Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicWaterSteamMultiFluidHeatExchanger.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.TestDynamicWaterSteamMultiFluidHeatExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicWaterSteamMultiFluidHeatExchanger")
translateModel(ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicWaterSteamMultiFluidHeatExchanger,tolerance=1e-06,outputFormat="empty",numberOfIntervals=5000,variableFilter="",fileNamePrefix="ThermoSysPro_ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicWaterSteamMultiFluidHeatExchanger")
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/package.mo): time 0.8216/0.8216, allocations: 150.9 MB / 167.2 MB, free: 14.53 MB / 142.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.0003404/0.0003404, allocations: 17.56 kB / 237.8 MB, free: 1.77 MB / 190.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.05402/0.05438, allocations: 31.34 MB / 269.1 MB, free: 7.059 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.TestDynamicWaterSteamMultiFluidHeatExchanger): time 1.642/1.696, allocations: 299.3 MB / 0.5551 GB, free: 8.395 MB / 446.1 MB
Notification: Performance of NFInst.instExpressions: time 0.5005/2.197, allocations: 201.1 MB / 0.7515 GB, free: 1.754 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001189/2.198, allocations: 34.41 kB / 0.7515 GB, free: 1.754 MB / 0.5919 GB
[/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).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/HeatExchangers/DynamicOnePhaseFlowPipe.mo:150:3-151:67: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/DynamicOnePhaseFlowPipe.mo:152:3-153:65: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/HeatExchangers/DynamicWaterSteamMultiFluidsHeatExchanger.mo:93:3-94:51:writable] Warning: Connector Cfg1 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/DynamicWaterSteamMultiFluidsHeatExchanger.mo:95:3-96:53:writable] Warning: Connector Cfg2 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/DynamicWaterSteamMultiFluidsHeatExchanger.mo:97:3-98:54:writable] Warning: Connector Cws1 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/DynamicWaterSteamMultiFluidsHeatExchanger.mo:99:3-100:52:writable] Warning: Connector Cws2 is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SourceP.mo:58:3-59:65:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermoSysPro 4.0.0-master/Fluid/BoundaryConditions/SinkP.mo:46:3-47:67:writable] Warning: Connector C is not balanced: The number of potential variables (9) is not equal to the number of flow variables (0).
Notification: Performance of NFTyping.typeComponents: time 0.001167/2.199, allocations: 403.2 kB / 0.7519 GB, free: 1.754 MB / 0.5919 GB
Notification: Performance of NFTyping.typeBindings: time 0.002149/2.201, allocations: 1.025 MB / 0.7529 GB, free: 1.695 MB / 0.5919 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 0.03756/2.239, allocations: 15.04 MB / 0.7676 GB, free: 1.359 MB / 0.5919 GB
Notification: Performance of NFFlatten.flatten: time 0.007123/2.246, allocations: 8.515 MB / 0.7759 GB, free: 1.328 MB / 0.5919 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.00393/2.25, allocations: 2.732 MB / 0.7786 GB, free: 1.168 MB / 0.5919 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.004353/2.255, allocations: 2.682 MB / 0.7812 GB, free: 1.152 MB / 0.5919 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.004419/2.259, allocations: 3.089 MB / 0.7842 GB, free: 256 kB / 0.5919 GB
Notification: Performance of NFPackage.collectConstants: time 0.001273/2.26, allocations: 0.6516 MB / 0.7848 GB, free: 256 kB / 0.5919 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.04712/2.307, allocations: 24.58 MB / 0.8089 GB, free: 1.367 MB / 0.6075 GB
Notification: Performance of NFScalarize.scalarize: time 0.002547/2.31, allocations: 1.948 MB / 0.8108 GB, free: 15.45 MB / 0.6231 GB
Notification: Performance of NFVerifyModel.verify: time 0.003533/2.314, allocations: 2.519 MB / 0.8132 GB, free: 12.96 MB / 0.6231 GB
Notification: Performance of NFConvertDAE.convert: time 0.0397/2.353, allocations: 18.56 MB / 0.8313 GB, free: 11.73 MB / 0.6387 GB
Notification: Performance of FrontEnd - DAE generated: time 5.861e-06/2.353, allocations: 0 / 0.8313 GB, free: 11.73 MB / 0.6387 GB
Notification: Performance of FrontEnd: time 2.154e-06/2.353, allocations: 0 / 0.8313 GB, free: 11.73 MB / 0.6387 GB
Notification: Performance of Transformations before backend: time 0.0002043/2.353, allocations: 1 kB / 0.8313 GB, free: 11.73 MB / 0.6387 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 1023
 * Number of variables: 1023
Notification: Performance of Generate backend data structure: time 0.02431/2.378, allocations: 6.782 MB / 0.838 GB, free: 4.953 MB / 0.6387 GB
Notification: Performance of prepare preOptimizeDAE: time 5.075e-05/2.378, allocations: 8.031 kB / 0.838 GB, free: 4.945 MB / 0.6387 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0009841/2.379, allocations: 411.3 kB / 0.8384 GB, free: 4.539 MB / 0.6387 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.004036/2.383, allocations: 1.997 MB / 0.8403 GB, free: 2.605 MB / 0.6387 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001289/2.384, allocations: 1.184 MB / 0.8415 GB, free: 1.254 MB / 0.6387 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0006343/2.385, allocations: 304 kB / 0.8418 GB, free: 0.957 MB / 0.6387 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.01499/2.4, allocations: 7.179 MB / 0.8488 GB, free: 9.711 MB / 0.6544 GB
Notification: Performance of preOpt findStateOrder (simulation): time 5.768e-05/2.4, allocations: 2.625 kB / 0.8488 GB, free: 9.711 MB / 0.6544 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0004581/2.4, allocations: 132 kB / 0.8489 GB, free: 9.582 MB / 0.6544 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 8.294e-05/2.401, allocations: 115.9 kB / 0.849 GB, free: 9.469 MB / 0.6544 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.02269/2.423, allocations: 10.93 MB / 0.8597 GB, free: 14.54 MB / 0.67 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 0.2109/2.634, allocations: 119.4 MB / 0.9763 GB, free: 10.46 MB / 0.795 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.02168/2.656, allocations: 8.049 MB / 0.9842 GB, free: 2.352 MB / 0.795 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.01085/2.667, allocations: 4.923 MB / 0.989 GB, free: 13.41 MB / 0.8106 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.8664/3.533, allocations: 416.8 MB / 1.396 GB, free: 37.4 MB / 0.8262 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 8.482e-05/3.533, allocations: 78 kB / 1.396 GB, free: 37.31 MB / 0.8262 GB
Notification: Performance of pre-optimization done (n=654): time 1.032e-05/3.533, allocations: 0 / 1.396 GB, free: 37.31 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=654): time 0.04033/3.574, allocations: 18.03 MB / 1.414 GB, free: 19.36 MB / 0.8262 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.792e-05/3.574, allocations: 98.84 kB / 1.414 GB, free: 19.25 MB / 0.8262 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001123/3.575, allocations: 1.015 MB / 1.415 GB, free: 18.24 MB / 0.8262 GB
Notification: Performance of collectPreVariables (initialization): time 0.0007196/3.576, allocations: 93.7 kB / 1.415 GB, free: 18.14 MB / 0.8262 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0003265/3.576, allocations: 0.7914 MB / 1.416 GB, free: 17.38 MB / 0.8262 GB
Notification: Performance of collectInitialBindings (initialization): time 0.001375/3.577, allocations: 2.162 MB / 1.418 GB, free: 15.24 MB / 0.8262 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.001505/3.579, allocations: 0.9309 MB / 1.419 GB, free: 14.3 MB / 0.8262 GB
Notification: Performance of setup shared object (initialization): time 3.658e-05/3.579, allocations: 301.1 kB / 1.419 GB, free: 14 MB / 0.8262 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.008403/3.587, allocations: 4.183 MB / 1.423 GB, free: 9.816 MB / 0.8262 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.008998/3.596, allocations: 4.836 MB / 1.428 GB, free: 4.801 MB / 0.8262 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.2286/3.825, allocations: 9.168 MB / 1.437 GB, free: 428.3 MB / 0.8262 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.003e-05/3.825, allocations: 6.469 kB / 1.437 GB, free: 428.3 MB / 0.8262 GB
Notification: Performance of matching and sorting (n=718) (initialization): time 0.03189/3.857, allocations: 14.46 MB / 1.451 GB, free: 428 MB / 0.8262 GB
Notification: Performance of prepare postOptimizeDAE: time 4.813e-05/3.857, allocations: 13.72 kB / 1.451 GB, free: 428 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 5.51e-05/3.857, allocations: 22.31 kB / 1.451 GB, free: 428 MB / 0.8262 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.07444/3.931, allocations: 21.33 MB / 1.472 GB, free: 426.2 MB / 0.8262 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0008164/3.932, allocations: 223.5 kB / 1.472 GB, free: 426.2 MB / 0.8262 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.03044/3.963, allocations: 17.04 MB / 1.489 GB, free: 413.8 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.004786/3.968, allocations: 0.8238 MB / 1.489 GB, free: 413 MB / 0.8262 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0006243/3.968, allocations: 211.8 kB / 1.49 GB, free: 412.8 MB / 0.8262 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 57
 * Number of states: 0 ()
 * Number of discrete variables: 12 (sourceP1.C.ftype,sourceP.C.ftype,sinkP.fluid,dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid,dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid,sinkP1.fluid,sourceP1.fluid1,sourceP.fluid1,dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.C1.diff_on_2,dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.C2.diff_on_1,dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.C1.diff_on_2,dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.C2.diff_on_1)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (109):
 * Single equations (assignments): 106
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 2
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 1
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 0 systems
 * Non-linear torn systems (#iteration vars, #inner vars): 1 system
   {(22,372)}
Notification: Performance of prepare postOptimizeDAE: time 0.001911/3.97, allocations: 1.011 MB / 1.491 GB, free: 411.8 MB / 0.8262 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0007457/3.971, allocations: 285 kB / 1.491 GB, free: 411.5 MB / 0.8262 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.03008/4.001, allocations: 16.45 MB / 1.507 GB, free: 395.2 MB / 0.8262 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 8.013e-05/4.001, allocations: 23.86 kB / 1.507 GB, free: 395.1 MB / 0.8262 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 3.351e-05/4.001, allocations: 8 kB / 1.507 GB, free: 395.1 MB / 0.8262 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.003093/4.004, allocations: 1.319 MB / 1.508 GB, free: 393.8 MB / 0.8262 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0006954/4.005, allocations: 81.53 kB / 1.508 GB, free: 393.7 MB / 0.8262 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.004069/4.009, allocations: 0.5041 MB / 1.509 GB, free: 393.2 MB / 0.8262 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0005968/4.01, allocations: 275.7 kB / 1.509 GB, free: 393 MB / 0.8262 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(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x) = $cse4

Variables:
1: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [4]
2: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [4]
3: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [6]
4: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [4]
5: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [4]
6: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [4]
7: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [4]
8: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [4]
9: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[1]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
10: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[1]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
[/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): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[1] = if sourceP.Q0 > 0.0 then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[1] else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2]
2/2 (10): $cse4 = ThermoSysPro.Properties.Fluid.Ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
3/12 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
4/13 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[1] = abs(4.0 * sourceP.Q0 * (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[1]) / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1]))
5/14 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[1] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[1] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[1] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[1] ^ 0.4 else 0.0
6/15 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1] else (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[1]) else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[1] + (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1]) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[1])) / (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[1]
7/16 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[1] > 1e-6) then 1.0 / (1.0 + 1.15e-6 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[1] ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[1] ^ 1.17) else 0.0
8/17 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[1] > 0.0) then 1.0 + 24000.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[1] ^ 1.16 + 1.37 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[1] ^ 0.86 else 1.0
9/18 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[1] = if noEvent(abs(sourceP.Q0) > 0.001) then abs((-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D / (4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1)) else 1e-5
10/19 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1] > 1.0) then 55.0 * (abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) ^ 0.12 / ((-log10(abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit)) ^ 0.55 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Mmol ^ 0.5) * (abs(dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi) ^ 0.67 else 100.0
11/20 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[1]
12/21 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[1] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1])
13/22 (1): 0.0 = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[1] * sourceP.Q0 + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[1] + (-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[2] * sourceP.Q0
14/23 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[1]
15/24 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[1] = if sourceP.diffusion then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[1] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[1] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2]) else 0.0
16/25 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[1] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[1]
17/26 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[1] = exp((-0.033) * (sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[1]) ^ 2.0)
18/27 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[1])
19/28 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1], 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
20/29 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
21/30 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
22/31 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[1] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[1]))
23/32 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[1] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
24/33 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] < 0.0) then 1.0 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] >= 0.0) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] < 0.8) then 1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1]) else (5.0 + (-5.0) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1])) + (-4.0 + 5.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[1] / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[1])
25/34 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[1] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
26/35 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[1] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[1]))
27/36 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D
28/37 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].cp
29/38 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].rho)
30/39 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].rho)
31/40 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1] = if noEvent(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2]) > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].x
32/41 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[1] = ThermoSysPro.Properties.Fluid.SpecificEnthalpy_PT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1], 290.0, 1, sourceP.mode, 0.01, 0.05, 0.22, 0.0)
33/42 (1): $cse3 = min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit - 1.0)
34/43 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1] = max($cse3, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ptriple)
35/44 (10): $cse12 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
36/54 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].x) = $cse12
37/64 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
38/78 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1] + (-dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[1]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[1] = 0.0
39/79 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[1] = 0.5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpfCorr * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[1] * sourceP.Q0 * abs(sourceP.Q0) / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[1])
40/80 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[1] = 9.80665 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[1] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z2 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.L
41/81 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[1] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[1]) / $cse2
42/82 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[1] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[1]) / $cse1
