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 0.001307/0.001307, 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 0.001529/0.001529, allocations: 173 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 0.9752/0.9752, allocations: 177.2 MB / 203.4 MB, free: 5.598 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 0.6989/0.6989, allocations: 118.7 MB / 378.6 MB, free: 1.484 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 2.044e-06/2.044e-06, allocations: 0 / 483.7 MB, free: 8.168 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.433e-05/2.637e-05, allocations: 2.312 kB / 483.7 MB, free: 8.164 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase): time 0.02238/0.0224, allocations: 22.57 MB / 0.4944 GB, free: 9.414 MB / 426.7 MB
Notification: Performance of NFInst.instExpressions: time 0.02/0.0424, allocations: 17.09 MB / 0.5111 GB, free: 8.895 MB / 442.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.002784/0.04518, allocations: 130.8 kB / 0.5112 GB, free: 8.766 MB / 442.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.001229/0.04641, allocations: 0.5265 MB / 0.5117 GB, free: 8.234 MB / 442.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.009801/0.05621, allocations: 3.806 MB / 0.5154 GB, free: 4.406 MB / 442.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.003028/0.05924, allocations: 1.18 MB / 0.5166 GB, free: 3.223 MB / 442.7 MB
Notification: Performance of NFFlatten.flatten: time 0.005173/0.06441, allocations: 4.619 MB / 0.5211 GB, free: 14.58 MB / 458.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0009276/0.06534, allocations: 428.2 kB / 0.5215 GB, free: 14.12 MB / 458.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.00353/0.06887, allocations: 2.458 MB / 0.5239 GB, free: 11.66 MB / 458.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.001679/0.07055, allocations: 1.219 MB / 0.5251 GB, free: 10.44 MB / 458.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.000479/0.07103, allocations: 200 kB / 0.5253 GB, free: 10.24 MB / 458.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.009628/0.08066, allocations: 5.957 MB / 0.5311 GB, free: 4.273 MB / 458.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0007296/0.08139, allocations: 0.5365 MB / 0.5316 GB, free: 3.734 MB / 458.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.002161/0.08355, allocations: 0.9975 MB / 0.5326 GB, free: 2.734 MB / 458.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.0162/0.09975, allocations: 7.254 MB / 0.5397 GB, free: 11.46 MB / 474.7 MB
Notification: Performance of FrontEnd - DAE generated: time 6.722e-06/0.09976, allocations: 0 / 0.5397 GB, free: 11.46 MB / 474.7 MB
Notification: Performance of FrontEnd: time 1.352e-06/0.09976, allocations: 0 / 0.5397 GB, free: 11.46 MB / 474.7 MB
Notification: Performance of Transformations before backend: time 6.044e-05/0.09982, allocations: 0 / 0.5397 GB, free: 11.46 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 0.00665/0.1065, allocations: 3.53 MB / 0.5431 GB, free: 7.855 MB / 474.7 MB
Notification: Performance of prepare preOptimizeDAE: time 4.538e-05/0.1065, allocations: 8.031 kB / 0.5431 GB, free: 7.848 MB / 474.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.002524/0.109, allocations: 0.9573 MB / 0.5441 GB, free: 6.887 MB / 474.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.002464/0.1115, allocations: 1.655 MB / 0.5457 GB, free: 5.145 MB / 474.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001055/0.1116, allocations: 143.6 kB / 0.5458 GB, free: 5.004 MB / 474.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0002398/0.1118, allocations: 199.9 kB / 0.546 GB, free: 4.809 MB / 474.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002899/0.1147, allocations: 2.057 MB / 0.548 GB, free: 2.52 MB / 474.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 3.575e-05/0.1148, allocations: 3.938 kB / 0.548 GB, free: 2.516 MB / 474.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.0001383/0.1149, allocations: 79.94 kB / 0.5481 GB, free: 2.438 MB / 474.