Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.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 0.0008033/0.0008033, allocations: 80.25 kB / 20.04 MB, free: 4.488 MB / 18.57 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 0.0007877/0.0007877, allocations: 173.9 kB / 23.34 MB, free: 1.184 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 0.8808/0.8808, allocations: 177.1 MB / 203.7 MB, free: 5.637 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.6434/0.6434, allocations: 116 MB / 376.1 MB, free: 4.156 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/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.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.d|fullMedium.adiabaticModel.state_in.h|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.state_in.phase|fullMedium.adiabaticModel.w_t|fullMedium.adiabaticModel.w_t_is|fullMedium.assertionLevel|fullMedium.clip_p_out|fullMedium.dh|fullMedium.dp|fullMedium.dp_fixed|fullMedium.dp_nom|fullMedium.dp_start|fullMedium.dr_corr|fullMedium.etaSpec|fullMedium.eta_actual|fullMedium.eta_fixed|fullMedium.eta_is|fullMedium.h_in|fullMedium.h_out|fullMedium.initM_flow|der.fullMedium.inlet.m_flow.|fullMedium.inlet.m_flow|fullMedium.inlet.r|fullMedium.inlet.state.T|fullMedium.inlet.state.d|fullMedium.inlet.state.h|fullMedium.inlet.state.p|fullMedium.inlet.state.phase|fullMedium.m_acceleration_0|fullMedium.m_flow|fullMedium.m_flowStateSelect|fullMedium.m_flow_0|fullMedium.outlet.m_flow|fullMedium.outlet.r|fullMedium.outlet.state.T|fullMedium.outlet.state.d|fullMedium.outlet.state.h|fullMedium.outlet.state.p|fullMedium.outlet.state.phase|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletSpec_prescribed|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.TC|incompressibleFluid.adiabaticModel.T_in|incompressibleFluid.adiabaticModel.T_out_is|incompressibleFluid.adiabaticModel.assertionLevel|incompressibleFluid.adiabaticModel.deltaDensityRel|incompressibleFluid.adiabaticModel.eta_is|incompressibleFluid.adiabaticModel.h_in|incompressibleFluid.adiabaticModel.h_out|incompressibleFluid.adiabaticModel.isDensityWithinTol|incompressibleFluid.adiabaticModel.p_out|incompressibleFluid.adiabaticModel.relTolDensity|incompressibleFluid.adiabaticModel.rho_in|incompressibleFluid.adiabaticModel.rho_out|incompressibleFluid.adiabaticModel.state_in.T|incompressibleFluid.adiabaticModel.state_in.d|incompressibleFluid.adiabaticModel.state_in.h|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.state_in.phase|incompressibleFluid.adiabaticModel.w_t|incompressibleFluid.adiabaticModel.w_t_is|incompressibleFluid.assertionLevel|incompressibleFluid.clip_p_out|incompressibleFluid.dh|incompressibleFluid.dp|incompressibleFluid.dp_fixed|incompressibleFluid.dp_nom|incompressibleFluid.dp_start|incompressibleFluid.dr_corr|incompressibleFluid.etaSpec|incompressibleFluid.eta_actual|incompressibleFluid.eta_fixed|incompressibleFluid.eta_is|incompressibleFluid.h_in|incompressibleFluid.h_out|incompressibleFluid.initM_flow|der.incompressibleFluid.inlet.m_flow.|incompressibleFluid.inlet.m_flow|incompressibleFluid.inlet.r|incompressibleFluid.inlet.state.T|incompressibleFluid.inlet.state.d|incompressibleFluid.inlet.state.h|incompressibleFluid.inlet.state.p|incompressibleFluid.inlet.state.phase|incompressibleFluid.m_acceleration_0|incompressibleFluid.m_flow|incompressibleFluid.m_flowStateSelect|incompressibleFluid.m_flow_0|incompressibleFluid.outlet.m_flow|incompressibleFluid.outlet.r|incompressibleFluid.outlet.state.T|incompressibleFluid.outlet.state.d|incompressibleFluid.outlet.state.h|incompressibleFluid.outlet.state.p|incompressibleFluid.outlet.state.phase|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletSpec_prescribed|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|isothermalReference.L|isothermalReference.P|isothermalReference.P_nom|isothermalReference.TC|isothermalReference.adiabaticModel.T_in|isothermalReference.adiabaticModel.T_out_is|isothermalReference.adiabaticModel.assertionLevel|isothermalReference.adiabaticModel.deltaDensityRel|isothermalReference.adiabaticModel.eta_is