43/83 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[1] = 6.283185307179586 * ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[1] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[1]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ntubes) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[1] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1])
44/84 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[1] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[1]
45/85 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dSi * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[1] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[1])
46/86 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[1] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.ntubes) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[1] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[1] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[1])
47/87 (1): 0.0 = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1] * sourceP1.Q + dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[1] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2] * sourceP1.Q
48/88 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[1] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[1]
49/89 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[1] = if sourceP1.diffusion then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[1] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[1] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2]) else 0.0
50/90 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[1] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[1]
51/91 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[1] = exp((-0.033) * (sourceP1.Q * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[1]) ^ 2.0)
52/92 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[1])
53/93 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[1] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(0.5 * (sourceP1.P0 + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
54/94 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[1] = ThermoSysPro.Properties.Fluid.Temperature_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
55/95 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[1] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
56/96 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[1] / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[1]
57/97 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[1] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[1] > 2000.0) then 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[1] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[1] ^ 0.4 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[1] * max(4.36, 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[1] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[1] ^ 0.4) / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
58/98 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
59/99 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[1] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[1]))
60/100 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
61/101 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[1] = ThermoSysPro.Properties.Fluid.Density_Ph(0.5 * (sourceP1.P0 + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
62/102 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[1] = 0.5 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpfCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[1] * sourceP1.Q * abs(sourceP1.Q) / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A ^ 2.0 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[1])
63/103 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
64/104 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[1] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[1] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[1] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D)) ^ 2.0 else 0.01
65/105 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[1] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[1]))
66/106 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[2] = exp((-0.033) * (sourceP1.Q * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[2]) ^ 2.0)
67/107 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[2] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3])
68/108 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[2]
69/109 (1): 0.0 = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2] * sourceP1.Q + dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[2] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3] * sourceP1.Q
70/110 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[2] = ThermoSysPro.Properties.Fluid.Density_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
71/111 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[2] = 0.5 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpfCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[2] * sourceP1.Q * abs(sourceP1.Q) / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A ^ 2.0 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[2])
72/112 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
73/113 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[2] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[2] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D)) ^ 2.0 else 0.01
74/114 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[2] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[2]))
75/115 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
76/116 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[2] = ThermoSysPro.Properties.Fluid.Temperature_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
77/117 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[2] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.ntubes) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[2] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[2] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[2])
78/118 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[2] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[2]) / $cse2
79/119 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[2] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[2]) / $cse1
80/120 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[2] = 6.283185307179586 * ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[2]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ntubes) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[2] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2])
81/121 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[2]
82/122 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2] > 1.0) then 55.0 * (abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) ^ 0.12 / ((-log10(abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit)) ^ 0.55 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Mmol ^ 0.5) * (abs(dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi) ^ 0.67 else 100.0
83/123 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2] else (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[2]) else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[2] + (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2]) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[2])) / (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[2]
84/124 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[2] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2])
85/125 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[2] = if noEvent(abs(sourceP.Q0) > 0.001) then abs((-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D / (4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1)) else 1e-5
86/126 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[2] > 0.0) then 1.0 + 24000.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[2] ^ 1.16 + 1.37 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[2] ^ 0.86 else 1.0
87/127 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[2] > 1e-6) then 1.0 / (1.0 + 1.15e-6 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[2] ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[2] ^ 1.17) else 0.0
88/128 (1): 0.0 = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[2] * sourceP.Q0 + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[2] + (-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[3] * sourceP.Q0
89/129 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[2]
90/130 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[2] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3])
91/131 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[3]
92/132 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[3] = exp((-0.033) * (sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[3]) ^ 2.0)
93/133 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[3])
94/134 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].rho)
95/135 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
96/136 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[3] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[3]))
97/137 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[3] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
98/138 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] < 0.0) then 1.0 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] >= 0.0) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] < 0.8) then 1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3]) else (5.0 + (-5.0) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3])) + (-4.0 + 5.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[3] / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[3])
99/139 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D
100/140 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[3] = 0.5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpfCorr * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[3] * sourceP.Q0 * abs(sourceP.Q0) / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[3])
101/141 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
102/142 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[3] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[3]))
103/143 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[3] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
104/144 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3], 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
105/145 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].rho)
106/146 (10): $cse6 = ThermoSysPro.Properties.Fluid.Ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
107/156 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].x, 0.1)
108/157 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[2] = abs(4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[2] / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2]))
109/158 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[2] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[2] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[2] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[2] ^ 0.4 else 0.0
110/159 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 0.0 else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].x, 0.9)
111/160 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[2] = abs(4.0 * sourceP.Q0 * (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[2]) / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2]))
112/161 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[2] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[2] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[2] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[2] ^ 0.4 else 0.0
113/162 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].x
114/163 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] >= 1.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].cp
115/164 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[2]
116/165 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].cp
117/166 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[2]
118/167 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2]) ^ 0.1 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2]) ^ 0.1 else ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2]) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2]) ^ 0.1
119/168 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[3] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].rho)
120/169 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
121/170 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
122/171 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[3] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].rho)
123/172 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
124/173 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
125/174 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].x) = $cse6
126/184 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].h - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].h
127/185 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2]) = ThermoSysPro.Properties.Fluid.Water_sat_P(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
128/199 (1): $cse7 = min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit - 1.0)
129/200 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3] = max($cse7, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ptriple)
130/201 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3] > 1.0) then 55.0 * (abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) ^ 0.12 / ((-log10(abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit)) ^ 0.55 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Mmol ^ 0.5) * (abs(dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi) ^ 0.67 else 100.0
131/202 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3] else (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[3]) else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[3] + (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3]) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[3])) / (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[3]
132/203 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[3] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3])
133/204 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[3]
134/205 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[3] = 6.283185307179586 * ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[3]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ntubes) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[3] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3])
135/206 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[3] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[3]) / $cse1
136/207 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[3] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[3]) / $cse2
137/208 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[3] = if noEvent(abs(sourceP.Q0) > 0.001) then abs((-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D / (4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1)) else 1e-5
138/209 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[3] > 0.0) then 1.0 + 24000.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[3] ^ 1.16 + 1.37 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[3] ^ 0.86 else 1.0
139/210 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[3] > 1e-6) then 1.0 / (1.0 + 1.15e-6 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[3] ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[3] ^ 1.17) else 0.0
140/211 (1): 0.0 = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[3] * sourceP.Q0 + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[3] + (-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[4] * sourceP.Q0
141/212 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[3]
142/213 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[3] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4])
143/214 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[3] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[4]
144/215 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[4] = exp((-0.033) * (sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[4]) ^ 2.0)
145/216 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[4] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5])
146/217 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[4]
147/218 (1): 0.0 = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[4] * sourceP.Q0 + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[4] + (-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[5] * sourceP.Q0
148/219 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4] > 1.0) then 55.0 * (abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) ^ 0.12 / ((-log10(abs(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit)) ^ 0.55 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Mmol ^ 0.5) * (abs(dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi) ^ 0.67 else 100.0
149/220 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4] else (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[4]) else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[4] + (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4]) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[4])) / (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[4]
150/221 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[4] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[4] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[4] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[4] ^ 0.4 else 0.0
151/222 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[4] = abs(4.0 * sourceP.Q0 * (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[4]) / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4]))
152/223 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 0.0 else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].x, 0.9)
153/224 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].x, 0.1)
154/225 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[4] = abs(4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[4] / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4]))
155/226 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[4] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[4] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[4] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[4] ^ 0.4 else 0.0
156/227 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].x
157/228 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] >= 1.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].cp
158/229 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[4]
159/230 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].cp
160/231 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[4]