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 5.768e-05/0.115, allocations: 71.97 kB / 0.5482 GB, free: 2.367 MB / 474.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001745/0.1167, allocations: 0.8974 MB / 0.5491 GB, free: 1.469 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 0.008987/0.1257, allocations: 8.037 MB / 0.5569 GB, free: 9.223 MB / 490.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.002063/0.1278, allocations: 1.006 MB / 0.5579 GB, free: 8.199 MB / 490.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0007217/0.1285, allocations: 464.3 kB / 0.5583 GB, free: 7.742 MB / 490.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.001271/0.1298, allocations: 0.5592 MB / 0.5589 GB, free: 7.18 MB / 490.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.001357/0.1311, allocations: 1.078 MB / 0.5599 GB, free: 5.996 MB / 490.7 MB
Notification: Performance of pre-optimization done (n=221): time 4.629e-06/0.1311, allocations: 0 / 0.5599 GB, free: 5.996 MB / 490.7 MB
Notification: Performance of matching and sorting (n=229): time 0.01216/0.1433, allocations: 4.867 MB / 0.5647 GB, free: 1.016 MB / 490.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 7.747e-05/0.1434, allocations: 146.2 kB / 0.5648 GB, free: 0.8398 MB / 490.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001577/0.1449, allocations: 1.475 MB / 0.5663 GB, free: 15.32 MB / 0.4948 GB
Notification: Performance of collectPreVariables (initialization): time 0.0001055/0.145, allocations: 57.7 kB / 0.5663 GB, free: 15.25 MB / 0.4948 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0007215/0.1458, allocations: 1.105 MB / 0.5674 GB, free: 14.14 MB / 0.4948 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0005367/0.1463, allocations: 0.7822 MB / 0.5682 GB, free: 13.35 MB / 0.4948 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0004861/0.1468, allocations: 381.8 kB / 0.5685 GB, free: 12.97 MB / 0.4948 GB
Notification: Performance of setup shared object (initialization): time 0.0001101/0.1469, allocations: 480.7 kB / 0.569 GB, free: 12.5 MB / 0.4948 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0007676/0.1477, allocations: 423.4 kB / 0.5694 GB, free: 12.07 MB / 0.4948 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.001059/0.1487, allocations: 0.8789 MB / 0.5702 GB, free: 11.02 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 0.002162/0.1509, allocations: 1.329 MB / 0.5715 GB, free: 9.543 MB / 0.4948 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 8.817e-06/0.1509, allocations: 4 kB / 0.5715 GB, free: 9.539 MB / 0.4948 GB
Notification: Performance of matching and sorting (n=283) (initialization): time 0.003639/0.1545, allocations: 1.942 MB / 0.5734 GB, free: 7.531 MB / 0.4948 GB
Notification: Performance of prepare postOptimizeDAE: time 6.346e-05/0.1546, allocations: 59.91 kB / 0.5735 GB, free: 7.461 MB / 0.4948 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.983e-05/0.1546, allocations: 11.98 kB / 0.5735 GB, free: 7.449 MB / 0.4948 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.00792/0.1625, allocations: 0.6452 MB / 0.5741 GB, free: 6.77 MB / 0.4948 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.001262/0.1638, allocations: 359.5 kB / 0.5745 GB, free: 6.418 MB / 0.4948 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.006669/0.1705, allocations: 12.4 MB / 0.5866 GB, free: 9.223 MB / 0.5105 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.001512/0.172, allocations: 76.3 kB / 0.5867 GB, free: 9.148 MB / 0.5105 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.0001609/0.1721, allocations: 83.97 kB / 0.5867 GB, free: 9.066 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 0.0006836/0.1728, allocations: 284.2 kB / 0.587 GB, free: 8.781 MB / 0.5105 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0003631/0.1732, allocations: 294.4 kB / 0.5873 GB, free: 8.492 MB / 0.5105 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.003264/0.1765, allocations: 2.465 