Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0009824/0.0009824, allocations: 92.22 kB / 19.65 MB, free: 276 kB / 13.93 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001878/0.001878, allocations: 169 kB / 23.02 MB, free: 1.547 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.9436/0.9436, allocations: 177.1 MB / 203.4 MB, free: 5.648 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.6969/0.6969, allocations: 118.6 MB / 378.6 MB, free: 1.52 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|conductionElementHEX_twoPhase.A|conductionElementHEX_twoPhase.L|conductionElementHEX_twoPhase.M|conductionElementHEX_twoPhase.Q_flow|conductionElementHEX_twoPhase.Re_exp_cond|conductionElementHEX_twoPhase.Re_exp_evap|conductionElementHEX_twoPhase.T|conductionElementHEX_twoPhase.T_0|conductionElementHEX_twoPhase.T_e|conductionElementHEX_twoPhase.T_heatPort|conductionElementHEX_twoPhase.U|conductionElementHEX_twoPhase.U_liq|conductionElementHEX_twoPhase.U_liq_nom|conductionElementHEX_twoPhase.U_min|conductionElementHEX_twoPhase.U_tp|conductionElementHEX_twoPhase.U_tp_nom|conductionElementHEX_twoPhase.U_vap|conductionElementHEX_twoPhase.U_vap_nom|conductionElementHEX_twoPhase.V|conductionElementHEX_twoPhase.clip_p_out|conductionElementHEX_twoPhase.deltaE_system|conductionElementHEX_twoPhase.delta_x|der.conductionElementHEX_twoPhase.h.|conductionElementHEX_twoPhase.dp|conductionElementHEX_twoPhase.dr_corr|conductionElementHEX_twoPhase.h|conductionElementHEX_twoPhase.h_0|conductionElementHEX_twoPhase.h_bubble|conductionElementHEX_twoPhase.h_dew|conductionElementHEX_twoPhase.h_in|conductionElementHEX_twoPhase.h_in_norm|conductionElementHEX_twoPhase.h_out|conductionElementHEX_twoPhase.heatPort.Q_flow|conductionElementHEX_twoPhase.heatPort.T|conductionElementHEX_twoPhase.init|conductionElementHEX_twoPhase.initM_flow|der.conductionElementHEX_twoPhase.inlet.m_flow.|conductionElementHEX_twoPhase.inlet.m_flow|conductionElementHEX_twoPhase.inlet.r|conductionElementHEX_twoPhase.inlet.state.T|conductionElementHEX_twoPhase.inlet.state.d|conductionElementHEX_twoPhase.inlet.state.h|conductionElementHEX_twoPhase.inlet.state.p|conductionElementHEX_twoPhase.inlet.state.phase|conductionElementHEX_twoPhase.k|conductionElementHEX_twoPhase.m_acceleration_0|conductionElementHEX_twoPhase.m_flow|conductionElementHEX_twoPhase.m_flowStateSelect|conductionElementHEX_twoPhase.m_flow_0|conductionElementHEX_twoPhase.m_flow_assert|conductionElementHEX_twoPhase.m_flow_nom|conductionElementHEX_twoPhase.nCellsParallel|conductionElementHEX_twoPhase.outlet.m_flow|conductionElementHEX_twoPhase.outlet.r|conductionElementHEX_twoPhase.outlet.state.T|conductionElementHEX_twoPhase.outlet.state.d|conductionElementHEX_twoPhase.outlet.state.h|conductionElementHEX_twoPhase.outlet.state.p|conductionElementHEX_twoPhase.outlet.state.phase|conductionElementHEX_twoPhase.p_in|conductionElementHEX_twoPhase.p_min|conductionElementHEX_twoPhase.p_out|conductionElementHEX_twoPhase.rho|conductionElementHEX_twoPhase.rho_min|conductionElementHEX_twoPhase.state.T|conductionElementHEX_twoPhase.state.d|conductionElementHEX_twoPhase.state.h|conductionElementHEX_twoPhase.state.p|conductionElementHEX_twoPhase.state.phase|conductionElementHEX_twoPhase.x|conductionElementHEX_twoPhase1.A|conductionElementHEX_twoPhase1.L|conductionElementHEX_twoPhase1.M|conductionElementHEX_twoPhase1.Q_flow|conductionElementHEX_twoPhase1.Re_exp_cond|conductionElementHEX_twoPhase1.Re_exp_evap|conductionElementHEX_twoPhase1.T|conductionElementHEX_twoPhase1.T_0|conductionElementHEX_twoPhase1.T_e|conductionElementHEX_twoPhase1.T_heatPort|conductionElementHEX_twoPhase1.U|conductionElementHEX_twoPhase1.U_liq|conductionElementHEX_twoPhase1.U_liq_nom|conductionElementHEX_twoPhase1.U_min|conductionElementHEX_twoPhase1.U_tp|conductionElementHEX_twoPhase1.U_tp_nom|conductionElementHEX_twoPhase1.U_vap|conductionElementHEX_twoPhase1.U_vap_nom|conductionElementHEX_twoPhase1.V|conductionElementHEX_twoPhase1.clip_p_out|conductionElementHEX_twoPhase1.deltaE_system|conductionElementHEX_twoPhase1.delta_x|der.conductionElementHEX_twoPhase1.h.|conductionElementHEX_twoPhase1.dp|conductionElementHEX_twoPhase1.dr_corr|conductionElementHEX_twoPhase1.h|conductionElementHEX_twoPhase1.h_0|conductionElementHEX_twoPhase1.h_bubble|conductionElementHEX_twoPhase1.h_dew|conductionElementHEX_twoPhase1.h_in|conductionElementHEX_twoPhase1.h_in_norm|conductionElementHEX_twoPhase1.h_out|conductionElementHEX_twoPhase1.heatPort.Q_flow|conductionElementHEX_twoPhase1.heatPort.T|conductionElementHEX_twoPhase1.init|conductionElementHEX_twoPhase1.initM_flow|der.conductionElementHEX_twoPhase1.inlet.m_flow.|conductionElementHEX_twoPhase1.inlet.m_flow|conductionElementHEX_twoPhase1.inlet.r|conductionElementHEX_twoPhase1.inlet.state.T|conductionElementHEX_twoPhase1.inlet.state.d|conductionElementHEX_twoPhase1.inlet.state.h|conductionElementHEX_twoPhase1.inlet.state.p|conductionElementHEX_twoPhase1.inlet.state.phase|conductionElementHEX_twoPhase1.k|conductionElementHEX_twoPhase1.m_acceleration_0|conductionElementHEX_twoPhase1.m_flow|conductionElementHEX_twoPhase1.m_flowStateSelect|conductionElementH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m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.d|source1.outlet.state.h|source1.outlet.state.p|source1.outlet.state.phase|source1.p0|source1.p0_par|source2.L|source2.T0|source2.T0_par|source2.h0|source2.h0_par|source2.h0_var|der.source2.outlet.m_flow.|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.d|source2.outlet.state.h|source2.outlet.state.p|source2.outlet.state.phase|source2.p0|source2.p0_par|source3.L|source3.T0|source3.T0_par|source3.h0|source3.h0_par|der.source3.outlet.m_flow.|source3.outlet.m_flow|source3.outlet.r|source3.outlet.state.T|source3.outlet.state.d|source3.outlet.state.h|source3.outlet.state.p|source3.outlet.state.phase|source3.p0|source3.p0_par|trapezoid.T_falling|trapezoid.T_rising|trapezoid.T_start|trapezoid.T_width|trapezoid.amplitude|trapezoid.count|trapezoid.falling|trapezoid.nperiod|trapezoid.offset|trapezoid.period|trapezoid.rising|trapezoid.startTime|trapezoid.width|trapezoid.y|trapezoid2.T_falling|trapezoid2.T_rising|trapezoid2.T_start|trapezoid2.T_width|trapezoid2.amplitude|trapezoid2.count|trapezoid2.falling|trapezoid2.nperiod|trapezoid2.offset|trapezoid2.period|trapezoid2.rising|trapezoid2.startTime|trapezoid2.width|trapezoid2.y|volume.A|volume.L|volume.M|volume.Q_flow|volume.T_heatPort|volume.T_start|volume.U|volume.U_med|volume.V|volume.V_par|volume.W_v|volume.d|volume.density_derp_h|volume.density_derp_h_set|der.volume.M.|der.volume.U_med.|der.volume.m_flow_in.|der.volume.m_flow_out.|volume.h_in|volume.h_out|volume.h_start|volume.inlet.m_flow|volume.inlet.r|volume.inlet.state.T|volume.inlet.state.d|volume.inlet.state.h|volume.inlet.state.p|volume.inlet.state.phase|volume.k_volume_damping|volume.m_flow_assert|volume.m_flow_in|volume.m_flow_out|volume.medium.MM|volume.medium.R_s|volume.medium.T|volume.medium.T_degC|volume.medium.X.[0-9,]+.