161/232 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4]) ^ 0.1 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4]) ^ 0.1 else ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4]) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4]) ^ 0.1
162/233 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[4] > 0.0) then 1.0 + 24000.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[4] ^ 1.16 + 1.37 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[4] ^ 0.86 else 1.0
163/234 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[4] > 1e-6) then 1.0 / (1.0 + 1.15e-6 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[4] ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[4] ^ 1.17) else 0.0
164/235 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[4] = 6.283185307179586 * ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[4]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ntubes) * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[4] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4])
165/236 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[4]
166/237 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dSi * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[4] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4])
167/238 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
168/239 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
169/240 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
170/241 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
171/242 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].h - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].h
172/243 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[4] = if noEvent(abs(sourceP.Q0) > 0.001) then abs((-dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4]) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D / (4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx1)) else 1e-5
173/244 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[5] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].rho)
174/245 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[5] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].rho)
175/246 (10): $cse10 = ThermoSysPro.Properties.Fluid.Ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
176/256 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].x) = $cse10
177/266 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4]) = ThermoSysPro.Properties.Fluid.Water_sat_P(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
178/280 (1): $cse11 = min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit - 1.0)
179/281 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[5] = max($cse11, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ptriple)
180/282 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[5] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] < 0.0) then 1.0 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] >= 0.0) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] < 0.8) then 1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[5]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[5]) else (5.0 + (-5.0) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[5]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[5])) + (-4.0 + 5.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[5] / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[5])
181/283 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[5] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[5] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[5] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
182/284 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[5] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[5]))
183/285 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
184/286 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[5] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5], 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] + sinkP.P0), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
185/287 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_s[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[5])
186/288 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[4] = exp((-0.033) * (sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_s[4]) ^ 2.0)
187/289 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[4] = if sinkP.diffusion then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[4] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[6] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5]) else 0.0
188/290 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[4] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_s[4]
189/291 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[5] = if noEvent(sinkP.P0 > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].rho)
190/292 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[5] = if noEvent(sinkP.P0 > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].rho)
191/293 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
192/294 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[5] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[5]))
193/295 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[5] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[5] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[5] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
194/296 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] = if noEvent(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] + sinkP.P0) > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].x
195/297 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[5] = if noEvent(sinkP.P0 > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].cp
196/298 (10): $cse16 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] + sinkP.P0), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
197/308 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].x) = $cse16
198/318 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[5] = if sourceP.Q0 > 0.0 then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5] else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[6]
199/319 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[4] = if sourceP.Q0 > 0.0 then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4] else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5]
200/320 (10): $cse8 = ThermoSysPro.Properties.Fluid.Ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
201/330 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] >= 1.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].cp
202/331 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[3]
203/332 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[3] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[3] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[3] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[3] ^ 0.4 else 0.0
204/333 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].cp
205/334 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[3]
206/335 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[3] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[3] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[3] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[3] ^ 0.4 else 0.0
207/336 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[4] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].rho)
208/337 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
209/338 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[3] = abs(4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[3] / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3]))
210/339 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3]) ^ 0.1 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3]) ^ 0.1 else ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3]) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3]) ^ 0.1
211/340 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
212/341 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[4] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].rho)
213/342 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
214/343 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[3] = abs(4.0 * sourceP.Q0 * (1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[3]) / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3]))
215/344 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
216/345 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].x, 0.1)
217/346 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 0.0 else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].x, 0.9)
218/347 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].x
219/348 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].h - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].h
220/349 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].x) = $cse8
221/359 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[3] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[3] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4])
222/360 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[3] = if sourceP.Q0 > 0.0 then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3] else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4]
223/361 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[2] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3])
224/362 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[2] = if sourceP.Q0 > 0.0 then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2] else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3]
225/363 (10): $cse13 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
226/373 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] = if noEvent(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3]) > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].x
227/374 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].cp
228/375 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[2])
229/376 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[2] = exp((-0.033) * (sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[2]) ^ 2.0)
230/377 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[2]
231/378 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[1] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2])
232/379 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[2] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[2]
233/380 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[1] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[2]
234/381 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] < 0.0) then 1.0 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] >= 0.0) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] < 0.8) then 1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2]) else (5.0 + (-5.0) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2])) + (-4.0 + 5.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[2] / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[2])
235/382 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[2] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[2] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D
236/383 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[2] = 0.5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpfCorr * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[2] * sourceP.Q0 * abs(sourceP.Q0) / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[2])
237/384 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
238/385 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[2] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[2]))
239/386 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[2] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
240/387 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2], 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
241/388 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].rho)
242/389 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1]) = ThermoSysPro.Properties.Fluid.Water_sat_P(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
243/403 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].h - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].h
244/404 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[2] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].rho)
245/405 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
246/406 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[1]
247/407 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] < dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb1) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1]) ^ 0.1 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) then ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xb2) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1]) ^ 0.1 else ((1.0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1]) / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1]) ^ 0.9 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1]) ^ 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1]) ^ 0.1
248/408 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].cp
249/409 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[2] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].rho)
250/410 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
251/411 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[1] = abs(4.0 * sourceP.Q0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[1] / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1]))
252/412 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[1] > 1e-6) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[1] > 1e-6) then 0.023 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[1] ^ 0.8 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[1] ^ 0.4 else 0.0
253/413 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[1] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[1] / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[1]
254/414 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
255/415 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] >= 1.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].cp
256/416 (1): $cse5 = min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit - 1.0)
257/417 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2] = max($cse5, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ptriple)
258/418 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
259/432 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] + (-dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[2]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[2] = 0.0
260/433 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x, 0.1)
261/434 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 0.0 else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x, 0.9)
262/435 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x
263/436 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].rho)
264/437 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
265/438 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[2] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[2]))
266/439 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[2] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[2] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[2] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
267/440 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].x) = $cse13
268/450 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[2] = 9.80665 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[2] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z2 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.L
269/451 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[5] = 9.80665 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[5] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z2 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.L
270/452 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] + (-dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[5]) - sinkP.P0 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[5] = 0.0
271/453 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[5] = 0.5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpfCorr * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[5] * sourceP.Q0 * abs(sourceP.Q0) / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[5])
272/454 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[5] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[5] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D
273/455 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3]) = ThermoSysPro.Properties.Fluid.Water_sat_P(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
274/469 (1): $cse9 = min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit - 1.0)
275/470 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4] = max($cse9, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.ptriple)
276/471 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] < 0.0) then 1.0 else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] >= 0.0) and noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] < 0.8) then 1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4]) else (5.0 + (-5.0) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * (1.0 + /*Real*/(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.a) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss * exp((-1.1904761904761906e-7) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4]) / (19.0 + 1e-5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4])) + (-4.0 + 5.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rgliss) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[4] / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[4])
277/472 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D
278/473 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[4] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
279/474 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[4] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[4]))
280/475 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
281/476 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
282/477 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[4] = abs(4.0 * sourceP.Q0 / (3.141592653589793 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Di * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv2[4]))
283/478 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[4] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.D)) ^ 2.0 else 0.01
284/479 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_rhoT(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4], 0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
285/480 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[4] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[4] * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[4])