|isothermalReference.adiabaticModel.h_in|isothermalReference.adiabaticModel.h_out|isothermalReference.adiabaticModel.h_out_is|isothermalReference.adiabaticModel.isDensityWithinTol|isothermalReference.adiabaticModel.p_out|isothermalReference.adiabaticModel.relTolDensity|isothermalReference.adiabaticModel.rho_in|isothermalReference.adiabaticModel.rho_out|isothermalReference.adiabaticModel.state_in.T|isothermalReference.adiabaticModel.state_in.d|isothermalReference.adiabaticModel.state_in.h|isothermalReference.adiabaticModel.state_in.p|isothermalReference.adiabaticModel.state_in.phase|isothermalReference.adiabaticModel.w_t|isothermalReference.adiabaticModel.w_t_is|isothermalReference.assertionLevel|isothermalReference.clip_p_out|isothermalReference.dh|isothermalReference.dp|isothermalReference.dp_fixed|isothermalReference.dp_nom|isothermalReference.dp_start|isothermalReference.dr_corr|isothermalReference.etaSpec|isothermalReference.eta_actual|isothermalReference.eta_fixed|isothermalReference.eta_is|isothermalReference.h_in|isothermalReference.h_out|isothermalReference.initM_flow|der.isothermalReference.inlet.m_flow.|isothermalReference.inlet.m_flow|isothermalReference.inlet.r|isothermalReference.inlet.state.T|isothermalReference.inlet.state.d|isothermalReference.inlet.state.h|isothermalReference.inlet.state.p|isothermalReference.inlet.state.phase|isothermalReference.m_acceleration_0|isothermalReference.m_flow|isothermalReference.m_flowStateSelect|isothermalReference.m_flow_0|isothermalReference.outlet.m_flow|isothermalReference.outlet.r|isothermalReference.outlet.state.T|isothermalReference.outlet.state.d|isothermalReference.outlet.state.h|isothermalReference.outlet.state.p|isothermalReference.outlet.state.phase|isothermalReference.outletSpec|isothermalReference.outletSpec_actual|isothermalReference.outletSpec_prescribed|isothermalReference.outletValueSpec|isothermalReference.pRatio|isothermalReference.pRatio_fixed|isothermalReference.p_in|isothermalReference.p_min|isothermalReference.p_out|isothermalReference.p_out_fixed|isothermalReference.singularityRegime|pressureDifference.duration|pressureDifference.height|pressureDifference.offset|pressureDifference.startTime|pressureDifference.y|sink.L|der.sink.inlet.m_flow.|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.m_flow|sink.m_flowSpec|sink.m_flow_fixed|sink1.L|der.sink1.inlet.m_flow.|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.m_flow|sink1.m_flowSpec|sink1.m_flow_fixed|sink2.L|der.sink2.inlet.m_flow.|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.m_flow|sink2.m_flowSpec|sink2.m_flow_fixed|source.L|source.T0|source.T0_par|source.h0|source.h0_par|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|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",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater")
translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.d|fullMedium.adiabaticModel.state_in.h|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.state_in.phase|fullMedium.adiabaticModel.w_t|fullMedium.adiabaticModel.w_t_is|fullMedium.assertionLevel|fullMedium.clip_p_out|fullMedium.dh|fullMedium.dp|fullMedium.dp_fixed|fullMedium.dp_nom|fullMedium.dp_start|fullMedium.dr_corr|fullMedium.etaSpec|fullMedium.eta_actual|fullMedium.eta_fixed|fullMedium.eta_is|fullMedium.h_in|fullMedium.h_out|fullMedium.initM_flow|der.fullMedium.inlet.m_flow.|fullMedium.inlet.m_flow|fullMedium.inlet.r|fullMedium.inlet.state.T|fullMedium.inlet.state.d|fullMedium.inlet.state.h|fullMedium.inlet.state.p|fullMedium.inlet.state.phase|fullMedium.m_acceleration_0|fullMedium.m_flow|fullMedium.m_flowStateSelect|fullMedium.m_flow_0|fullMedium.outlet.m_flow|fullMedium.outlet.r|fullMedium.outlet.state.T|fullMedium.outlet.state.d|fullMedium.outlet.state.h|fullMedium.outlet.state.p|fullMedium.outlet.state.phase|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletSpec_prescribed|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.TC|incompressibleFluid.adiabaticModel.T_in|incompressibleFluid.adiabaticModel.T_out_is|incompressibleFluid.adiabaticModel.assertionLevel|incompressibleFluid.adiabaticModel.deltaDensityRel|incompressibleFluid.adiabaticModel.eta_is|incompressibleFluid.adiabaticModel.h_in|incompressibleFluid.adiabaticModel.h_out|incompressibleFluid.adiabaticModel.isDensityWithinTol|incompressibleFluid.adiabaticModel.p_out|incompressibleFluid.adiabaticModel.relTolDensity|incompressibleFluid.adiabaticModel.rho_in|incompressibleFluid.adiabaticModel.rho_out|incompressibleFluid.adiabaticModel.state_in.T|incompressibleFluid.adiabaticModel.state_in.d|incompressibleFluid.adiabaticModel.state_in.h|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.state_in.phase|incompressibleFluid.adiabaticModel.w_t|incompressibleFluid.adiabaticModel.w_t_is|incompressibleFluid.assertionLevel|incompressibleFluid.clip_p_out|incompressibleFluid.dh|incompressibleFluid.dp|incompressibleFluid.dp_fixed|incompressibleFluid.dp_nom|incompressibleFluid.dp_start|incompressibleFluid.dr_corr|incompressibleFluid.etaSpec|incompressibleFluid.eta_actual|incompressibleFluid.eta_fixed|incompressibleFluid.eta_is|incompressibleFluid.h_in|incompressibleFluid.h_out|incompressibleFluid.initM_flow|der.incompressibleFluid.inlet.m_flow.|incompressibleFluid.inlet.m_flow|incompressibleFluid.inlet.r|incompressibleFluid.inlet.state.T|incompressibleFluid.inlet.state.d|incompressibleFluid.inlet.state.h|incompressibleFluid.inlet.state.p|incompressibleFluid.inlet.state.phase|incompressibleFluid.m_acceleration_0|incompressibleFluid.m_flow|incompressibleFluid.m_flowStateSelect|incompressibleFluid.m_flow_0|incompressibleFluid.outlet.m_flow|incompressibleFluid.outlet.r|incompressibleFluid.outlet.state.T|incompressibleFluid.outlet.state.d|incompressibleFluid.outlet.state.h|incompressibleFluid.outlet.state.p|incompressibleFluid.outlet.state.phase|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletSpec_prescribed|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|isothermalReference.L|isothermalReference.P|isothermalReference.P_nom|isothermalReference.TC|isothermalReference.adiabaticModel.T_in|isothermalReference.adiabaticModel.T_out_is|isothermalReference.adiabaticModel.assertionLevel|isothermalReference.adiabaticModel.deltaDensityRel|isothermalReference.adiabaticModel.eta_is|isothermalReference.adiabaticModel.h_in|isothermalReference.adiabaticModel.h_out|isothermalReference.adiabaticModel.h_out_is|isothermalReference.adiabaticModel.isDensityWithinTol|isothermalReference.adiabaticModel.p_out|isothermalReference.adiabaticModel.relTolDensity|isothermalReference.adiabaticModel.rho_in|isothermalReference.adiabaticModel.rho_out|isothermalReference.adiabaticModel.state_in.T|isothermalReference.adiabaticModel.state_in.d|isothermalReference.adiabaticModel.state_in.h|isothermalReference.adiabaticModel.state_in.p|isothermalReference.adiabaticModel.state_in.phase|isothermalReference.adiabaticModel.w_t|isothermalReference.adiabaticModel.w_t_is|isothermalReference.assertionLevel|isothermalReference.clip_p_out|isothermalReference.dh|isothermalReference.dp|isothermalReference.dp_fixed|isothermalReference.dp_nom|isothermalReference.dp_start|isothermalReference.dr_corr|isothermalReference.etaSpec|isothermalReference.eta_actual|isothermalReference.eta_fixed|isothermalReference.eta_is|isothermalReference.h_in|isothermalReference.h_out|isothermalReference.initM_flow|der.isothermalReference.inlet.m_flow.|isothermalReference.inlet.m_flow|isothermalReference.inlet.r|isothermalReference.inlet.state.T|isothermalReference.inlet.state.d|isothermalReference.inlet.state.h|isothermalReference.inlet.state.p|isothermalReference.inlet.state.phase|isothermalReference.m_acceleration_0|isothermalReference.m_flow|isothermalReference.m_flowStateSelect|isothermalReference.m_flow_0|isothermalReference.outlet.m_flow|isothermalReference.outlet.r|isothermalReference.outlet.state.T|isothermalReference.outlet.state.d|isothermalReference.outlet.state.h|isothermalReference.outlet.state.p|isothermalReference.outlet.state.phase|isothermalReference.outletSpec|isothermalReference.outletSpec_actual|isothermalReference.outletSpec_prescribed|isothermalReference.outletValueSpec|isothermalReference.pRatio|isothermalReference.pRatio_fixed|isothermalReference.p_in|isothermalReference.p_min|isothermalReference.p_out|isothermalReference.p_out_fixed|isothermalReference.singularityRegime|pressureDifference.duration|pressureDifference.height|pressureDifference.offset|pressureDifference.startTime|pressureDifference.y|sink.L|der.sink.inlet.m_flow.