|volume.medium.d|der.volume.medium.h.|der.volume.medium.p.|der.volume.medium.u.|volume.medium.h|volume.medium.p|volume.medium.p_bar|volume.medium.phase|volume.medium.preferredMediumStates|volume.medium.quality|volume.medium.sat.Tsat|volume.medium.sat.psat|volume.medium.standardOrderComponents|volume.medium.state.T|volume.medium.state.d|der.volume.medium.state.d.|volume.medium.state.h|volume.medium.state.p|volume.medium.state.phase|volume.medium.u|volume.outlet.m_flow|volume.outlet.r|volume.outlet.state.T|volume.outlet.state.d|volume.outlet.state.h|volume.outlet.state.p|volume.outlet.state.phase|volume.p_in|volume.p_start|volume.r|volume.r_damping|volume.r_in|volume.r_out|volume.state_in.T|volume.state_in.d|volume.state_in.h|volume.state_in.p|volume.state_in.phase|volume.state_out.T|volume.state_out.d|volume.state_out.h|volume.state_out.p|volume.state_out.phase|volume1.A|volume1.L|volume1.M|volume1.Q_flow|volume1.T_heatPort|volume1.T_start|volume1.U|volume1.U_med|volume1.V|volume1.V_par|volume1.W_v|volume1.d|volume1.density_derp_h|volume1.density_derp_h_set|der.volume1.M.|der.volume1.U_med.|der.volume1.m_flow_in.|der.volume1.m_flow_out.|volume1.h_in|volume1.h_out|volume1.h_start|volume1.heatPort.Q_flow|volume1.heatPort.T|volume1.inlet.m_flow|volume1.inlet.r|volume1.inlet.state.T|volume1.inlet.state.d|volume1.inlet.state.h|volume1.inlet.state.p|volume1.inlet.state.phase|volume1.k_volume_damping|volume1.m_flow_assert|volume1.m_flow_in|volume1.m_flow_out|volume1.medium.MM|volume1.medium.R_s|volume1.medium.T|volume1.medium.T_degC|volume1.medium.X.[0-9,]+.|volume1.medium.d|der.volume1.medium.h.|der.volume1.medium.p.|der.volume1.medium.u.|volume1.medium.h|volume1.medium.p|volume1.medium.p_bar|volume1.medium.phase|volume1.medium.preferredMediumStates|volume1.medium.quality|volume1.medium.sat.Tsat|volume1.medium.sat.psat|volume1.medium.standardOrderComponents|volume1.medium.state.T|volume1.medium.state.d|der.volume1.medium.state.d.|volume1.medium.state.h|volume1.medium.state.p|volume1.medium.state.phase|volume1.medium.u|volume1.outlet.m_flow|volume1.outlet.r|volume1.outlet.state.T|volume1.outlet.state.d|volume1.outlet.state.h|volume1.outlet.state.p|volume1.outlet.state.phase|volume1.p_in|volume1.p_start|volume1.r|volume1.r_damping|volume1.r_in|volume1.r_out|volume1.state_in.T|volume1.state_in.d|volume1.state_in.h|volume1.state_in.p|volume1.state_in.phase|volume1.state_out.T|volume1.state_out.d|volume1.state_out.h|volume1.state_out.p|volume1.state_out.phase",fileNamePrefix="ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 2.154e-06/2.154e-06, allocations: 0 / 483.7 MB, free: 8.156 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 3.519e-05/3.734e-05, allocations: 2.312 kB / 483.7 MB, free: 8.152 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase): time 0.0321/0.03213, allocations: 22.55 MB / 0.4944 GB, free: 9.426 MB / 426.7 MB
Notification: Performance of NFInst.instExpressions: time 0.02147/0.0536, allocations: 17.1 MB / 0.5111 GB, free: 8.93 MB / 442.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.002939/0.05654, allocations: 126.8 kB / 0.5112 GB, free: 8.805 MB / 442.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.001508/0.05805, allocations: 0.5304 MB / 0.5117 GB, free: 8.27 MB / 442.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.01055/0.0686, allocations: 3.792 MB / 0.5154 GB, free: 4.457 MB / 442.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.003585/0.07219, allocations: 1.184 MB / 0.5166 GB, free: 3.27 MB / 442.7 MB
Notification: Performance of NFFlatten.flatten: time 0.005796/0.07798, allocations: 4.627 MB / 0.5211 GB, free: 14.62 MB / 458.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.001052/0.07904, allocations: 424.3 kB / 0.5215 GB, free: 14.16 MB / 458.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.004609/0.08365, allocations: 2.412 MB / 0.5238 GB, free: 11.75 MB / 458.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.002082/0.08573, allocations: 1.223 MB / 0.525 GB, free: 10.52 MB / 458.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.0005511/0.08628, allocations: 207.9 kB / 0.5252 GB, free: 10.32 MB / 458.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.009505/0.09578, allocations: 5.941 MB / 0.531 GB, free: 4.363 MB / 458.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0006633/0.09645, allocations: 0.5481 MB / 0.5316 GB, free: 3.812 MB / 458.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.001826/0.09827, allocations: 1.005 MB / 0.5326 GB, free: 2.805 MB / 458.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.01513/0.1134, allocations: 7.262 MB / 0.5397 GB, free: 11.53 MB / 474.7 MB
Notification: Performance of FrontEnd - DAE generated: time 7.304e-06/0.1134, allocations: 0 / 0.5397 GB, free: 11.53 MB / 474.7 MB
Notification: Performance of FrontEnd: time 1.664e-06/0.1134, allocations: 0 / 0.5397 GB, free: 11.53 MB / 474.7 MB
Notification: Performance of Transformations before backend: time 9.475e-05/0.1135, allocations: 0 / 0.5397 GB, free: 11.53 MB / 474.7 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 520
 * Number of variables: 520
Notification: Performance of Generate backend data structure: time 0.00665/0.1202, allocations: 3.538 MB / 0.5431 GB, free: 7.91 MB / 474.7 MB
Notification: Performance of prepare preOptimizeDAE: time 5.204e-05/0.1202, allocations: 12.03 kB / 0.5431 GB, free: 7.898 MB / 474.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001941/0.1221, allocations: 0.9534 MB / 0.544 GB, free: 6.941 MB / 474.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.002416/0.1246, allocations: 1.69 MB / 0.5457 GB, free: 5.164 MB / 474.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 9.739e-05/0.1247, allocations: 139.6 kB / 0.5458 GB, free: 5.027 MB / 474.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0002159/0.1249, allocations: 199.9 kB / 0.546 GB, free: 4.832 MB / 474.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002454/0.1273, allocations: 2.056 MB / 0.548 GB, free: 2.543 MB / 474.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 2.96e-05/0.1274, allocations: 4 kB / 0.548 GB, free: 2.539 MB / 474.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001126/0.1275, allocations: 91.86 kB / 0.5481 GB, free: 2.449 MB / 474.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.903e-05/0.1275, allocations: 67.97 kB / 0.5482 GB, free: 2.383 MB / 474.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001436/0.129, allocations: 0.8819 MB / 0.549 GB, free: 1.5 MB / 474.7 MB
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 0.008313/0.1373, allocations: 8.049 MB / 0.5569 GB, free: 9.242 MB / 490.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.001971/0.1392, allocations: 0.9972 MB / 0.5579 GB, free: 8.227 MB / 490.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0006137/0.1399, allocations: 472.2 kB / 0.5583 GB, free: 7.762 MB / 490.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.001078/0.1409, allocations: 0.5673 MB / 0.5589 GB, free: 7.191 MB / 490.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.001115/0.142, allocations: 1.081 MB / 0.5599 GB, free: 6.008 MB / 490.7 MB