286/481 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov2[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4] else min(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].rho)
287/482 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4] else max(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].rho)
288/483 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[4] = 0.5 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpfCorr * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[4] * sourceP.Q0 * abs(sourceP.Q0) / (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.A ^ 2.0 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol2[4])
289/484 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[4] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].cp
290/485 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4] = if noEvent(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5]) > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].x
291/486 (10): $cse15 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
292/496 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].x) = $cse15
293/506 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[4] = 9.80665 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[4] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z2 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.L
294/507 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] + (-dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[4]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[4] = 0.0
295/508 (10): $cse14 = ThermoSysPro.Properties.Fluid.Ph(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mode, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
296/518 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] = if noEvent(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4]) > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then 1.0 else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].x
297/519 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[3] = if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pcrit) or noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3] > dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tcrit) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].cp else if noEvent(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3] <= 0.0) then dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].cp else dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].cp
298/520 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].x) = $cse14
299/530 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
300/544 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] + dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5]), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
301/558 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3] + (-dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[3]) - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4] - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[3] = 0.0
302/559 (14): (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5]) = ThermoSysPro.Properties.Fluid.Water_sat_P(0.5 * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5] + sinkP.P0), dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.fluid)
303/573 (1): -dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[4] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[4]) / $cse2
304/574 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerWall.dx * dynamicMultiFluidHeatExchanger.ExchangerWall.ntubes * dynamicMultiFluidHeatExchanger.ExchangerWall.lambda * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[4] - dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[4]) / $cse1
305/575 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[4]
306/576 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dSi * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[4] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[4])
307/577 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[4] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.ntubes) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[4] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[4] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[4])
308/578 (1): 0.0 = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4] * sourceP1.Q + dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[4] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5] * sourceP1.Q
309/579 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[4] = ThermoSysPro.Properties.Fluid.Density_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
310/580 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[4] = 0.5 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpfCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[4] * sourceP1.Q * abs(sourceP1.Q) / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A ^ 2.0 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[4])
311/581 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
312/582 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[4] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[4] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D)) ^ 2.0 else 0.01
313/583 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[4] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[4]))
314/584 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
315/585 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[4] = ThermoSysPro.Properties.Fluid.Temperature_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
316/586 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[4] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
317/587 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[4] / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[4]
318/588 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[4] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[4] > 2000.0) then 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[4] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[4] ^ 0.4 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[4] * max(4.36, 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[4] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[4] ^ 0.4) / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
319/589 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[4] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
320/590 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[4] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[4]))
321/591 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
322/592 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[4] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
323/593 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[3] = ThermoSysPro.Properties.Fluid.Temperature_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
324/594 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[3] = 6.283185307179586 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx1 * /*Real*/(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.ntubes) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[3] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[3] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[3])
325/595 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[3]
326/596 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dSi * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[3] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[3])
327/597 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[3] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
328/598 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[3] / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[3]
329/599 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[3] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[3] > 2000.0) then 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[3] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[3] ^ 0.4 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[3] * max(4.36, 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[3] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[3] ^ 0.4) / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
330/600 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
331/601 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[3] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[3]))
332/602 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
333/603 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[3] = ThermoSysPro.Properties.Fluid.Density_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
334/604 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[3] = 0.5 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpfCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[3] * sourceP1.Q * abs(sourceP1.Q) / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A ^ 2.0 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[3])
335/605 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
336/606 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[3] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[3] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D)) ^ 2.0 else 0.01
337/607 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[3] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[3]))
338/608 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[3] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
339/609 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[3] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
340/610 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[3])
341/611 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[3] = exp((-0.033) * (sourceP1.Q * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[3]) ^ 2.0)
342/612 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[3] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4])
343/613 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[3]
344/614 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[3] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[3] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4])
345/615 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[3]
346/616 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[4] = exp((-0.033) * (sourceP1.Q * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[4]) ^ 2.0)
347/617 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[4])
348/618 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[4] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[4]
349/619 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[4] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5])
350/620 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[4]
351/621 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[3] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[4]
352/622 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[3] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[2]
353/623 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[2] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3])
354/624 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[3] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[3]
355/625 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[2] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[3]
356/626 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[3] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
357/627 (1): 0.0 = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3] * sourceP1.Q + dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[3] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4] * sourceP1.Q
358/628 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3] = if sourceP1.Q > 0.0 then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3] else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4]
359/629 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[2] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
360/630 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[2] / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[2]
361/631 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[2] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[2] > 2000.0) then 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[2] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[2] ^ 0.4 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hcCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[2] * max(4.36, 0.023 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[2] ^ 0.8 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[2] ^ 0.4) / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
362/632 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dSi * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[2] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[2])
363/633 (1): dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[2]
364/634 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[2] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
365/635 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[2] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[2]))
366/636 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
367/637 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2] = if sourceP1.Q > 0.0 then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2] else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3]
368/638 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1] = if sourceP1.Q > 0.0 then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[1] else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2]
369/639 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[1] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(0.5 * (sourceP1.P0 + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
370/640 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[1] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(0.5 * (sourceP1.P0 + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
371/641 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[1] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[1] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[1] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2])
372/642 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[3] = 9.80665 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[3] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z2 - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z1) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.L
373/643 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3] + (-dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[3]) - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[3] = 0.0
374/644 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[4] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
375/645 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4] + (-dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[4]) - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[4] = 0.0
376/646 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[5] = ThermoSysPro.Properties.Fluid.Density_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5] + sinkP1.P0), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
377/647 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[5] = 0.5 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpfCorr * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[5] * sourceP1.Q * abs(sourceP1.Q) / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A ^ 2.0 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[5])
378/648 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[5] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[5] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D
379/649 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[5] = if noEvent(dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[5] > 1.0) then 0.25 / log10(13.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[5] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rugosrel / (3.7 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.D)) ^ 2.0 else 0.01
380/650 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[5] = abs(4.0 * sourceP1.Q / (3.141592653589793 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Di * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[5]))
381/651 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[5] = ThermoSysPro.Properties.Fluid.DynamicViscosity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5] + sinkP1.P0), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
382/652 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[5] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5] + sinkP1.P0), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
383/653 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_s[4] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[5] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[5])
384/654 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[4] = exp((-0.033) * (sourceP1.Q * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_s[4]) ^ 2.0)
385/655 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[4] = if sinkP1.diffusion then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[4] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[4] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[6] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5]) else 0.0
386/656 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[4] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_s[4]
387/657 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[5] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5] + sinkP1.P0), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
388/658 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5] = if sourceP1.Q > 0.0 then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5] else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[6]
389/659 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4] = if sourceP1.Q > 0.0 then dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4] else dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5]
390/660 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[5] = 9.80665 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[5] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z2 - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z1) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.L
391/661 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5] + (-dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[5]) - sinkP1.P0 - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[5] = 0.0
392/662 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[4] = 9.80665 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[4] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z2 - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z1) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.L