MB / 0.5897 GB, free: 6.008 MB / 0.5105 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.002366/0.1788, allocations: 1.812 MB / 0.5915 GB, free: 4.152 MB / 0.5105 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 1.938e-05/0.1788, allocations: 7.938 kB / 0.5915 GB, free: 4.145 MB / 0.5105 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.756e-05/0.1789, allocations: 11.95 kB / 0.5915 GB, free: 4.133 MB / 0.5105 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.006242/0.1851, allocations: 4.816 MB / 0.5962 GB, free: 15.15 MB / 0.5261 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 9.197e-06/0.1851, allocations: 4 kB / 0.5962 GB, free: 15.15 MB / 0.5261 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0009413/0.186, allocations: 424 kB / 0.5966 GB, free: 14.73 MB / 0.5261 GB
Notification: Performance of postOpt tearingSystem (simulation): time 0.001588/0.1876, allocations: 0.5937 MB / 0.5972 GB, free: 14.1 MB / 0.5261 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.000155/0.1878, allocations: 71.95 kB / 0.5972 GB, free: 14.03 MB / 0.5261 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.005868/0.1937, allocations: 14.09 MB / 0.611 GB, free: 15.07 MB / 0.5417 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 4.048e-06/0.1937, allocations: 4 kB / 0.611 GB, free: 15.07 MB / 0.5417 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.004392/0.1981, allocations: 3.172 MB / 0.6141 GB, free: 11.7 MB / 0.5417 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0008837/0.1989, allocations: 441.7 kB / 0.6145 GB, free: 11.27 MB / 0.5417 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001955/0.1991, allocations: 63.89 kB / 0.6146 GB, free: 11.2 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0006475/0.1998, allocations: 87.94 kB / 0.6147 GB, free: 11.12 MB / 0.5417 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0003003/0.2001, allocations: 205.8 kB / 0.6149 GB, free: 10.92 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.0001095/0.2002, allocations: 95.89 kB / 0.615 GB, free: 10.82 MB / 0.5417 GB
Notification: Performance of sorting global known variables: time 0.0008604/0.2011, allocations: 0.8897 MB / 0.6158 GB, free: 9.914 MB / 0.5417 GB
Notification: Performance of sort global known variables: time 9e-08/0.2011, allocations: 0 / 0.6158 GB, free: 9.914 MB / 0.5417 GB
Notification: Performance of remove unused functions: time 0.003486/0.2045, allocations: 1.011 MB / 0.6168 GB, free: 8.902 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 0.009678/0.2142, allocations: 3.74 MB / 0.6205 GB, free: 5.152 MB / 0.5417 GB
Notification: Performance of simCode: created initialization part: time 0.003963/0.2182, allocations: 3.216 MB / 0.6236 GB, free: 1.68 MB / 0.5417 GB
Notification: Performance of simCode: created event and clocks part: time 9.438e-06/0.2182, allocations: 0 / 0.6236 GB, free: 1.68 MB / 0.5417 GB
Notification: Performance of simCode: created simulation system equations: time 0.001887/0.2201, allocations: 1.957 MB / 0.6255 GB, free: 15.61 MB / 0.5573 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.00402/0.2241, allocations: 1.257 MB / 0.6267 GB, free: 14.38 MB / 0.5573 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.008204/0.2323, allocations: 5.185 MB / 0.6318 GB, free: 9.07 MB / 0.5573 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0005235/0.2328, allocations: 497.5 kB / 0.6323 GB, free: 8.559 MB / 0.5573 GB
Notification: Performance of simCode: alias equations: time 0.001599/0.2344, allocations: 453.1 kB / 0.6327 GB, free: 8.113 MB / 0.5573 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0006446/0.2351, allocations: 224.4 kB / 0.6329 GB, free: 7.895 MB / 0.5573 GB
Notification: Performance of SimCode: time 2.565e-06/0.2351, allocations: 0 / 0.6329 GB, free: 7.895 MB / 0.5573 GB
Notification: Performance of Templates: time 0.3072/0.5422, allocations: 71.26 MB / 0.7025 GB, free: 89.96 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: 16.452835546806455]