Notification: Performance of pre-optimization done (n=221): time 4.208e-06/0.1421, allocations: 0 / 0.5599 GB, free: 6.008 MB / 490.7 MB
Notification: Performance of matching and sorting (n=229): time 0.01058/0.1526, allocations: 4.848 MB / 0.5647 GB, free: 1.047 MB / 490.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 9.395e-05/0.1527, allocations: 158.1 kB / 0.5648 GB, free: 0.8594 MB / 490.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001454/0.1542, allocations: 1.464 MB / 0.5663 GB, free: 15.35 MB / 0.4948 GB
Notification: Performance of collectPreVariables (initialization): time 0.0001061/0.1543, allocations: 61.7 kB / 0.5663 GB, free: 15.28 MB / 0.4948 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0007779/0.1551, allocations: 1.102 MB / 0.5674 GB, free: 14.17 MB / 0.4948 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0006187/0.1557, allocations: 0.7822 MB / 0.5682 GB, free: 13.38 MB / 0.4948 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0004662/0.1561, allocations: 385.8 kB / 0.5685 GB, free: 13 MB / 0.4948 GB
Notification: Performance of setup shared object (initialization): time 0.000163/0.1563, allocations: 488.7 kB / 0.569 GB, free: 12.52 MB / 0.4948 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0006856/0.157, allocations: 415.4 kB / 0.5694 GB, free: 12.09 MB / 0.4948 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0008473/0.1578, allocations: 0.8789 MB / 0.5702 GB, free: 11.04 MB / 0.4948 GB
Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: conductionElementHEX_twoPhase1.deltaE_system = $START.conductionElementHEX_twoPhase1.deltaE_system (0.0 = $START.conductionElementHEX_twoPhase1.deltaE_system)
Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: conductionElementHEX_twoPhase.deltaE_system = $START.conductionElementHEX_twoPhase.deltaE_system (0.0 = $START.conductionElementHEX_twoPhase.deltaE_system)
Notification: Performance of analyzeInitialSystem (initialization): time 0.001849/0.1597, allocations: 1.332 MB / 0.5715 GB, free: 9.57 MB / 0.4948 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 8.806e-06/0.1597, allocations: 4 kB / 0.5715 GB, free: 9.566 MB / 0.4948 GB
Notification: Performance of matching and sorting (n=283) (initialization): time 0.0027/0.1624, allocations: 1.934 MB / 0.5734 GB, free: 7.566 MB / 0.4948 GB
Notification: Performance of prepare postOptimizeDAE: time 6.336e-05/0.1625, allocations: 71.39 kB / 0.5735 GB, free: 7.484 MB / 0.4948 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.562e-05/0.1625, allocations: 8.5 kB / 0.5735 GB, free: 7.477 MB / 0.4948 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.004517/0.167, allocations: 0.6374 MB / 0.5741 GB, free: 6.805 MB / 0.4948 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0008901/0.1679, allocations: 367.5 kB / 0.5745 GB, free: 6.445 MB / 0.4948 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.005815/0.1737, allocations: 12.4 MB / 0.5866 GB, free: 9.246 MB / 0.5105 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001198/0.1749, allocations: 80.11 kB / 0.5867 GB, free: 9.168 MB / 0.5105 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001431/0.175, allocations: 79.97 kB / 0.5867 GB, free: 9.09 MB / 0.5105 GB
Warning: The initial conditions are over specified. The following 2 initial equations are redundant, so they are removed from the initialization system:
         conductionElementHEX_twoPhase1.deltaE_system = $START.conductionElementHEX_twoPhase1.deltaE_system
         conductionElementHEX_twoPhase.deltaE_system = $START.conductionElementHEX_twoPhase.deltaE_system.
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 32
 * Number of states: 0 ()
 * Number of discrete variables: 28 (volume1.medium.phase,flowResistance2.outlet.state.phase,source3.outlet.state.phase,mCV3.outlet.state.phase,volume1.inlet.state.phase,trapezoid.count,$PRE.trapezoid.count,trapezoid.T_start,$PRE.trapezoid.T_start,source1.outlet.state.phase,mCV1.outlet.state.phase,conductionElementHEX_twoPhase1.state.phase,conductionElementHEX_twoPhase1.outlet.state.phase,$whenCondition2,volume.medium.phase,trapezoid2.count,$PRE.trapezoid2.count,trapezoid2.T_start,$PRE.trapezoid2.T_start,flowResistance.outlet.state.phase,source2.outlet.state.phase,mCV2.outlet.state.phase,volume.inlet.state.phase,source.outlet.state.phase,mCV.outlet.state.phase,conductionElementHEX_twoPhase.state.phase,conductionElementHEX_twoPhase.outlet.state.phase,$whenCondition1)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (199):
 * Single equations (assignments): 173
 * Array equations: 0
 * Algorithm blocks: 2
 * Record equations: 16
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 8
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 6 systems
   {(1,4,100.0%), (1,2,100.0%), (1,2,100.0%), (1,4,100.0%), (1,2,100.0%), (1,2,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 2 systems
   {(1,1), (1,1)}
Notification: Performance of prepare postOptimizeDAE: time 0.0006126/0.1757, allocations: 284 kB / 0.587 GB, free: 8.805 MB / 0.5105 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0003523/0.176, allocations: 298.4 kB / 0.5873 GB, free: 8.512 MB / 0.5105 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003102/0.1791, allocations: 2.458 MB / 0.5897 GB, free: 6.023 MB / 0.5105 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.00224/0.1813, allocations: 1.804 MB / 0.5915 GB, free: 4.176 MB / 0.5105 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 1.869e-05/0.1814, allocations: 7.938 kB / 0.5915 GB, free: 4.168 MB / 0.5105 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.87e-05/0.1814, allocations: 15.95 kB / 0.5915 GB, free: 4.152 MB / 0.5105 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.006196/0.1876, allocations: 4.82 MB / 0.5962 GB, free: 15.17 MB / 0.5261 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 9.978e-06/0.1876, allocations: 4 kB / 0.5962 GB, free: 15.16 MB / 0.5261 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0009442/0.1885, allocations: 423.9 kB / 0.5966 GB, free: 14.75 MB / 0.5261 GB
Notification: Performance of postOpt tearingSystem (simulation): time 0.001687/0.1902, allocations: 0.5937 MB / 0.5972 GB, free: 14.11 MB / 0.5261 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.0001784/0.1904, allocations: 71.95 kB / 0.5972 GB, free: 14.04 MB / 0.5261 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.006952/0.1974, allocations: 14.1 MB / 0.611 GB, free: 15.08 MB / 0.5417 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 3.647e-06/0.1974, allocations: 4 kB / 0.611 GB, free: 15.08 MB / 0.5417 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.005226/0.2026, allocations: 3.172 MB / 0.6141 GB, free: 11.71 MB / 0.5417 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.001101/0.2037, allocations: 437.8 kB / 0.6145 GB, free: 11.28 MB / 0.5417 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.000206/0.2039, allocations: 63.89 kB / 0.6146 GB, free: 11.22 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0006788/0.2046, allocations: 87.94 kB / 0.6147 GB, free: 11.13 MB / 0.5417 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0003861/0.205, allocations: 205.8 kB / 0.6149 GB, free: 10.93 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0001208/0.2051, allocations: 87.95 kB / 0.615 GB, free: 10.85 MB / 0.5417 GB