393/663 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[3] = dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[4]
394/664 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[4] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[4]
395/665 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[3] = 9.80665 * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rho2[3] * (dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z2 - dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.z1) * dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dx2 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.L
396/666 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[3] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[3]
397/667 (1): dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[2] = 1.0 / dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[3]
398/668 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[2] = ThermoSysPro.Properties.Fluid.SpecificHeatCapacityCp_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
399/669 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[2] * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.A * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[2])
400/670 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[2] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[2]
401/671 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[1] = 1.0 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[2]
402/672 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[2] = ThermoSysPro.Properties.Fluid.ThermalConductivity_Ph(0.5 * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2] + dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3]), dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2], dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.fluid, dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mode, 0.01, 0.05, 0.22, 0.0)
403/673 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2] + (-dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[2]) - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[2] = 0.0
404/674 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[2] = 9.80665 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[2] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z2 - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z1) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.L
405/675 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[2] = dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[1]
406/676 (1): dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[1] = 9.80665 * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[1] * (dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z2 - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.z1) * dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dx2 / dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.L
407/677 (1): sourceP1.P0 + (-dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[1]) - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2] - dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[1] = 0.0
408/678 (10): ThermoSysPro.Properties.WaterSteam.Common.ThermoProperties_ph(dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.T1[1], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhoc[2], dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].u, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].s, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duph, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duhp, dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x) = $cse4

Variables:
1: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [4]
2: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [4]
3: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [6]
4: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [4]
5: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [4]
6: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [4]
7: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [4]
8: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [4]
9: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[1]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
10: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[1]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
11: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[1]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
12: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[2]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
13: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[2]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
14: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[2]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in hydraulic node i" type: Real [5]
15: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[1]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
16: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[2]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
17: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[2]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
18: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[2]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in hydraulic node i" type: Real [5]
19: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[2]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
20: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[3]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
21: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[3]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
22: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[4]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
23: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[3]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
24: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[4]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
25: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[5]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
26: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[5]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
27: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[4]:VARIABLE(start = 71016.1223718091 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
28: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[5]:VARIABLE(start = 71016.125 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
29: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[5]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in hydraulic node i" type: Real [5]
30: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[4]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
31: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[4]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
32: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[4]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
33: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_s[4]:VARIABLE()  "Diffusion resistance at outlet of thermal node i" type: Real [4]
34: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[5]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in hydraulic node i" type: Real [5]
35: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[5]:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
36: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[5]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in hydraulic node i" type: Real [5]
37: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[5]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in hydraulic node i" type: Real [5]
38: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[5]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i" type: Real [5]
39: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[5]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
40: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[5]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in hydraulic node i" type: Real [5]
41: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[4]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
42: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[4]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in hydraulic node i" type: Real [5]
43: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpf[3]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
44: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dpg[3]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
45: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[1]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
46: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[1]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in hydraulic node i" type: Real [5]
47: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[1]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in hydraulic node i" type: Real [5]
48: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[1]:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
49: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[2]:VARIABLE(start = 71016.125 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
50: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[2]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in thermal node i" type: Real [4]
51: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[2]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in thermal node i" type: Real [4]
52: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[2]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in thermal node i" type: Real [4]
53: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[2]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
54: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[2]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
55: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[2]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i" type: Real [4]
56: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[2]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i" type: Real [4]
57: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[2]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in thermal node i" type: Real [4]
58: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.h[3]:VARIABLE(start = 71016.12237180988 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
59: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[3]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
60: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k2[3]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in hydraulic node i" type: Real [5]
61: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[2]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
62: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[3]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
63: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[2]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
64: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[2]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
65: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_s[3]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
66: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[4]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
67: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[4]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
68: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[4]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
69: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[4]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in hydraulic node i" type: Real [5]
70: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[4]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
71: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[4]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
72: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rs[3]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
73: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Js[3]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
74: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[3]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
75: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[3]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
76: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[3]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
77: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[3]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in hydraulic node i" type: Real [5]
78: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[3]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
79: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[3]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in hydraulic node i" type: Real [5]
80: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[3]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in hydraulic node i" type: Real [5]
81: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[3]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i" type: Real [5]
82: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[3]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
83: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[3]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in hydraulic node i" type: Real [5]
84: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[3]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in thermal node i" type: Real [4]
85: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[3]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in thermal node i" type: Real [4]
86: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[3]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in thermal node i" type: Real [4]
87: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[3]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i" type: Real [4]
88: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[3]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i" type: Real [4]
89: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[3]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in thermal node i" type: Real [4]
90: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[3]:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
91: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[3]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
92: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[3]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
93: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[3]:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [4]
94: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[4]:VARIABLE(min = 0.0 start = 180002.39588440701 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
95: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[4]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in thermal node i" type: Real [4]
96: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[4]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in thermal node i" type: Real [4]
97: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[4]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in thermal node i" type: Real [4]
98: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[4]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i" type: Real [4]
99: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[4]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i" type: Real [4]
100: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[4]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in thermal node i" type: Real [4]
101: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[4]:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [4]
102: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[5]:VARIABLE(min = 0.0 start = 140001.5973181204 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
103: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[4]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in hydraulic node i" type: Real [5]
104: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[4]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in hydraulic node i" type: Real [5]
105: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[4]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i" type: Real [5]
106: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[4]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
107: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[4]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in hydraulic node i" type: Real [5]
108: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[4]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
109: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[4]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
110: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[4]:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
111: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[4]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
112: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[4]:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
113: dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[4]:VARIABLE(min = 0.0 start = 290.05847909289605 unit = "K" nominal = 300.0 )  "Average wall temperature in section i" type: Real [4]
114: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
115: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
116: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
117: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
118: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
119: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
120: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
121: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
122: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
123: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
124: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
125: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[5].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
126: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
127: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[5].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
128: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[3]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
129: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
130: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
131: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
132: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
133: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
134: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
