable
659: $cse48.x:VARIABLE(protected = true )  type: Real unreplaceable
660: $cse48.s:VARIABLE(protected = true )  type: Real unreplaceable
661: $cse48.d:VARIABLE(protected = true )  type: Real unreplaceable
662: $cse48.ddph:VARIABLE(protected = true )  type: Real unreplaceable
663: $cse48.T:VARIABLE(protected = true )  type: Real unreplaceable
664: $cse48.duph:VARIABLE(protected = true )  type: Real unreplaceable
665: $cse48.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
666: dynamicTwoPhaseFlowPipe1.P[7]:VARIABLE(min = 0.0 start = 99999.99999999 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
667: $cse63.u:VARIABLE(protected = true )  type: Real unreplaceable
668: $cse63.cp:VARIABLE(protected = true )  type: Real unreplaceable
669: $cse63.duhp:VARIABLE(protected = true )  type: Real unreplaceable
670: $cse63.d:VARIABLE(protected = true )  type: Real unreplaceable
671: $cse63.T:VARIABLE(protected = true )  type: Real unreplaceable
672: $cse63.duph:VARIABLE(protected = true )  type: Real unreplaceable
673: $cse63.x:VARIABLE(protected = true )  type: Real unreplaceable
674: dynamicTwoPhaseFlowPipe1.pro2[6].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
675: dynamicTwoPhaseFlowPipe1.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]
676: dynamicTwoPhaseFlowPipe1.pro2[6].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
677: dynamicTwoPhaseFlowPipe1.pro2[6].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
678: dynamicTwoPhaseFlowPipe1.pro2[6].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
679: dynamicTwoPhaseFlowPipe1.lambdav[6]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
680: dynamicTwoPhaseFlowPipe1.Rev2[6]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
681: dynamicTwoPhaseFlowPipe1.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]
682: dynamicTwoPhaseFlowPipe1.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]
683: dynamicTwoPhaseFlowPipe1.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]
684: dynamicTwoPhaseFlowPipe1.kl2[6]:VARIABLE(start = 0.5995743350548642 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
685: dynamicTwoPhaseFlowPipe1.lambdal[6]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
686: dynamicTwoPhaseFlowPipe1.Rel2[6]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
687: dynamicTwoPhaseFlowPipe1.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]
688: dynamicTwoPhaseFlowPipe1.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]
689: dynamicTwoPhaseFlowPipe1.cpl2[6]:VARIABLE(start = 4178.913555072556 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
690: dynamicTwoPhaseFlowPipe1.xv2[6]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
691: dynamicTwoPhaseFlowPipe1.filo[6]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
692: dynamicTwoPhaseFlowPipe1.khi[6]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
693: dynamicTwoPhaseFlowPipe1.dpf[6]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
694: dynamicTwoPhaseFlowPipe1.dpa[6]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
695: dynamicTwoPhaseFlowPipe1.rhoc[6]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
696: dynamicTwoPhaseFlowPipe1.pro1[5].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
697: dynamicTwoPhaseFlowPipe1.pro1[5].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
698: dynamicTwoPhaseFlowPipe1.pro1[5].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
699: dynamicTwoPhaseFlowPipe1.pro1[5].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
700: dynamicTwoPhaseFlowPipe1.pro1[5].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
701: dynamicTwoPhaseFlowPipe1.T1[5]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
702: dynamicTwoPhaseFlowPipe1.pro1[5].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
703: $cse46.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
704: $cse46.s:VARIABLE(protected = true )  type: Real unreplaceable
705: $cse46.u:VARIABLE(protected = true )  type: Real unreplaceable
706: $cse46.d:VARIABLE(protected = true )  type: Real unreplaceable
707: $cse46.ddph:VARIABLE(protected = true )  type: Real unreplaceable
708: $cse46.cp:VARIABLE(protected = true )  type: Real unreplaceable
709: $cse46.duhp:VARIABLE(protected = true )  type: Real unreplaceable
710: $cse46.T:VARIABLE(protected = true )  type: Real unreplaceable
711: $cse46.duph:VARIABLE(protected = true )  type: Real unreplaceable
712: $cse46.x:VARIABLE(protected = true )  type: Real unreplaceable
713: dynamicTwoPhaseFlowPipe1.P[6]:VARIABLE(min = 0.0 start = 99999.999999988 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