Notification: Performance of sorting global known variables: time 0.001135/0.2062, allocations: 0.8936 MB / 0.6158 GB, free: 9.934 MB / 0.5417 GB
Notification: Performance of sort global known variables: time 2.41e-07/0.2062, allocations: 0 / 0.6158 GB, free: 9.934 MB / 0.5417 GB
Notification: Performance of remove unused functions: time 0.004237/0.2104, allocations: 1.007 MB / 0.6168 GB, free: 8.926 MB / 0.5417 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 18
 * Number of states: 16 (conductionElementHEX_twoPhase.h,mCV.dp_int,volume.M,volume.U_med,mCV2.inlet.m_flow,mCV2.dp_int,flowResistance.inlet.m_flow,flowResistance1.inlet.m_flow,conductionElementHEX_twoPhase1.h,mCV1.dp_int,volume1.M,volume1.U_med,mCV3.inlet.m_flow,mCV3.dp_int,flowResistance2.inlet.m_flow,flowResistance3.inlet.m_flow)
 * Number of discrete variables: 38 (conductionElementHEX_twoPhase.state.phase,conductionElementHEX_twoPhase.outlet.state.phase,mCV.outlet.state.phase,flowResistance.outlet.state.phase,source.outlet.state.phase,mCV2.outlet.state.phase,volume.inlet.state.phase,source2.outlet.state.phase,$cse17.phase,$cse21.phase,$cse22.phase,$cse23.phase,$cse24,$cse28.phase,$cse29.phase,$cse30.phase,$cse31.phase,$whenCondition1,trapezoid2.T_start,trapezoid2.count,conductionElementHEX_twoPhase1.state.phase,conductionElementHEX_twoPhase1.outlet.state.phase,mCV1.outlet.state.phase,flowResistance2.outlet.state.phase,mCV3.outlet.state.phase,volume1.inlet.state.phase,$cse1.phase,$cse5.phase,$cse7.phase,$cse8,$cse12.phase,$cse14.phase,$cse15.phase,$whenCondition2,trapezoid.T_start,trapezoid.count,source3.outlet.state.phase,source1.outlet.state.phase)
 * Number of discrete states: 2 (trapezoid.count,trapezoid2.count)
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (235):
 * Single equations (assignments): 207
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 14
 * When equations: 4
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 10
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 6 systems
   {(1,4,100.0%), (1,2,100.0%), (1,2,100.0%), (1,4,100.0%), (1,2,100.0%), (1,2,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 4 systems
   {(1,1), (1,3), (1,1), (1,3)}
Notification: Performance of Backend phase and start with SimCode phase: time 0.009426/0.2199, allocations: 3.741 MB / 0.6205 GB, free: 5.176 MB / 0.5417 GB
Notification: Performance of simCode: created initialization part: time 0.003788/0.2237, allocations: 3.22 MB / 0.6236 GB, free: 1.699 MB / 0.5417 GB
Notification: Performance of simCode: created event and clocks part: time 8.025e-06/0.2237, allocations: 3.938 kB / 0.6236 GB, free: 1.695 MB / 0.5417 GB
Notification: Performance of simCode: created simulation system equations: time 0.001795/0.2255, allocations: 1.953 MB / 0.6255 GB, free: 15.63 MB / 0.5573 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.003518/0.229, allocations: 1.253 MB / 0.6267 GB, free: 14.41 MB / 0.5573 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.007744/0.2367, allocations: 5.193 MB / 0.6318 GB, free: 9.086 MB / 0.5573 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0004816/0.2372, allocations: 0.4936 MB / 0.6323 GB, free: 8.566 MB / 0.5573 GB
Notification: Performance of simCode: alias equations: time 0.001418/0.2386, allocations: 461 kB / 0.6327 GB, free: 8.113 MB / 0.5573 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0005129/0.2391, allocations: 220.4 kB / 0.6329 GB, free: 7.898 MB / 0.5573 GB
Notification: Performance of SimCode: time 2.314e-06/0.2391, allocations: 0 / 0.6329 GB, free: 7.898 MB / 0.5573 GB
Notification: Performance of Templates: time 0.2871/0.5262, allocations: 63.75 MB / 0.6952 GB, free: 97.21 MB / 0.5573 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe ; mkfifo ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe >> ../files/ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.sim & ./ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase -abortSlowSimulation -alarm=240  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable conductionElementHEX_twoPhase.Re_exp_cond in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable conductionElementHEX_twoPhase.Re_exp_cond from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable conductionElementHEX_twoPhase.Re_exp_evap in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable conductionElementHEX_twoPhase.Re_exp_evap from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable conductionElementHEX_twoPhase.U_min in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable conductionElementHEX_twoPhase.U_min from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable conductionElementHEX_twoPhase1.Re_exp_cond in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable conductionElementHEX_twoPhase1.Re_exp_cond from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable conductionElementHEX_twoPhase1.Re_exp_evap in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable conductionElementHEX_twoPhase1.Re_exp_evap from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable conductionElementHEX_twoPhase1.U_min in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable conductionElementHEX_twoPhase1.U_min from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable mCV.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable mCV.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable mCV1.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable mCV1.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable mCV2.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable mCV2.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable mCV3.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable mCV3.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable volume.der(m_flow_in) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable volume.der(m_flow_in) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable volume.der(m_flow_out) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable volume.der(m_flow_out) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable volume.medium.state.der(d) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable volume.medium.state.der(d) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable volume1.der(m_flow_in) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable volume1.der(m_flow_in) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable volume1.der(m_flow_out) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable volume1.der(m_flow_out) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
Error: Could not read variable volume1.medium.state.der(d) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat.