135: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
136: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
137: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
138: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
139: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
140: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
141: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
142: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
143: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
144: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
145: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
146: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
147: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
148: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
149: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
150: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
151: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[3]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [5]
152: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[3]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [5]
153: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
154: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
155: $cse14.T:VARIABLE(protected = true )  type: Real unreplaceable
156: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
157: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[3].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
158: $cse14.s:VARIABLE(protected = true )  type: Real unreplaceable
159: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[3]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
160: $cse14.cp:VARIABLE(protected = true )  type: Real unreplaceable
161: $cse14.ddph:VARIABLE(protected = true )  type: Real unreplaceable
162: $cse14.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
163: $cse14.x:VARIABLE(protected = true )  type: Real unreplaceable
164: $cse14.duhp:VARIABLE(protected = true )  type: Real unreplaceable
165: $cse14.u:VARIABLE(protected = true )  type: Real unreplaceable
166: $cse14.duph:VARIABLE(protected = true )  type: Real unreplaceable
167: $cse14.d:VARIABLE(protected = true )  type: Real unreplaceable
168: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[4]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
169: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[4]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
170: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
171: $cse15.duhp:VARIABLE(protected = true )  type: Real unreplaceable
172: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
173: $cse15.T:VARIABLE(protected = true )  type: Real unreplaceable
174: $cse15.u:VARIABLE(protected = true )  type: Real unreplaceable
175: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[4]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
176: $cse15.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
177: $cse15.ddph:VARIABLE(protected = true )  type: Real unreplaceable
178: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[4]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [5]
179: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
180: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
181: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
182: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
183: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
184: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[4]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [5]
185: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[4].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
186: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[4]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
187: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
188: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
189: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
190: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[4]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [5]
191: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[4]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [5]
192: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[4]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [5]
193: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
194: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
195: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
196: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[4]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [5]
197: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[4]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [5]
198: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[4]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [5]
199: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[4]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [6]
200: $cse9:VARIABLE(protected = true )  type: Real unreplaceable
201: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
202: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
203: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
204: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
205: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
206: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
207: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
208: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
209: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
210: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
211: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
212: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
213: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[3].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
214: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[3].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
215: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[4]:VARIABLE(min = 0.0 start = 180002.3972020214 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
216: $cse15.x:VARIABLE(protected = true )  type: Real unreplaceable
217: $cse15.duph:VARIABLE(protected = true )  type: Real unreplaceable
218: $cse15.s:VARIABLE(protected = true )  type: Real unreplaceable
219: $cse15.d:VARIABLE(protected = true )  type: Real unreplaceable
220: $cse15.cp:VARIABLE(protected = true )  type: Real unreplaceable
221: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[5]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [5]
222: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[5]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
223: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[5]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
224: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[5]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
225: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[2]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
226: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
227: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
228: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
229: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
230: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
231: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
232: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
233: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[2]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [5]
234: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[2]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [5]
235: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
236: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
237: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[1]:VARIABLE()  "Vapor mass fraction in thermal node i" type: Real [4]
238: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[1]:VARIABLE()  "Bounded upper value for the vapor mass fraction" type: Real [4]
239: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[1]:VARIABLE()  "Bounded lower value for the vapor mass fraction" type: Real [4]
240: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[2]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
241: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
242: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[2]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [6]
243: $cse5:VARIABLE(protected = true )  type: Real unreplaceable
244: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[1]:VARIABLE(start = 2000.0 unit = "J/(kg.K)" nominal = 2000.0 )  "Specific heat capacity in thermal node i for the vapor" type: Real [4]
245: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[1]:VARIABLE(start = 0.03 unit = "W/(m.K)" nominal = 0.03 )  "Thermal conductivity in thermal node i for the vapor" type: Real [4]
246: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[1]:VARIABLE(start = 1.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the vapor" type: Real [4]
247: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[1]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the vapor fraction" type: Real [4]
248: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[1]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in thermal node i for the vapor" type: Real [4]
249: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[1]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 )  "Dynamic viscosity in thermal node i for the vapor" type: Real [4]
250: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[1]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in thermal node i for the vapor" type: Real [4]
251: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[1]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in thermal node i for the liquid" type: Real [4]
252: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[1]:VARIABLE(start = 1.0 nominal = 1.0 )  "Martinelli number" type: Real [4]
253: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[1]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the liquid" type: Real [4]
254: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[1]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in thermal node i for the liquid" type: Real [4]
255: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[1]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density in thermal node i for the liquid" type: Real [4]
256: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[1]:VARIABLE(start = 2e6 unit = "J/kg" nominal = 2e6 )  "Specific enthalpy for vaporisation" type: Real [4]
257: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
258: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
259: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
260: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
261: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
262: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
263: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
264: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
265: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
266: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[1].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
267: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
268: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
269: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
270: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[1].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
271: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[2]:VARIABLE(min = 0.0 start = 260001.59801114563 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
272: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
273: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
274: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
275: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
276: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
277: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
278: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
279: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
280: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[2].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
281: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
282: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
283: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
284: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
285: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[2]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [5]
286: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[2]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [5]
287: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[2]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [5]
288: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
289: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
290: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[2]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
291: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[2]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [5]
292: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[1]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
293: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[2]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
294: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[1]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
295: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[1]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
296: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[2]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
297: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[2]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
298: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[2]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [5]
299: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[2]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [5]
300: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
301: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
302: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[2].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
303: $cse13.cp:VARIABLE(protected = true )  type: Real unreplaceable
304: $cse13.x:VARIABLE(protected = true )  type: Real unreplaceable
305: $cse13.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
306: $cse13.u:VARIABLE(protected = true )  type: Real unreplaceable
307: $cse13.duhp:VARIABLE(protected = true )  type: Real unreplaceable
308: $cse13.s:VARIABLE(protected = true )  type: Real unreplaceable
309: $cse13.duph:VARIABLE(protected = true )  type: Real unreplaceable
310: $cse13.ddph:VARIABLE(protected = true )  type: Real unreplaceable
311: $cse13.d:VARIABLE(protected = true )  type: Real unreplaceable
312: $cse13.T:VARIABLE(protected = true )  type: Real unreplaceable
313: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[2]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
314: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[2]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
315: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[3]:VARIABLE(start = 71016.12237181216 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
316: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[3]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
317: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [4]
318: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [4]
319: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[3]:VARIABLE(start = 2e6 unit = "J/kg" nominal = 2e6 )  "Specific enthalpy for vaporisation" type: Real [4]
320: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [4]
321: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [4]
322: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [4]
323: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [4]
324: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[3]:VARIABLE()  "Vapor mass fraction in thermal node i" type: Real [4]
325: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[3]:VARIABLE()  "Bounded upper value for the vapor mass fraction" type: Real [4]
326: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[3]:VARIABLE()  "Bounded lower value for the vapor mass fraction" type: Real [4]
327: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [4]
328: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[3]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in thermal node i for the liquid" type: Real [4]
329: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[3]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in thermal node i for the liquid" type: Real [4]
330: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[3]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Dynamic viscosity in thermal node i for the liquid" type: Real [4]
331: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[3]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density in thermal node i for the liquid" type: Real [4]
332: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[3]:VARIABLE(start = 0.03 unit = "W/(m.K)" nominal = 0.03 )  "Thermal conductivity in thermal node i for the vapor" type: Real [4]
333: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[3]:VARIABLE(start = 1.0 nominal = 1.0 )  "Martinelli number" type: Real [4]
334: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[3]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in thermal node i for the vapor" type: Real [4]
335: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[3]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 )  "Dynamic viscosity in thermal node i for the vapor" type: Real [4]
336: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[3]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in thermal node i for the vapor" type: Real [4]
337: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [6]
338: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [4]
339: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[3]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the liquid fraction" type: Real [4]
340: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[3]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the liquid" type: Real [4]
341: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[3]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in thermal node i for the liquid" type: Real [4]
342: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[3]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the vapor fraction" type: Real [4]
343: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[3]:VARIABLE(start = 1.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the vapor" type: Real [4]