714: dynamicTwoPhaseFlowPipe1.lsat2[5].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
715: dynamicTwoPhaseFlowPipe1.lsat2[5].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
716: dynamicTwoPhaseFlowPipe1.lsat2[5].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
717: dynamicTwoPhaseFlowPipe1.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]
718: dynamicTwoPhaseFlowPipe1.kl2[5]:VARIABLE(start = 0.5995743350555206 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
719: dynamicTwoPhaseFlowPipe1.cpl2[5]:VARIABLE(start = 4179.389099400846 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
720: dynamicTwoPhaseFlowPipe1.lambdav[5]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
721: dynamicTwoPhaseFlowPipe1.Rev2[5]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
722: dynamicTwoPhaseFlowPipe1.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]
723: dynamicTwoPhaseFlowPipe1.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]
724: dynamicTwoPhaseFlowPipe1.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]
725: dynamicTwoPhaseFlowPipe1.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]
726: dynamicTwoPhaseFlowPipe1.Rel2[5]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
727: dynamicTwoPhaseFlowPipe1.lambdal[5]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
728: dynamicTwoPhaseFlowPipe1.filo[5]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
729: dynamicTwoPhaseFlowPipe1.khi[5]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
730: dynamicTwoPhaseFlowPipe1.dpf[5]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
731: dynamicTwoPhaseFlowPipe1.dpa[5]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
732: dynamicTwoPhaseFlowPipe1.rhoc[5]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
733: dynamicTwoPhaseFlowPipe1.pro1[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
734: dynamicTwoPhaseFlowPipe1.pro1[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
735: $cse44.cp:VARIABLE(protected = true )  type: Real unreplaceable
736: $cse44.u:VARIABLE(protected = true )  type: Real unreplaceable
737: $cse44.duhp:VARIABLE(protected = true )  type: Real unreplaceable
738: $cse44.x:VARIABLE(protected = true )  type: Real unreplaceable
739: $cse44.duph:VARIABLE(protected = true )  type: Real unreplaceable
740: $cse44.ddph:VARIABLE(protected = true )  type: Real unreplaceable
741: $cse44.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
742: $cse44.d:VARIABLE(protected = true )  type: Real unreplaceable
743: $cse44.s:VARIABLE(protected = true )  type: Real unreplaceable
744: $cse44.T:VARIABLE(protected = true )  type: Real unreplaceable
745: dynamicTwoPhaseFlowPipe1.P[5]:VARIABLE(min = 0.0 start = 99999.999999985 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
746: dynamicTwoPhaseFlowPipe1.lambdav[4]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
747: dynamicTwoPhaseFlowPipe1.Rev2[4]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
748: dynamicTwoPhaseFlowPipe1.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]
749: dynamicTwoPhaseFlowPipe1.pro1[3].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
750: dynamicTwoPhaseFlowPipe1.pro1[3].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
751: dynamicTwoPhaseFlowPipe1.pro1[3].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
752: dynamicTwoPhaseFlowPipe1.pro1[3].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
753: dynamicTwoPhaseFlowPipe1.pro1[3].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
754: dynamicTwoPhaseFlowPipe1.pro1[3].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
755: $cse42.ddph:VARIABLE(protected = true )  type: Real unreplaceable
756: $cse42.x:VARIABLE(protected = true )  type: Real unreplaceable
757: dynamicTwoPhaseFlowPipe1.T1[3]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
758: dynamicTwoPhaseFlowPipe1.pro1[3].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
759: dynamicTwoPhaseFlowPipe1.pro1[3].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
760: dynamicTwoPhaseFlowPipe1.rhoc[4]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
761: dynamicTwoPhaseFlowPipe1.dpa[4]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
762: dynamicTwoPhaseFlowPipe1.dpf[4]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
763: dynamicTwoPhaseFlowPipe1.khi[4]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
764: dynamicTwoPhaseFlowPipe1.filo[4]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