Warning: Get data of variable volume1.medium.state.der(d) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,NonlinearSystems.simulation[1].Calls,NonlinearSystems.simulation[1].Iterations,NonlinearSystems.simulation[1].Jacobians,NonlinearSystems.simulation[1].Residues,NonlinearSystems.simulation[2].Calls,NonlinearSystems.simulation[2].Iterations,NonlinearSystems.simulation[2].Jacobians,NonlinearSystems.simulation[2].Residues,Time,conductionElementHEX_twoPhase.A,conductionElementHEX_twoPhase.L,conductionElementHEX_twoPhase.M,conductionElementHEX_twoPhase.Q_flow,conductionElementHEX_twoPhase.Re_exp_cond,conductionElementHEX_twoPhase.Re_exp_evap,conductionElementHEX_twoPhase.T,conductionElementHEX_twoPhase.T_0,conductionElementHEX_twoPhase.T_e,conductionElementHEX_twoPhase.T_heatPort,conductionElementHEX_twoPhase.U,conductionElementHEX_twoPhase.U_liq,conductionElementHEX_twoPhase.U_liq_nom,conductionElementHEX_twoPhase.U_min,conductionElementHEX_twoPhase.U_tp,conductionElementHEX_twoPhase.U_tp_nom,conductionElementHEX_twoPhase.U_vap,conductionElementHEX_twoPhase.U_vap_nom,conductionElementHEX_twoPhase.V,conductionElementHEX_twoPhase.clip_p_out,conductionElementHEX_twoPhase.deltaE_system,conductionElementHEX_twoPhase.delta_x,der(conductionElementHEX_twoPhase.h),conductionElementHEX_twoPhase.dp,conductionElementHEX_twoPhase.dr_corr,conductionElementHEX_twoPhase.h,conductionElementHEX_twoPhase.h_0,conductionElementHEX_twoPhase.h_bubble,conductionElementHEX_twoPhase.h_dew,conductionElementHEX_twoPhase.h_in,conductionElementHEX_twoPhase.h_in_norm,conductionElementHEX_twoPhase.h_out,conductionElementHEX_twoPhase.heatPort.Q_flow,conductionElementHEX_twoPhase.heatPort.T,conductionElementHEX_twoPhase.init,conductionElementHEX_twoPhase.initM_flow,der(conductionElementHEX_twoPhase.inlet.m_flow),conductionElementHEX_twoPhase.inlet.m_flow,conductionElementHEX_twoPhase.inlet.r,conductionElementHEX_twoPhase.inlet.state.T,conductionElementHEX_twoPhase.inlet.state.d,conductionElementHEX_twoPhase.inlet.state.h,conductionElementHEX_twoPhase.inlet.state.p,conductionElementHEX_twoPhase.inlet.state.phase,conductionElementHEX_twoPhase.k,conductionElementHEX_twoPhase.m_acceleration_0,conductionElementHEX_twoPhase.m_flow,conductionElementHEX_twoPhase.m_flowStateSelect,conductionElementHEX_twoPhase.m_flow_0,conductionElementHEX_twoPhase.m_flow_assert,conductionElementHEX_twoPhase.m_flow_nom,conductionElementHEX_twoPhase.nCellsParallel,conductionElementHEX_twoPhase.outlet.m_flow,conductionElementHEX_twoPhase.outlet.r,conductionElementHEX_twoPhase.outlet.state.T,conductionElementHEX_twoPhase.outlet.state.d,conductionElementHEX_twoPhase.outlet.state.h,conductionElementHEX_twoPhase.outlet.state.p,conductionElementHEX_twoPhase.outlet.state.phase,conductionElementHEX_twoPhase.p_in,conductionElementHEX_twoPhase.p_min,conductionElementHEX_twoPhase.p_out,conductionElementHEX_twoPhase.rho,conductionElementHEX_twoPhase.rho_min,conductionElementHEX_twoPhase.state.T,conductionElementHEX_twoPhase.state.d,conductionElementHEX_twoPhase.state.h,conductionElementHEX_twoPhase.state.p,conductionElementHEX_twoPhase.state.phase,conductionElementHEX_twoPhase.x,conductionElementHEX_twoPhase1.A,conductionElementHEX_twoPhase1.L,conductionElementHEX_twoPhase1.M,conductionElementHEX_twoPhase1.Q_flow,conductionElementHEX_twoPhase1.Re_exp_cond,conductionElementHEX_twoPhase1.Re_exp_evap,conductionElementHEX_twoPhase1.T,conductionElementHEX_twoPhase1.T_0,conductionElementHEX_twoPhase1.T_e,conductionElementHEX_twoPhase1.T_heatPort,conductionElementHEX_twoPhase1.U,conductionElementHEX_twoPhase1.U_liq,conductionElementHEX_twoPhase1.U_liq_nom,conductionElementHEX_twoPhase1.U_min,conductionElementHEX_twoPhase1.U_tp,conductionElementHEX_twoPhase1.U_tp_nom,conductionElementHEX_twoPhase1.U_vap,conductionElementHEX_twoPhase1.U_vap_nom,conductionElementHEX_twoPhase1.V,conductionElementHEX_twoPhase1.clip_p_out,conductionElementHEX_twoPhase1.deltaE_system,conductionElementHEX_twoPhase1.delta_x,der(conductionElementHEX_twoPhase1.h),conductionElementHEX_twoPhase1.dp,conductionElementHEX_twoPhase1.dr_corr,conductionElementHEX_twoPhase1.h,conductionElementHEX_twoPhase1.h_0,conductionElementHEX_twoPhase1.h_bubble,conductionElementHEX_twoPhase1.h_dew,conductionElementHEX_twoPhase1.h_in,conductionElementHEX_twoPhase1.h_in_norm,conductionElementHEX_twoPhase1.h_out,conductionElementHEX_twoPhase1.heatPort.Q_flow,conductionElementHEX_twoPhase1.heatPort.T,conductionElementHEX_twoPhase1.init,conductionElementHEX_twoPhase1.initM_flow,der(conductionElementHEX_twoPhase1.inlet.m_flow),conductionElementHEX_twoPhase1.inlet.m_flow,conductionElementHEX_twoPhase1.inlet.r,conductionElementHEX_twoPhase1.inlet.state.T,conductionElementHEX_twoPhase1.inlet.state.d,conductionElementHEX_twoPhase1.inlet.state.h,conductionElementHEX_twoPhase1.inlet.state.p,conductionElementHEX_twoPhase1.inlet.state.phase,conductionElementHEX_twoPhase1.k,conductionElementHEX_twoPhase1.m_acceleration_0,conductionElementHEX_twoPhase1.m_flow,conductionElementHEX_twoPhase1.m_flowStateSelect,conductionElemen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ce.T0_par,source.h0,source.h0_par,source.h0_var,der(source.outlet.m_flow),source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.d,source.outlet.state.h,source.outlet.state.p,source.outlet.state.phase,source.p0,source.p0_par,source1.L,source1.T0,source1.T0_par,source1.h0,source1.h0_par,der(source1.outlet.m_flow),source1.outlet.m_flow,source1.outlet.r,source1.outlet.state.T,source1.outlet.state.d,source1.outlet.state.h,source1.outlet.state.p,source1.outlet.state.phase,source1.p0,source1.p0_par,source2.L,source2.T0,source2.T0_par,source2.h0,source2.h0_par,source2.h0_var,der(source2.outlet.m_flow),source2.outlet.m_flow,source2.outlet.r,source2.outlet.state.T,source2.outlet.state.d,source2.outlet.state.h,source2.outlet.state.p,source2.outlet.state.phase,source2.p0,source2.p0_par,source3.L,source3.T0,source3.T0_par,source3.h0,source3.h0_par,der(source3.outlet.m_flow),source3.outlet.m_flow,source3.outlet.r,source3.outlet.state.T,source3.outlet.state.d,source3.outlet.state.h,source3.outlet.state.p,source3.outlet.state.phase,source3.p0,source3.p0_par,trapezoid.T_falling,trapezoid.T_rising,trapezoid.T_start,trapezoid.T_width,trapezoid.amplitude,trapezoid.count,trapezoid.falling,trapezoid.nperiod,trapezoid.offset,trapezoid.period,trapezoid.rising,trapezoid.startTime,trapezoid.width,trapezoid.y,trapezoid2.T_falling,trapezoid2.T_rising,trapezoid2.T_start,trapezoid2.T_width,trapezoid2.amplitude,trapezoid2.count,trapezoid2.falling,trapezoid2.nperiod,trapezoid2.offset,trapezoid2.period,trapezoid2.rising,trapezoid2.startTime,trapezoid2.width,trapezoid2.y,volume.A,volume.L,volume.M,volume.Q_flow,volume.T_heatPort,volume.T_start,volume.U,volume.U_med,volume.V,volume.V_par,volume.W_v,volume.d,volume.density_derp_h,volume.density_derp_h_set,der(volume.M),der(volume.U_med),der(volume.m_flow_in),der(volume.m_flow_out),volume.h_in,volume.h_out,volume.h_start,volume.inlet.m_flow,volume.inlet.r,volume.inlet.state.T,volume.inlet.state.d,volume.inlet.state.h,volume.inlet.state.p,volume.inlet.state.phase,volume.k_volume_damping,volume.m_flow_assert,volume.m_flow_in,volume.m_flow_out,volume.medium.MM,volume.medium.R_s,volume.medium.T,volume.medium.T_degC,volume.medium.X[1],volume.medium.d,der(volume.medium.h),der(volume.medium.p),der(volume.medium.u),volume.medium.h,volume.medium.p,volume.medium.p_bar,volume.medium.phase,volume.medium.preferredMediumStates,volume.medium.quality,volume.medium.sat.Tsat,volume.medium.sat.psat,volume.medium.standardOrderComponents,volume.medium.state.T,volume.medium.state.d,der(volume.medium.state.d),volume.medium.state.h,volume.medium.state.p,volume.medium.state.phase,volume.medium.u,volume.outlet.m_flow,volume.outlet.r,volume.outlet.state.T,volume.outlet.state.d,volume.outlet.state.h,volume.outlet.state.p,volume.outlet.state.phase,volume.p_in,volume.p_start,volume.r,volume.r_damping,volume.r_in,volume.r_out,volume.state_in.T,volume.state_in.d,volume.state_in.h,volume.state_in.p,volume.state_in.phase,volume.state_out.T,volume.state_out.d,volume.state_out.h,volume.state_out.p,volume.state_out.phase,volume1.A,volume1.L,volume1.M,volume1.Q_flow,volume1.T_heatPort,volume1.T_start,volume1.U,volume1.U_med,volume1.V,volume1.V_par,volume1.W_v,volume1.d,volume1.density_derp_h,volume1.density_derp_h_set,der(volume1.M),der(volume1.U_med),der(volume1.m_flow_in),der(volume1.m_flow_out),volume1.h_in,volume1.h_out,volume1.h_start,volume1.heatPort.Q_flow,volume1.heatPort.T,volume1.inlet.m_flow,volume1.inlet.r,volume1.inlet.state.T,volume1.inlet.state.d,volume1.inlet.state.h,volume1.inlet.state.p,volume1.inlet.state.phase,volume1.k_volume_damping,volume1.m_flow_assert,volume1.m_flow_in,volume1.m_flow_out,volume1.medium.MM,volume1.medium.R_s,volume1.medium.T,volume1.medium.T_degC,volume1.medium.X[1],volume1.medium.d,der(volume1.medium.h),der(volume1.medium.p),der(volume1.medium.u),volume1.medium.h,volume1.medium.p,volume1.medium.p_bar,volume1.medium.phase,volume1.medium.preferredMediumStates,volume1.medium.quality,volume1.medium.sat.Tsat,volume1.medium.sat.psat,volume1.medium.standardOrderComponents,volume1.medium.state.T,volume1.medium.state.d,der(volume1.medium.state.d),volume1.medium.state.h,volume1.medium.state.p,volume1.medium.state.phase,volume1.medium.u,volume1.outlet.m_flow,volume1.outlet.r,volume1.outlet.state.T,volume1.outlet.state.d,volume1.outlet.state.h,volume1.outlet.state.p,volume1.outlet.state.phase,volume1.p_in,volume1.p_start,volume1.r,volume1.r_damping,volume1.r_in,volume1.r_out,volume1.state_in.T,volume1.state_in.d,volume1.state_in.h,volume1.state_in.p,volume1.state_in.phase,volume1.state_out.T,volume1.state_out.d,volume1.state_out.h,volume1.state_out.p,volume1.state_out.phase

Variables in the result:$cse1.T,$cse1.d,$cse1.h,$cse1.p,$cse1.phase,$cse12.T,$cse12.d,$cse12.h,$cse12.p,$cse12.phase,$cse13.T,$cse13.d,$cse13.h,$cse13.p,$cse13.phase,$cse14.T,$cse14.d,$cse14.h,$cse14.p,$cse14.phase,$cse15.T,$cse15.d,$cse15.h,$cse15.p,$cse15.phase,$cse17.T,$cse17.d,$cse17.h,$cse17.p,$cse17.phase,$cse21.T,$cse21.d,$cse21.h,$cse21.p,$cse21.phase,$cse22.T,$cse22.d,$cse22.h,$cse22.p,$cse22.phase,$cse28.T,$cse28.d,$cse28.h,$cse28.p,$cse28.phase,$cse29.T,$cse29.d,$cse29.h,$cse29.p,$cse29.phase,$cse30.T,$cse30.d,$cse30.h,$cse30.p,$cse30.phase,$cse31.T,$cse31.d,$cse31.h,$cse31.p,$cse31.phase,$cse5.T,$cse5.d,$cse5.h,$cse5.p,$cse5.phase,$cse6.T,$cse6.d,$cse6.h,$cse6.p,$cse6.phase,conductionElementHEX_twoPhase.A,conductionElementHEX_twoPhase.L,conductionElementHEX_twoPhase.M,conductionElementHEX_twoPhase.Q_flow,conductionElementHEX_twoPhase.T,conductionElementHEX_twoPhase.T_0,conductionElementHEX_twoPhase.T_e,conductionElementHEX_twoPhase.T_heatPort,conductionElementHEX_twoPhase.U,conductionElementHEX_twoPhase.U_liq,conductionElementHEX_twoPhase.U_liq_nom,conductionElementHEX_twoPhase.U_tp,conductionElementHEX_twoPhase.U_tp_nom,conductionElementHEX_twoPhase.U_vap,conductionElementHEX_twoPhase.U_vap_nom,conductionElementHEX_twoPhase.V,conductionElementHEX_twoPhase.clip_p_out,conductionElementHEX_twoPhase.deltaE_system,conductionElementHEX_twoPhase.delta_x,conductionElementHEX_twoPhase.dp,conductionElementHEX_twoPhase.dr_corr,conductionElementHEX_twoPhase.h,conductionElementHEX_twoPhase.h_0,conductionElementHEX_twoPhase.h_bubble,conductionElementHEX_twoPhase.h_dew,conductionElementHEX_twoPhase.h_in,conductionElementHEX_twoPhase.h_in_norm,conductionElementHEX_twoPhase.h_out,conductionElementHEX_twoPhase.heatPort.Q_flow,conductionElementHEX_twoPhase.heatPort.T,conductionElementHEX_twoPhase.init,conductionElementHEX_twoPhase.initM_flow,conductionElementHEX_twoPhase.inlet.m_flow,conductionElementHEX_twoPhase.inlet.r,conductionElementHEX_twoPhase.inlet.state.T,conductionElementHEX_twoPhase.inlet.state.d,conductionElementHEX_twoPhase.inlet.state.h,conductionElementHEX_twoPhase.inlet.state.p,conductionElementHEX_twoPhase.inlet.state.phase,conductionElementHEX_twoPhase.k,conductionElementHEX_twoPhase.m_acceleration_0,conductionElementHEX_twoPhase.m_flow,conductionElementHEX_twoPhase.m_flowStateSelect,conductionElementHEX_twoPhase.m_flow_0,conductionElementHEX_twoPhase.m_flow_assert,conductionElementHEX_twoPhase.m_flow_nom,conductionElementHEX_twoPhase.nCellsParallel,conductionElementHEX_twoPhase.outlet.m_flow,conductionElementHEX_twoPhase.outlet.r,conductionElementHEX_twoPhase.outlet.state.T,conductionElementHEX_twoPhase.outlet.state.d,conductionElementHEX_twoPhase.outlet.state.h,conductionElementHEX_twoPhase