344: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[3]:VARIABLE(start = 2000.0 unit = "J/(kg.K)" nominal = 2000.0 )  "Specific heat capacity in thermal node i for the vapor" type: Real [4]
345: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[3].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [4]
346: $cse8.ddph:VARIABLE(protected = true )  type: Real unreplaceable
347: $cse8.u:VARIABLE(protected = true )  type: Real unreplaceable
348: $cse8.duph:VARIABLE(protected = true )  type: Real unreplaceable
349: $cse8.s:VARIABLE(protected = true )  type: Real unreplaceable
350: $cse8.d:VARIABLE(protected = true )  type: Real unreplaceable
351: $cse8.x:VARIABLE(protected = true )  type: Real unreplaceable
352: $cse8.cp:VARIABLE(protected = true )  type: Real unreplaceable
353: $cse8.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
354: $cse8.T:VARIABLE(protected = true )  type: Real unreplaceable
355: $cse8.duhp:VARIABLE(protected = true )  type: Real unreplaceable
356: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[4]:VARIABLE(start = 71016.12237181274 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
357: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[5]:VARIABLE(start = 71016.125 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
358: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
359: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
360: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
361: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
362: $cse16.s:VARIABLE(protected = true )  type: Real unreplaceable
363: $cse16.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
364: $cse16.cp:VARIABLE(protected = true )  type: Real unreplaceable
365: $cse16.T:VARIABLE(protected = true )  type: Real unreplaceable
366: $cse16.u:VARIABLE(protected = true )  type: Real unreplaceable
367: $cse16.duph:VARIABLE(protected = true )  type: Real unreplaceable
368: $cse16.duhp:VARIABLE(protected = true )  type: Real unreplaceable
369: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[5]:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
370: $cse16.ddph:VARIABLE(protected = true )  type: Real unreplaceable
371: $cse16.d:VARIABLE(protected = true )  type: Real unreplaceable
372: $cse16.x:VARIABLE(protected = true )  type: Real unreplaceable
373: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
374: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
375: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[5]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [5]
376: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[5]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [5]
377: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
378: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
379: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[5].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
380: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[5]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [5]
381: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[5]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [5]
382: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
383: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
384: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
385: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[4]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
386: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[4]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
387: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[4]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
388: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_s[4]:VARIABLE()  "Diffusion resistance at outlet of thermal node i" type: Real [4]
389: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[5]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [5]
390: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
391: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
392: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[5]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [5]
393: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[5]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [5]
394: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[5]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [6]
395: $cse11:VARIABLE(protected = true )  type: Real unreplaceable
396: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
397: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
398: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
399: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
400: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
401: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
402: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
403: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
404: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
405: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[4].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
406: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
407: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
408: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
409: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[4].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
410: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [4]
411: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [4]
412: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [4]
413: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [4]
414: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [4]
415: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [6]
416: $cse10.duhp:VARIABLE(protected = true )  type: Real unreplaceable
417: $cse10.d:VARIABLE(protected = true )  type: Real unreplaceable
418: $cse10.duph:VARIABLE(protected = true )  type: Real unreplaceable
419: $cse10.cp:VARIABLE(protected = true )  type: Real unreplaceable
420: $cse10.ddph:VARIABLE(protected = true )  type: Real unreplaceable
421: $cse10.T:VARIABLE(protected = true )  type: Real unreplaceable
422: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[5]:VARIABLE(min = 0.0 start = 140001.59819646296 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
423: $cse10.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
424: $cse10.u:VARIABLE(protected = true )  type: Real unreplaceable
425: $cse10.s:VARIABLE(protected = true )  type: Real unreplaceable
426: $cse10.x:VARIABLE(protected = true )  type: Real unreplaceable
427: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[4]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density in thermal node i for the liquid" type: Real [4]
428: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[4]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in thermal node i for the vapor" type: Real [4]
429: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[4]:VARIABLE(start = 0.0 nominal = 4e-4 )  "Boiling number" type: Real [4]
430: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[4]:VARIABLE(start = 2e6 unit = "J/kg" nominal = 2e6 )  "Specific enthalpy for vaporisation" type: Real [4]
431: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[4]:VARIABLE(start = 0.03 unit = "W/(m.K)" nominal = 0.03 )  "Thermal conductivity in thermal node i for the vapor" type: Real [4]
432: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[4]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in thermal node i for the liquid" type: Real [4]
433: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[4]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 )  "Dynamic viscosity in thermal node i for the vapor" type: Real [4]
434: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[4]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Dynamic viscosity in thermal node i for the liquid" type: Real [4]
435: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [4]
436: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [4]
437: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [4]
438: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[4]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 2e4 )  "Fluid heat exchange coefficient in node i" type: Real [4]
439: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[4]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
440: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[4]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
441: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[4]:VARIABLE()  "Corrective term for nucleation removal" type: Real [4]
442: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[4]:VARIABLE()  "Corrective term for hcl" type: Real [4]
443: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[4]:VARIABLE(start = 1.0 nominal = 1.0 )  "Martinelli number" type: Real [4]
444: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[4]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the liquid" type: Real [4]
445: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[4]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in thermal node i for the liquid" type: Real [4]
446: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[4]:VARIABLE(start = 1.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the vapor" type: Real [4]
447: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[4]:VARIABLE(start = 2000.0 unit = "J/(kg.K)" nominal = 2000.0 )  "Specific heat capacity in thermal node i for the vapor" type: Real [4]
448: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[4]:VARIABLE()  "Vapor mass fraction in thermal node i" type: Real [4]
449: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[4]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the vapor fraction" type: Real [4]
450: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[4]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in thermal node i for the vapor" type: Real [4]
451: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[4]:VARIABLE()  "Bounded lower value for the vapor mass fraction" type: Real [4]
452: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[4].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [4]
453: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[4]:VARIABLE()  "Bounded upper value for the vapor mass fraction" type: Real [4]
454: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[4]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in thermal node i for the liquid" type: Real [4]
455: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[4]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the liquid fraction" type: Real [4]
456: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[4]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 5e5 )  "Fluid heat exchange coefficient for vaporization in thermal node i" type: Real [4]
457: dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[4]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Power in section i of side 1" type: Real [4]
458: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[4]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
459: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[4]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
460: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[4]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
461: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[4]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
462: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_s[3]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at outlet of thermal node i" type: Real [4]
463: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[3]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
464: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[3]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
465: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[3]:VARIABLE()  "Corrective term for nucleation removal" type: Real [4]
466: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[3]:VARIABLE()  "Corrective term for hcl" type: Real [4]
467: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[3]:VARIABLE(start = 0.0 nominal = 4e-4 )  "Boiling number" type: Real [4]
468: dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[3]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Power in section i of side 1" type: Real [4]
469: dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[3]:VARIABLE(min = 0.0 start = 290.0493302229999 unit = "K" nominal = 300.0 )  "Average wall temperature in section i" type: Real [4]
470: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[3]:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
471: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[3]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
472: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[3]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
473: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[3]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 2e4 )  "Fluid heat exchange coefficient in node i" type: Real [4]
474: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[3]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 5e5 )  "Fluid heat exchange coefficient for vaporization in thermal node i" type: Real [4]
475: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[3]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [6]
476: $cse7:VARIABLE(protected = true )  type: Real unreplaceable
477: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
478: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
479: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
480: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [4]
481: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
482: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [4]
483: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [4]
484: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [4]
485: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
486: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
487: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
488: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [4]
489: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat1[2].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [4]
490: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat1[2].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [4]
491: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lv[2]:VARIABLE(start = 2e6 unit = "J/kg" nominal = 2e6 )  "Specific enthalpy for vaporisation" type: Real [4]
492: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [4]
493: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [4]
494: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [4]
495: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl1[2]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in thermal node i for the liquid" type: Real [4]
496: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[2]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Dynamic viscosity in thermal node i for the liquid" type: Real [4]
497: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhol1[2]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 998.0 )  "Fluid density in thermal node i for the liquid" type: Real [4]
498: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kv1[2]:VARIABLE(start = 0.03 unit = "W/(m.K)" nominal = 0.03 )  "Thermal conductivity in thermal node i for the vapor" type: Real [4]
499: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.muv1[2]:VARIABLE(min = 0.0 start = 1e-5 unit = "Pa.s" nominal = 1e-4 )  "Dynamic viscosity in thermal node i for the vapor" type: Real [4]
500: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rhov1[2]:VARIABLE(min = 0.0 start = 1.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in thermal node i for the vapor" type: Real [4]
501: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [6]
502: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [4]
503: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [4]
504: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Xtt[2]:VARIABLE(start = 1.0 nominal = 1.0 )  "Martinelli number" type: Real [4]
505: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prl[2]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the liquid" type: Real [4]
506: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl1[2]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in thermal node i for the liquid" type: Real [4]
507: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Prv[2]:VARIABLE(start = 1.0 nominal = 1.0 )  "Fluid Prandtl number in node i for the vapor" type: Real [4]
508: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpv1[2]:VARIABLE(start = 2000.0 unit = "J/(kg.K)" nominal = 2000.0 )  "Specific heat capacity in thermal node i for the vapor" type: Real [4]
509: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv1[2]:VARIABLE()  "Vapor mass fraction in thermal node i" type: Real [4]
510: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[2]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the liquid fraction" type: Real [4]
511: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[2]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in thermal node i for the liquid" type: Real [4]
512: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbs[2]:VARIABLE()  "Bounded upper value for the vapor mass fraction" type: Real [4]
513: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcv[2]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the vapor fraction" type: Real [4]
514: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev1[2]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in thermal node i for the vapor" type: Real [4]
515: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xbi[2]:VARIABLE()  "Bounded lower value for the vapor mass fraction" type: Real [4]
516: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [4]
517: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [4]
518: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [4]
519: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[2].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [4]
520: $cse6.cp:VARIABLE(protected = true )  type: Real unreplaceable
521: $cse6.ddph:VARIABLE(protected = true )  type: Real unreplaceable
522: $cse6.s:VARIABLE(protected = true )  type: Real unreplaceable
523: $cse6.T:VARIABLE(protected = true )  type: Real unreplaceable
524: $cse6.x:VARIABLE(protected = true )  type: Real unreplaceable
525: $cse6.duhp:VARIABLE(protected = true )  type: Real unreplaceable
526: $cse6.d:VARIABLE(protected = true )  type: Real unreplaceable
527: $cse6.u:VARIABLE(protected = true )  type: Real unreplaceable
528: $cse6.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
529: $cse6.duph:VARIABLE(protected = true )  type: Real unreplaceable
530: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[3]:VARIABLE(min = 0.0 start = 220002.39710936273 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