765: dynamicTwoPhaseFlowPipe1.lambdal[4]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
766: dynamicTwoPhaseFlowPipe1.Rel2[4]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
767: dynamicTwoPhaseFlowPipe1.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]
768: dynamicTwoPhaseFlowPipe1.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]
769: dynamicTwoPhaseFlowPipe1.pro2[4].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
770: dynamicTwoPhaseFlowPipe1.pro2[4].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
771: $cse61.s:VARIABLE(protected = true )  type: Real unreplaceable
772: $cse61.d:VARIABLE(protected = true )  type: Real unreplaceable
773: $cse61.x:VARIABLE(protected = true )  type: Real unreplaceable
774: $cse61.T:VARIABLE(protected = true )  type: Real unreplaceable
775: $cse61.duph:VARIABLE(protected = true )  type: Real unreplaceable
776: $cse61.duhp:VARIABLE(protected = true )  type: Real unreplaceable
777: $cse61.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
778: $cse61.ddph:VARIABLE(protected = true )  type: Real unreplaceable
779: $cse61.cp:VARIABLE(protected = true )  type: Real unreplaceable
780: $cse61.u:VARIABLE(protected = true )  type: Real unreplaceable
781: dynamicTwoPhaseFlowPipe1.hb[4]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
782: dynamicTwoPhaseFlowPipe1.J[4]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [10]
783: dynamicTwoPhaseFlowPipe1.Je[4]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
784: dynamicTwoPhaseFlowPipe1.re[4]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
785: dynamicTwoPhaseFlowPipe1.diff_res_e[4]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
786: dynamicTwoPhaseFlowPipe1.gamma[4]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
787: dynamicTwoPhaseFlowPipe1.h[4]:VARIABLE(start = 119086.65906940492 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
788: $cse42.duhp:VARIABLE(protected = true )  type: Real unreplaceable
789: $cse42.d:VARIABLE(protected = true )  type: Real unreplaceable
790: $cse42.u:VARIABLE(protected = true )  type: Real unreplaceable
791: $cse42.duph:VARIABLE(protected = true )  type: Real unreplaceable
792: $cse42.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
793: $cse42.s:VARIABLE(protected = true )  type: Real unreplaceable
794: $cse42.T:VARIABLE(protected = true )  type: Real unreplaceable
795: $cse42.cp:VARIABLE(protected = true )  type: Real unreplaceable
796: dynamicTwoPhaseFlowPipe1.P[4]:VARIABLE(min = 0.0 start = 99999.999999983 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
797: $cse60.duph:VARIABLE(protected = true )  type: Real unreplaceable
798: $cse60.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
799: dynamicTwoPhaseFlowPipe1.dpg[2]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [11]
800: $cse59.duph:VARIABLE(protected = true )  type: Real unreplaceable
801: dynamicTwoPhaseFlowPipe1.pro2[2].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [11]
802: dynamicTwoPhaseFlowPipe1.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]
803: dynamicTwoPhaseFlowPipe1.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]
804: dynamicTwoPhaseFlowPipe1.pro2[2].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [11]
805: dynamicTwoPhaseFlowPipe1.pro2[2].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [11]
806: dynamicTwoPhaseFlowPipe1.pro2[2].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [11]
807: dynamicTwoPhaseFlowPipe1.pro2[2].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [11]
808: dynamicTwoPhaseFlowPipe1.pro2[2].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [11]
809: dynamicTwoPhaseFlowPipe1.cpl2[2]:VARIABLE(start = 4182.2694439224715 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
810: dynamicTwoPhaseFlowPipe1.xv2[2]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
811: dynamicTwoPhaseFlowPipe1.pro2[2].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
812: dynamicTwoPhaseFlowPipe1.lambdav[2]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
813: dynamicTwoPhaseFlowPipe1.Rev2[2]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
814: dynamicTwoPhaseFlowPipe1.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]
815: dynamicTwoPhaseFlowPipe1.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]
816: dynamicTwoPhaseFlowPipe1.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]
817: dynamicTwoPhaseFlowPipe1.kl2[2]:VARIABLE(start = 0.5995743350579683 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
818: dynamicTwoPhaseFlowPipe1.dpa[2]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