.outlet.state.p,conductionElementHEX_twoPhase.outlet.state.phase,conductionElementHEX_twoPhase.p_in,conductionElementHEX_twoPhase.p_min,conductionElementHEX_twoPhase.p_out,conductionElementHEX_twoPhase.rho,conductionElementHEX_twoPhase.rho_min,conductionElementHEX_twoPhase.state.T,conductionElementHEX_twoPhase.state.d,conductionElementHEX_twoPhase.state.h,conductionElementHEX_twoPhase.state.p,conductionElementHEX_twoPhase.state.phase,conductionElementHEX_twoPhase.x,conductionElementHEX_twoPhase1.A,conductionElementHEX_twoPhase1.L,conductionElementHEX_twoPhase1.M,conductionElementHEX_twoPhase1.Q_flow,conductionElementHEX_twoPhase1.T,conductionElementHEX_twoPhase1.T_0,conductionElementHEX_twoPhase1.T_e,conductionElementHEX_twoPhase1.T_heatPort,conductionElementHEX_twoPhase1.U,conductionElementHEX_twoPhase1.U_liq,conductionElementHEX_twoPhase1.U_liq_nom,conductionElementHEX_twoPhase1.U_tp,conductionElementHEX_twoPhase1.U_tp_nom,conductionElementHEX_twoPhase1.U_vap,conductionElementHEX_twoPhase1.U_vap_nom,conductionElementHEX_twoPhase1.V,conductionElementHEX_twoPhase1.clip_p_out,conductionElementHEX_twoPhase1.deltaE_system,conductionElementHEX_twoPhase1.delta_x,conductionElementHEX_twoPhase1.dp,conductionElementHEX_twoPhase1.dr_corr,conductionElementHEX_twoPhase1.h,conductionElementHEX_twoPhase1.h_0,conductionElementHEX_twoPhase1.h_bubble,conductionElementHEX_twoPhase1.h_dew,conductionElementHEX_twoPhase1.h_in,conductionElementHEX_twoPhase1.h_in_norm,conductionElementHEX_twoPhase1.h_out,conductionElementHEX_twoPhase1.heatPort.Q_flow,conductionElementHEX_twoPhase1.heatPort.T,conductionElementHEX_twoPhase1.init,conductionElementHEX_twoPhase1.initM_flow,conductionElementHEX_twoPhase1.inlet.m_flow,conductionElementHEX_twoPhase1.inlet.r,conductionElementHEX_twoPhase1.inlet.state.T,conductionElementHEX_twoPhase1.inlet.state.d,conductionElementHEX_twoPhase1.inlet.state.h,conductionElementHEX_twoPhase1.inlet.state.p,conductionElementHEX_twoPhase1.inlet.state.phase,conductionElementHEX_twoPhase1.k,conductionElementHEX_twoPhase1.m_acceleration_0,conductionElementHEX_twoPhase1.m_flow,conductionElementHEX_twoPhase1.m_flowStateSelect,conductionElementHEX_twoPhase1.m_flow_0,conductionElementHEX_twoPhase1.m_flow_assert,conductionElementHEX_twoPhase1.m_flow_nom,conductionElementHEX_twoPhase1.nCellsParallel,conductionElementHEX_twoPhase1.outlet.m_flow,conductionElementHEX_twoPhase1.outlet.r,conductionElementHEX_twoPhase1.outlet.state.T,conductionElementHEX_twoPhase1.outlet.state.d,conductionElementHEX_twoPhase1.outlet.state.h,conductionElementHEX_twoPhase1.outlet.state.p,conductionElementHEX_twoPhase1.outlet.state.phase,conductionElementHEX_twoPhase1.p_in,conductionElementHEX_twoPhase1.p_min,conductionElementHEX_twoPhase1.p_out,conductionElementHEX_twoPhase1.rho,conductionElementHEX_twoPhase1.rho_min,conductionElementHEX_twoPhase1.state.T,conductionElementHEX_twoPhase1.state.d,conductionElementHEX_twoPhase1.state.h,conductionElementHEX_twoPhase1.state.p,conductionElementHEX_twoPhase1.state.phase,conductionElementHEX_twoPhase1.x,der(conductionElementHEX_twoPhase.h),der(conductionElementHEX_twoPhase1.h),der(flowResistance.inlet.m_flow),der(flowResistance1.inlet.m_flow),der(flowResistance2.inlet.m_flow),der(flowResistance3.inlet.m_flow),der(mCV.dp_int),der(mCV1.dp_int),der(mCV2.dp_int),der(mCV2.inlet.m_flow),der(mCV3.dp_int),der(mCV3.inlet.m_flow),der(volume.M),der(volume.U_med),der(volume.medium.h),der(volume.medium.p),der(volume.medium.u),der(volume1.M),der(volume1.U_med),der(volume1.medium.h),der(volume1.medium.p),der(volume1.medium.u),dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,flowResistance1.D_h,flowResistance1.L,flowResistance1.L_value,flowResistance1.a,flowResistance1.areaCross,flowResistance1.areaCrossInput,flowResistance1.areaHydraulic,flowResistance1.b,flowResistance1.clip_p_out,flowResistance1.dp,flowResistance1.dp_ref_color,flowResistance1.dr_corr,flowResistance1.h_in,flowResistance1.h_out,flowResistance1.initM_flow,flowResistance1.inlet.m_flow,flowResistance1.inlet.r,flowResistance1.inlet.state.T,flowResistance1.inlet.state.d,flowResistance1.inlet.state.h,flowResistance1.inlet.state.p,flowResistance1.inlet.state.phase,flowResistance1.l,flowResistance1.m_acceleration_0,flowResistance1.m_flow,flowResistance1.m_flowStateSelect,flowResistance1.m_flow_0,flowResistance1.mu_in,flowResistance1.outlet.m_flow,flowResistance1.outlet.r,flowResistance1.outlet.state.T,flowResistance1.outlet.state.d,flowResistance1.outlet.state.h,flowResistance1.outlet.state.p,flowResistance1.outlet.state.phase,flowResistance1.p_in,flowResistance1.p_min,flowResistance1.p_out,flowResistance1.perimeter,flowResistance1.perimeterInput,flowResistance1.phi,flowResistance1.pressureDropSignificantDigits,flowResistance1.r,flowResistance1.rho_in,flowResistance1.rho_min,flowResistance1.shape,flowResistance2.D_h,flowResistance2.L,flowResistance2.L_value,flowResistance2.a,flowResistance2.areaCross,flowResistance2.areaCrossInput,flowResistance2.areaHydraulic,flowResistance2.b,flowResistance2.clip_p_out,flowResistance2.dp,flowResistance2.dp_ref_color,flowResistance2.dr_corr,flowResistance2.h_in,flowResistance2.h_out,flowResistance2.initM_flow,flowResistance2.inlet.m_flow,flowResistance2.inlet.r,flowResistance2.inlet.state.T,flowResistance2.inlet.state.d,flowResistance2.inlet.state.h,flowResistance2.inlet.state.p,flowResistance2.inlet.state.phase,flowResistance2.l,flowResistance2.m_acceleration_0,flowResistance2.m_flow,flowResistance2.m_flowStateSelect,flowResistance2.m_flow_0,flowResistance2.mu_in,flowResistance2.outlet.m_flow,flowResistance2.outlet.r,flowResistance2.outlet.state.T,flowResistance2.outlet.state.d,flowResistance2.outlet.state.h,flowResistance2.outlet.state.p,flowResistance2.outlet.state.phase,flowResistance2.p_in,flowResistance2.p_min,flowResistance2.p_out,flowResistance2.perimeter,flowResistance2.perimeterInput,flowResistance2.phi,flowResistance2.pressureDropSignificantDigits,flowResistance2.r,flowResistance2.rho_in,flowResistance2.rho_min,flowResistance2.shape,flowResistance3.D_h,flowResistance3.L,flowResistance3.L_value,flowResistance3.a,flowResistance3.areaCross,flowResistance3.areaCrossInput,flowResistance3.areaHydraulic,flowResistance3.b,flowResistance3.clip_p_out,flowResistance3.dp,flowResistance3.dp_ref_color,flowResistance3.dr_corr,flowResistance3.h_in,flowResistance3.h_out,flowResistance3.initM_flow,flowResistance3.inlet.m_flow,flowResistance3.inlet.r,flowResistance3.inlet.state.T,flowResistance3.inlet.state.d,flowResistance3.inlet.state.h,flowResistance3.inlet.state.p,flowResistance3.inlet.state.phase,flowResistance3.l,flowResistance3.m_acceleration_0,flowResistance3.m_flow,flowResistance3.m_flowStateSelect,flowResistance3.m_flow_0,flowResistance3.mu_in,flowResistance3.outlet.m_flow,flowResistance3.outlet.r,flowResistance3.outlet.state.T,flowResistance3.outlet.state.d,flowResistance3.outlet.state.h,flowResistance3.outlet.state.p,flowResistance3.outlet.state.phase,flowResistance3.p_in,flowResistance3.p_min,flowResistance3.p_out,flowResistance3.perimeter,flowResistance3.perimeterInput,flowResistance3.phi,flowResistance3.pressureDropSignificantDigits,flowResistance3.r,flowResistance3.rho_in,flowResistance3.rho_min,flowResistance3.shape,mCV.L,mCV.TC,mCV.V_flow,mCV.V_flow_set,mCV.clip_p_out,mCV.dp,mCV.dp_corr,mCV.dp_int,mCV.dr,mCV.dr_corr,mCV.dr_set,mCV.enableClippingOutput,mCV.h_in,mCV.h_out,mCV.initM_flow,mCV.inlet.m_flow,mCV.inlet.r,mCV.inlet.state.T,mCV.inlet.state.d,mCV.inlet.state.h,mCV.inlet.state.p,mCV.inlet.state.phase,mCV.k1,mCV.k2,mCV.m_acceleration_0,mCV.m_flow,mCV.m_flowStateSelect,mCV.m_flow_0,mCV.m_flow_set,mCV.massFlow_set_par,mCV.mode,mCV.outlet.m_flow,mCV.outlet.r,mCV.outlet.state.T,mCV.outlet.state.d,mCV.outlet.state.h,mCV.outlet.state.p,mCV.outlet.state.phase,mCV.p_in,mCV.p_min,mCV.p_min_par,mCV.p_out,mCV.rho_in,mCV.setpoint,mCV.volumeFlow_set_par,mCV1.L,mCV1.TC,mCV1.V_flow,mCV1.V_flow_set,mCV1.clip_p_out,mCV1.dp,mCV1.dp_corr,mCV1.dp_int,mCV1.dr,mCV1.dr_corr,mCV1.dr_set,mCV1.enableClippingOutput,mCV1.h_in,mCV1.h_out,mCV1.initM_flow,mCV1.inlet.m_flow,mCV1.inlet.r,mCV1.inlet.state.T,mCV1.inlet.state.d,mCV1.inlet.state.h,mCV1.inlet.state.p,mCV1.inlet.state.phase,mCV1.k1,mCV1.k2,mCV1.m_acceleration_0,mCV1.m_flow,mCV1.m_flowStateSelect,mCV1.m_flow_0,mCV1.m_flow_set,mCV1.massFlow_set_par,mCV1.mode,mCV1.outlet.m_flow,mCV1.outlet.r,mCV1.outlet.state.T,mCV1.outlet.state.d,mCV1.outlet.state.h,mCV1.outlet.state.p,mCV1.outlet.state.phase,mCV1.p_in,mCV1.p_min,mCV1.p_min_par,mCV1.p_out,mCV1.rho_in,mCV1.setpoint,mCV1.volumeFlow_set_par,mCV2.L,mCV2.TC,mCV2.V_flow,mCV2.V_flow_set,mCV2.clip_p_out,mCV2.dp,mCV2.dp_corr,mCV2.dp_int,mCV2.dr,mCV2.dr_corr,mCV2.dr_set,mCV2.enableClippingOutput,mCV2.h_in,mCV2.h_out,mCV2.initM_flow,mCV2.inlet.m_flow,mCV2.inlet.r,mCV2.inlet.state.T,mCV2.inlet.state.d,mCV2.inlet.state.h,mCV2.inlet.state.p,mCV2.inlet.state.phase,mCV2.k1,mCV2.k2,mCV2.m_acceleration_0,mCV2.m_flow,mCV2.m_flowStateSelect,mCV2.m_flow_0,mCV2.m_flow_set,mCV2.massFlow_set_par,mCV2.mode,mCV2.outlet.m_flow,mCV2.outlet.r,mCV2.outlet.state.T,mCV2.outlet.state.d,mCV2.outlet.state.h,mCV2.outlet.state.p,mCV2.outlet.state.phase,mCV2.p_in,mCV2.p_min,mCV2.p_min_par,mCV2.p_out,mCV2.rho_in,mCV2.setpoint,mCV2.volumeFlow_set_par,mCV3.L,mCV3.TC,mCV3.V_flow,mCV3.V_flow_set,mCV3.clip_p_out,mCV3.dp,mCV3.dp_corr,mCV3.dp_int,mCV3.dr,mCV3.dr_corr,mCV3.dr_set,mCV3.enableClippingOutput,mCV3.h_in,mCV3.h_out,mCV3.initM_flow,mCV3.inlet.m_flow,mCV3.inlet.r,mCV3.inlet.state.T,mCV3.inlet.state.d,mCV3.inlet.state.h,mCV3.inlet.state.p,mCV3.inlet.state.phase,mCV3.k1,mCV3.k2,mCV3.m_acceleration_0,mCV3.m_flow,mCV3.m_flowStateSelect,mCV3.m_flow_0,mCV3.m_flow_set,mCV3.massFlow_set_par,mCV3.mode,mCV3.outlet.m_flow,mCV3.outlet.r,mCV3.outlet.state.T,mCV3.outlet.state.d,mCV3.outlet.state.h,mCV3.outlet.state.p,mCV3.outlet.state.phase,mCV3.p_in,mCV3.p_min,mCV3.p_min_par,mCV3.p_out,mCV3.rho_in,mCV3.setpoint,mCV3.volumeFlow_set_par,prescribedTemperature.T,prescribedTemperature.port.Q_flow,prescribedTemperature.port.T,prescribedTemperature1.T,prescribedTemperature1.port.Q_flow,prescribedTemperature1.port.T,sink.L,sink.inlet.m_flow,sink.inlet.r,sink.inlet.state.T,sink.inlet.state.d,sink.inlet.state.h,sink.inlet.state.p,sink.inlet.state.phase,sink.p,sink.p0,sink.p0_par,sink.r,sink1.L,sink1.inlet.m_flow,sink1.inlet.r,sink1.inlet.state.T,sink1.inlet.state.d,sink1.inlet.state.h,sink1.inlet.state.p,sink1.inlet.state.phase,sink1.p,sink1.p0,sink1.p0_par,sink1.r,sink2.L,sink2.inlet.m_flow,sink2.inlet.r,sink2.inlet.state.T,sink2.inlet.state.d,sink2.inlet.state.h,sink2.inlet.state.p,sink2.inlet.state.phase,sink2.p,sink2.p0,sink2.p0_par,sink2.r,sink3.L,sink3.inlet.m_flow,sink3.inlet.r,sink3.inlet.state.T,sink3.inlet.state.d,sink3.inlet.state.h,sink3.inlet.state.p,sink3.inlet.state.phase,sink3.p,sink3.p0,sink3.p0_par,sink3.r,source.L,source.T0,source.T0_par,source.h0,source.h0_par,source.h0_var,source.outlet.m_flow,source.outlet.r,source.outlet.stat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filterSimulationResults("ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.diff.mat", vars={"volume1.state_out.p", "volume1.state_out.d", "volume1.r_out", "volume1.r_in", "volume1.r_damping", "volume1.r", "volume1.outlet.m_flow", "volume1.medium.quality", "volume1.medium.p_bar", "volume1.medium.der(u)", "volume1.medium.der(p)", "volume1.medium.der(h)", "volume1.medium.T_degC", "volume1.m_flow_in", "volume1.heatPort.Q_flow", "volume1.h_in", "volume1.der(U_med)", "volume1.der(M)", "volume1.U_med", "volume1.M", "source3.outlet.r", "sink3.inlet.state.d", "mCV3.dr_set", "mCV3.dp_int", "mCV3.dp", "mCV3.V_flow", "flowResistance3.dp"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
filterSimulationResults("/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_ref.mat", "/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.diff.ref.mat", vars={"volume1.state_out.p", "volume1.state_out.d", "volume1.r_out", "volume1.r_in", "volume1.r_damping", "volume1.r", "volume1.outlet.m_flow", "volume1.medium.quality", "volume1.medium.p_bar", "volume1.medium.der(u)", "volume1.medium.der(p)", "volume1.medium.der(h)", "volume1.medium.T_degC", "volume1.m_flow_in", "volume1.heatPort.Q_flow", "volume1.h_in", "volume1.der(U_med)", "volume1.der(M)", "volume1.U_med", "volume1.M", "source3.outlet.r", "sink3.inlet.state.d", "mCV3.dr_set", "mCV3.dp_int", "mCV3.dp", "mCV3.V_flow", "flowResistance3.dp"}, removeDescription=false) [Timeout 660]
""
[Timeout remaining time 660]
[Calling sys.exit(0), Time elapsed: 24.03747961902991]