531: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
532: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
533: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
534: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
535: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
536: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
537: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
538: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
539: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
540: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[3].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
541: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[3].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
542: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[3]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [5]
543: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[3]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [5]
544: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[3]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [5]
545: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
546: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
547: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[3]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
548: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[3]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [5]
549: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[3]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [5]
550: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[3]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [5]
551: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
552: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
553: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
554: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[3]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
555: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[3]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
556: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.rs[2]:VARIABLE()  "Value of r(Q/gamma) for outlet of thermal node i" type: Real [4]
557: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Js[2]:VARIABLE(unit = "W" )  "Thermal power diffusion from outlet of thermal node i" type: Real [4]
558: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[2]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
559: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[2]:VARIABLE()  "Corrective term for nucleation removal" type: Real [4]
560: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[2]:VARIABLE()  "Corrective term for hcl" type: Real [4]
561: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[2]:VARIABLE(start = 0.0 nominal = 4e-4 )  "Boiling number" type: Real [4]
562: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[2]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
563: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[2]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 2e4 )  "Fluid heat exchange coefficient in node i" type: Real [4]
564: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[2]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 5e5 )  "Fluid heat exchange coefficient for vaporization in thermal node i" type: Real [4]
565: dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[2]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Power in section i of side 1" type: Real [4]
566: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[2]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
567: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[2]:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
568: dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[2]:VARIABLE(min = 0.0 start = 290.0401814264445 unit = "K" nominal = 300.0 )  "Average wall temperature in section i" type: Real [4]
569: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[2]:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
570: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[2]:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [4]
571: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[3]:VARIABLE(min = 0.0 start = 220002.3957916478 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
572: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu2[2]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in hydraulic node i" type: Real [5]
573: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[2]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in hydraulic node i" type: Real [5]
574: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[2]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i" type: Real [5]
575: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[2]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
576: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[2]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in hydraulic node i" type: Real [5]
577: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hb[2]:VARIABLE(unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
578: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[2]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
579: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[2]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
580: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[2]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
581: sourceP1.Q:VARIABLE(start = 2702.7912398488343 unit = "kg/s" nominal = 10.0 )  "Fluid mass flow rate" type: Real
582: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re2[1]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in hydraulic node i" type: Real [5]
583: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.lambda[1]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i" type: Real [5]
584: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.khi[1]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
585: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.rho2[1]:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" nominal = 1.0 )  "Fluid density in hydraulic node i" type: Real [5]
586: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.k1[1]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Fluid thermal conductivity in thermal node i" type: Real [4]
587: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Re1[1]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Fluid Reynolds number in thermal node i" type: Real [4]
588: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.mu1[1]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Fluid dynamic viscosity in thermal node i" type: Real [4]
589: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.hc[1]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i" type: Real [4]
590: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Pr[1]:VARIABLE(start = 4.0 nominal = 1.0 )  "Fluid Prandtl number in node i" type: Real [4]
591: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp1[1]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in thermal node i" type: Real [4]
592: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.T1[1]:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Fluid temperature in thermal node i" type: Real [4]
593: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.P[2]:VARIABLE(min = 0.0 start = 260001.59713260198 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
594: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.cp2[1]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Fluid specific heat capacity in hydraulic node i" type: Real [5]
595: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.re[1]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
596: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.diff_res_e[1]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
597: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.gamma_e[1]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
598: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Je[1]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
599: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.J[1]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
600: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_diff[1]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
601: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.Tp[1]:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
602: dynamicMultiFluidHeatExchanger.ExchangerMultiFluids.dW1_conv[1]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
603: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_diff[1]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Diffusion thermal power exchanged on the liquid side for node i" type: Real [4]
604: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Tp1[1]:VARIABLE(min = 0.0 start = 500.0 unit = "K" nominal = 300.0 )  "Wall temperature in node i" type: Real [4]
605: dynamicMultiFluidHeatExchanger.ExchangerWall.Tp[1]:VARIABLE(min = 0.0 start = 290.03103270324897 unit = "K" nominal = 300.0 )  "Average wall temperature in section i" type: Real [4]
606: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpg[1]:VARIABLE(unit = "Pa" )  "Gravity pressure loss in node i" type: Real [5]
607: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.khi[1]:VARIABLE()  "Hydraulic pressure loss coefficient in node i" type: Real [5]
608: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dpf[1]:VARIABLE(unit = "Pa" )  "Friction pressure loss in node i" type: Real [5]
609: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
610: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
611: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
612: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
613: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].cp:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant pressure" type: Real [5]
614: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].h:VARIABLE(unit = "J/kg" )  "Specific enthalpy" type: Real [5]
615: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
616: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].pt:VARIABLE()  "Derivative of pressure wrt. temperature" type: Real [5]
617: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
618: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
619: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].rho:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real [5]
620: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real [5]
621: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.vsat2[1].P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Pressure" type: Real [5]
622: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lsat2[1].cv:VARIABLE(unit = "J/(kg.K)" )  "Specific heat capacity at constant volume" type: Real [5]
623: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 )  "Specific inner energy" type: Real [5]
624: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].duhp:VARIABLE(unit = "1" )  "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real [5]
625: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific heat capacity at constant presure" type: Real [5]
626: $cse12.duhp:VARIABLE(protected = true )  type: Real unreplaceable
627: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].ddph:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt. pressure at constant specific enthalpy" type: Real [5]
628: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 )  "Specific entropy" type: Real [5]
629: $cse12.duph:VARIABLE(protected = true )  type: Real unreplaceable
630: $cse12.ddph:VARIABLE(protected = true )  type: Real unreplaceable
631: $cse12.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
632: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hb[1]:VARIABLE(start = 1e5 unit = "J/kg" )  "Fluid specific enthalpy at the boundary of node i" type: Real [5]
633: $cse12.s:VARIABLE(protected = true )  type: Real unreplaceable
634: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Pb[1]:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 )  "Bounded fluid pressure in node i" type: Real [6]
635: $cse3:VARIABLE(protected = true )  type: Real unreplaceable
636: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[1]:VARIABLE(start = 71016.125 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
637: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.P[1]:VARIABLE(min = 0.0 start = 3e5 unit = "Pa" nominal = 1e5 )  "Fluid pressure in node i" type: Real [6]
638: $cse12.cp:VARIABLE(protected = true )  type: Real unreplaceable
639: $cse12.x:VARIABLE(protected = true )  type: Real unreplaceable
640: $cse12.u:VARIABLE(protected = true )  type: Real unreplaceable
641: $cse12.T:VARIABLE(protected = true )  type: Real unreplaceable
642: $cse12.d:VARIABLE(protected = true )  type: Real unreplaceable
643: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].ddhp:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt. specific enthalpy at constant pressure" type: Real [5]
644: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.xv2[1]:VARIABLE()  "Vapor mass fraction in hydraulic node i" type: Real [5]
645: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].x:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Vapor mass fraction" type: Real [5]
646: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro2[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [5]
647: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
648: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
649: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.cpl2[1]:VARIABLE(start = 4000.0 unit = "J/(kg.K)" nominal = 4000.0 )  "Specific heat capacity in hydraulic node i for the liquid" type: Real [5]
650: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.filo[1]:VARIABLE()  "Pressure loss coefficient for two-phase flow" type: Real [5]
651: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
652: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel2[1]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in hydraulic node i for the liquid" type: Real [5]
653: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdal[1]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the liquid" type: Real [5]
654: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.lambdav[1]:VARIABLE(start = 0.03 nominal = 0.03 )  "Friction pressure loss coefficient in node i for the vapor)" type: Real [5]
655: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rev2[1]:VARIABLE(start = 1000.0 unit = "1" nominal = 5e5 )  "Reynolds number in hydraulic node i for the vapor" type: Real [5]
656: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
657: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
658: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [5]
659: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.kl2[1]:VARIABLE(start = 0.6 unit = "W/(m.K)" nominal = 0.6 )  "Thermal conductivity in hydraulic node i for the liquid" type: Real [5]
660: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.re[1]:VARIABLE()  "Value of r(Q/gamma) for inlet of thermal node i" type: Real [4]
661: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.diff_res_e[1]:VARIABLE()  "Diffusion resistance at inlet of thermal node i" type: Real [4]
662: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.gamma_e[1]:VARIABLE(unit = "kg/s" )  "Diffusion conductance at inlet of thermal node i" type: Real [4]
663: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Je[1]:VARIABLE(unit = "W" )  "Thermal power diffusion from inlet of thermal node i" type: Real [4]
664: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.J[1]:VARIABLE(unit = "W" )  "Total thermal power diffusion of thermal node i" type: Real [4]
665: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hi[1]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 2e4 )  "Fluid heat exchange coefficient in node i" type: Real [4]
666: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.dW1_conv[1]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Convection thermal power exchanged on the liquid side for node i" type: Real [4]
667: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.heb[1]:VARIABLE(start = 0.0 unit = "W/(m2.K)" nominal = 5e5 )  "Fluid heat exchange coefficient for vaporization in thermal node i" type: Real [4]
668: dynamicMultiFluidHeatExchanger.ExchangerWall.dW1[1]:VARIABLE(start = 3e5 unit = "W" nominal = 3e5 )  "Power in section i of side 1" type: Real [4]
669: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Bo[1]:VARIABLE(start = 0.0 nominal = 4e-4 )  "Boiling number" type: Real [4]
670: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.E[1]:VARIABLE()  "Corrective term for hcl" type: Real [4]
671: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.S[1]:VARIABLE()  "Corrective term for nucleation removal" type: Real [4]
672: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.hcl[1]:VARIABLE(start = 2000.0 unit = "W/(m2.K)" nominal = 200.0 )  "Fluid heat exchange coefficient in node i for the liquid fraction" type: Real [4]
673: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.Rel1[1]:VARIABLE(start = 6e4 unit = "1" nominal = 5000.0 )  "Reynolds number in thermal node i for the liquid" type: Real [4]
674: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.mul1[1]:VARIABLE(min = 0.0 start = 2e-4 unit = "Pa.s" nominal = 2e-4 )  "Dynamic viscosity in thermal node i for the liquid" type: Real [4]
675: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.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 [4]
676: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.pro1[1].duph:VARIABLE(unit = "m3/kg" )  "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real [4]
677: $cse4.ddhp:VARIABLE(protected = true )  type: Real unreplaceable
678: $cse4.duph:VARIABLE(protected = true )  type: Real unreplaceable
679: $cse4.T:VARIABLE(protected = true )  type: Real unreplaceable
680: $cse4.cp:VARIABLE(protected = true )  type: Real unreplaceable
681: $cse4.x:VARIABLE(protected = true )  type: Real unreplaceable
682: $cse4.s:VARIABLE(protected = true )  type: Real unreplaceable
683: $cse4.ddph:VARIABLE(protected = true )  type: Real unreplaceable
684: $cse4.duhp:VARIABLE(protected = true )  type: Real unreplaceable
685: $cse4.d:VARIABLE(protected = true )  type: Real unreplaceable
686: $cse4.u:VARIABLE(protected = true )  type: Real unreplaceable
687: dynamicMultiFluidHeatExchanger.TwoPhaseFlowPipe.h[2]:VARIABLE(start = 71016.125 unit = "J/kg" nominal = 1e6 )  "Fluid specific enthalpy in node i" type: Real [6]
[/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 0.2613/4.271, allocations: 403.5 MB / 1.903 GB, free: 406.5 MB / 0.8262 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ThermoSysPro.Fluid.Examples.SimpleExamples.TestDynamicWaterSteamMultiFluidHeatExchanger could not be translated