819: dynamicTwoPhaseFlowPipe1.dpf[2]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
820: dynamicTwoPhaseFlowPipe1.khi[2]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
821: dynamicTwoPhaseFlowPipe1.filo[2]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
822: dynamicTwoPhaseFlowPipe1.lambdal[2]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
823: dynamicTwoPhaseFlowPipe1.Rel2[2]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
824: dynamicTwoPhaseFlowPipe1.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]
825: dynamicTwoPhaseFlowPipe1.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]
826: dynamicTwoPhaseFlowPipe1.vsat2[2].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
827: dynamicTwoPhaseFlowPipe1.lsat2[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
828: dynamicTwoPhaseFlowPipe1.vsat2[2].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
829: dynamicTwoPhaseFlowPipe1.vsat2[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [11]
830: dynamicTwoPhaseFlowPipe1.lsat2[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
831: dynamicTwoPhaseFlowPipe1.vsat2[2].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
832: dynamicTwoPhaseFlowPipe1.lsat2[2].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
833: dynamicTwoPhaseFlowPipe1.vsat2[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [11]
834: dynamicTwoPhaseFlowPipe1.lsat2[2].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [11]
835: dynamicTwoPhaseFlowPipe1.vsat2[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
836: dynamicTwoPhaseFlowPipe1.lsat2[2].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [11]
837: dynamicTwoPhaseFlowPipe1.lsat2[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [11]
838: dynamicTwoPhaseFlowPipe1.vsat2[2].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [11]
839: dynamicTwoPhaseFlowPipe1.lsat2[2].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [11]
840: dynamicTwoPhaseFlowPipe1.Pb[3]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [12]
841: $cse41:VARIABLE(protected = true )  type: Real unreplaceable
842: dynamicTwoPhaseFlowPipe1.pro1[2].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [10]
843: dynamicTwoPhaseFlowPipe1.T1[2]:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [10]
844: dynamicTwoPhaseFlowPipe1.pro1[2].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [10]
845: $cse40.T:VARIABLE(protected = true )  type: Real unreplaceable
846: dynamicTwoPhaseFlowPipe1.pro1[2].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [10]
847: dynamicTwoPhaseFlowPipe1.pro1[2].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [10]
848: dynamicTwoPhaseFlowPipe1.pro1[2].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [10]
849: dynamicTwoPhaseFlowPipe1.pro1[2].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [10]
850: dynamicTwoPhaseFlowPipe1.pro1[2].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [10]
851: dynamicTwoPhaseFlowPipe1.pro1[2].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
852: $cse40.cp:VARIABLE(protected = true )  type: Real unreplaceable
853: dynamicTwoPhaseFlowPipe1.P[3]:VARIABLE(min = 0.0 start = 99999.999999981 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
854: $cse40.x:VARIABLE(protected = true )  type: Real unreplaceable
855: $cse40.ddph:VARIABLE(protected = true )  type: Real unreplaceable
856: $cse40.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
857: $cse40.u:VARIABLE(protected = true )  type: Real unreplaceable
858: $cse40.s:VARIABLE(protected = true )  type: Real unreplaceable
859: $cse40.d:VARIABLE(protected = true )  type: Real unreplaceable
860: $cse40.duhp:VARIABLE(protected = true )  type: Real unreplaceable
861: $cse40.duph:VARIABLE(protected = true )  type: Real unreplaceable
862: dynamicTwoPhaseFlowPipe1.h[3]:VARIABLE(start = 107482.21110144592 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
863: dynamicTwoPhaseFlowPipe1.re[3]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
864: dynamicTwoPhaseFlowPipe1.diff_res_e[3]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
865: dynamicTwoPhaseFlowPipe1.gamma[3]:VARIABLE(unit = "kg/s" )  "Total diffusion conductance in hydraulic node i" type: Real [11]
866: dynamicTwoPhaseFlowPipe1.hb[3]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
867: $cse60.d:VARIABLE(protected = true )  type: Real unreplaceable
868: dynamicTwoPhaseFlowPipe1.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]
869: dynamicTwoPhaseFlowPipe1.xv2[3]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [11]