|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.m_flow|sink.m_flowSpec|sink.m_flow_fixed|sink1.L|der.sink1.inlet.m_flow.|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.m_flow|sink1.m_flowSpec|sink1.m_flow_fixed|sink2.L|der.sink2.inlet.m_flow.|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.m_flow|sink2.m_flowSpec|sink2.m_flow_fixed|source.L|source.T0|source.T0_par|source.h0|source.h0_par|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|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",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.563e-06/1.563e-06, allocations: 0 / 0.5547 GB, free: 12.69 MB / 490.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.88e-05/2.036e-05, allocations: 6.25 kB / 0.5548 GB, free: 12.68 MB / 490.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater): time 0.03839/0.03841, allocations: 63.87 MB / 0.6171 GB, free: 12.59 MB / 0.5417 GB
Notification: Performance of NFInst.instExpressions: time 0.01563/0.05404, allocations: 19.87 MB / 0.6365 GB, free: 8.652 MB / 0.5573 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0005602/0.0546, allocations: 71.31 kB / 0.6366 GB, free: 8.582 MB / 0.5573 GB
Notification: Performance of NFTyping.typeComponents: time 0.001115/0.05572, allocations: 0.5895 MB / 0.6372 GB, free: 7.988 MB / 0.5573 GB
Notification: Performance of NFTyping.typeBindings: time 0.01281/0.06853, allocations: 7.518 MB / 0.6445 GB, free: 448 kB / 0.5573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.2928/0.3613, allocations: 1.351 MB / 0.6458 GB, free: 16.47 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.002322/0.3637, allocations: 1.725 MB / 0.6475 GB, free: 16.34 MB / 0.5573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003187/0.364, allocations: 164 kB / 0.6477 GB, free: 16.31 MB / 0.5573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.006378/0.3704, allocations: 5.772 MB / 0.6533 GB, free: 14.82 MB / 0.5573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004845/0.3708, allocations: 406.3 kB / 0.6537 GB, free: 14.76 MB / 0.5573 GB
Notification: Performance of NFPackage.collectConstants: time 7.762e-05/0.3709, allocations: 69.44 kB / 0.6538 GB, free: 14.76 MB / 0.5573 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01545/0.3864, allocations: 10.35 MB / 0.6639 GB, free: 14.69 MB / 0.5573 GB
Notification: Performance of NFScalarize.scalarize: time 0.0001379/0.3865, allocations: 192.4 kB / 0.6641 GB, free: 14.63 MB / 0.5573 GB
Notification: Performance of NFVerifyModel.verify: time 0.0004597/0.387, allocations: 355.7 kB / 0.6644 GB, free: 14.58 MB / 0.5573 GB
Notification: Performance of NFConvertDAE.convert: time 0.01453/0.4015, allocations: 9.029 MB / 0.6732 GB, free: 14.25 MB / 0.5573 GB
Notification: Performance of FrontEnd - DAE generated: time 4.939e-06/0.4015, allocations: 3.938 kB / 0.6732 GB, free: 14.25 MB / 0.5573 GB
Notification: Performance of FrontEnd: time 1.303e-06/0.4015, allocations: 0 / 0.6732 GB, free: 14.25 MB / 0.5573 GB
Notification: Performance of Transformations before backend: time 3.376e-05/0.4015, allocations: 1.156 kB / 0.6732 GB, free: 14.25 MB / 0.5573 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 202
 * Number of variables: 202
Notification: Performance of Generate backend data structure: time 0.006355/0.4079, allocations: 2.267 MB / 0.6754 GB, free: 13.09 MB / 0.5573 GB