870: dynamicTwoPhaseFlowPipe1.pro2[3].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [11]
871: dynamicTwoPhaseFlowPipe1.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]
872: dynamicTwoPhaseFlowPipe1.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]
873: dynamicTwoPhaseFlowPipe1.kl2[3]:VARIABLE(start = 0.5995743350571023 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [11]
874: dynamicTwoPhaseFlowPipe1.cpl2[3]:VARIABLE(start = 4181.033777873867 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [11]
875: dynamicTwoPhaseFlowPipe1.lambdav[3]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [11]
876: dynamicTwoPhaseFlowPipe1.Rev2[3]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [11]
877: dynamicTwoPhaseFlowPipe1.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]
878: dynamicTwoPhaseFlowPipe1.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]
879: dynamicTwoPhaseFlowPipe1.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]
880: dynamicTwoPhaseFlowPipe1.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]
881: dynamicTwoPhaseFlowPipe1.Rel2[3]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [11]
882: dynamicTwoPhaseFlowPipe1.filo[3]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [11]
883: dynamicTwoPhaseFlowPipe1.lambdal[3]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [11]
884: dynamicTwoPhaseFlowPipe1.khi[3]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [11]
885: dynamicTwoPhaseFlowPipe1.dpf[3]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [11]
886: dynamicTwoPhaseFlowPipe1.dpa[3]:VARIABLE(unit = "Pa" )  "Advection term for the mass balance equation in node i" type: Real [11]
887: dynamicTwoPhaseFlowPipe1.rhoc[3]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
888: dynamicTwoPhaseFlowPipe1.rhoc[2]:VARIABLE(min = 1e-9 max = 1e5 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density at the boudary of node i" type: Real [12]
889: dynamicTwoPhaseFlowPipe1.pro1[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [10]
890: $cse38.x:VARIABLE(protected = true )  type: Real unreplaceable
891: $cse38.T:VARIABLE(protected = true )  type: Real unreplaceable
892: $cse38.duph:VARIABLE(protected = true )  type: Real unreplaceable
893: $cse38.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
894: $cse38.u:VARIABLE(protected = true )  type: Real unreplaceable
895: $cse38.ddph:VARIABLE(protected = true )  type: Real unreplaceable
896: $cse38.cp:VARIABLE(protected = true )  type: Real unreplaceable
897: $cse38.s:VARIABLE(protected = true )  type: Real unreplaceable
898: $cse38.d:VARIABLE(protected = true )  type: Real unreplaceable
899: $cse38.duhp:VARIABLE(protected = true )  type: Real unreplaceable
900: dynamicTwoPhaseFlowPipe1.P[2]:VARIABLE(min = 0.0 start = 99999.999999978 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [12]
901: $cse59.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
902: $cse59.cp:VARIABLE(protected = true )  type: Real unreplaceable
903: $cse59.u:VARIABLE(protected = true )  type: Real unreplaceable
904: $cse59.ddph:VARIABLE(protected = true )  type: Real unreplaceable
905: $cse59.x:VARIABLE(protected = true )  type: Real unreplaceable
906: $cse59.s:VARIABLE(protected = true )  type: Real unreplaceable
907: $cse59.d:VARIABLE(protected = true )  type: Real unreplaceable
908: $cse59.duhp:VARIABLE(protected = true )  type: Real unreplaceable
909: $cse59.T:VARIABLE(protected = true )  type: Real unreplaceable
910: dynamicTwoPhaseFlowPipe1.hb[2]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [11]
911: dynamicTwoPhaseFlowPipe1.h[2]:VARIABLE(start = 95792.53373784182 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [12]
912: dynamicTwoPhaseFlowPipe1.diff_res_t:VARIABLE(start = 1e4 )  "Total diffusion resistance in the pipe" type: Real
913: dynamicTwoPhaseFlowPipe1.re[1]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [10]
914: dynamicTwoPhaseFlowPipe1.diff_res_e[1]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [10]
915: dynamicTwoPhaseFlowPipe1.gamma_e[1]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [10]
916: dynamicTwoPhaseFlowPipe1.Je[1]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [10]
917: dynamicTwoPhaseFlowPipe1.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 <failed> postOpt createDAEmodeBDAE (simulation): time 0.2807/4.906, allocations: 342.1 MB / 1.906 GB, free: 387.9 MB / 0.8263 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestDiffusion_DynamicTwoPhaseFlowPipe could not be translated