Notification: Performance of prepare preOptimizeDAE: time 4.224e-05/0.4079, allocations: 9.344 kB / 0.6754 GB, free: 13.09 MB / 0.5573 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0008621/0.4088, allocations: 284.7 kB / 0.6757 GB, free: 13.02 MB / 0.5573 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001078/0.4099, allocations: 0.8213 MB / 0.6765 GB, free: 12.72 MB / 0.5573 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001096/0.41, allocations: 221.7 kB / 0.6767 GB, free: 12.54 MB / 0.5573 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 8.631e-05/0.4101, allocations: 83 kB / 0.6768 GB, free: 12.54 MB / 0.5573 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001241/0.4113, allocations: 0.9825 MB / 0.6778 GB, free: 12.33 MB / 0.5573 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.564e-05/0.4113, allocations: 3.188 kB / 0.6778 GB, free: 12.33 MB / 0.5573 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 4.112e-05/0.4114, allocations: 35.06 kB / 0.6778 GB, free: 12.33 MB / 0.5573 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.223e-05/0.4114, allocations: 18.66 kB / 0.6778 GB, free: 12.33 MB / 0.5573 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0009245/0.4123, allocations: 0.6878 MB / 0.6785 GB, free: 12.32 MB / 0.5573 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.002393/0.4147, allocations: 2.85 MB / 0.6813 GB, free: 10.85 MB / 0.5573 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.00091/0.4156, allocations: 0.5227 MB / 0.6818 GB, free: 10.82 MB / 0.5573 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0002271/0.4158, allocations: 194.2 kB / 0.682 GB, free: 10.81 MB / 0.5573 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.05644/0.4723, allocations: 34.89 MB / 0.716 GB, free: 7.016 MB / 0.573 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.048e-05/0.4723, allocations: 36.5 kB / 0.7161 GB, free: 6.977 MB / 0.573 GB
Notification: Performance of pre-optimization done (n=43): time 3.207e-06/0.4723, allocations: 0 / 0.7161 GB, free: 6.977 MB / 0.573 GB
Notification: Performance of matching and sorting (n=43): time 0.001492/0.4738, allocations: 0.7632 MB / 0.7168 GB, free: 6.371 MB / 0.573 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.189e-05/0.4738, allocations: 59.39 kB / 0.7169 GB, free: 6.301 MB / 0.573 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005393/0.4744, allocations: 0.6441 MB / 0.7175 GB, free: 5.793 MB / 0.573 GB
Notification: Performance of collectPreVariables (initialization): time 2.621e-05/0.4744, allocations: 36.95 kB / 0.7175 GB, free: 5.758 MB / 0.573 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002313/0.4746, allocations: 0.4897 MB / 0.718 GB, free: 5.426 MB / 0.573 GB
Notification: Performance of collectInitialBindings (initialization): time 8.295e-05/0.4747, allocations: 158.3 kB / 0.7182 GB, free: 5.293 MB / 0.573 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 9.403e-05/0.4748, allocations: 98.27 kB / 0.7183 GB, free: 5.227 MB / 0.573 GB
Notification: Performance of setup shared object (initialization): time 8.321e-05/0.4749, allocations: 329.8 kB / 0.7186 GB, free: 4.906 MB / 0.573 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0001724/0.4751, allocations: 129.2 kB / 0.7187 GB, free: 4.82 MB / 0.573 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.000224/0.4753, allocations: 255.8 kB / 0.719 GB, free: 4.57 MB / 0.573 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0004456/0.4757, allocations: 413.8 kB / 0.7193 GB, free: 4.242 MB / 0.573 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.158e-06/0.4757, allocations: 4 kB / 0.7193 GB, free: 4.238 MB / 0.573 GB
Notification: Performance of matching and sorting (n=58) (initialization): time 0.0005919/0.4763, allocations: 0.4982 MB / 0.7198 GB, free: 3.863 MB / 0.573 GB
Notification: Performance of prepare postOptimizeDAE: time 1.706e-05/0.4764, allocations: 8.5 kB / 0.7198 GB, free: 3.855 MB / 0.573 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 8.295e-06/0.4764, allocations: 4 kB / 0.7198 GB, free: 3.852 MB / 0.573 GB
Notification: Performance of postOpt tearingSystem (initialization): time 1.695e-05/0.4764, allocations: 8 kB / 0.7199 GB, free: 3.844 MB / 0.573 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002235/0.4766, allocations: 120.2 kB / 0.72 GB, free: 3.742 MB / 0.573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 8.917e-06/0.4766, allocations: 7.984 kB / 0.72 GB, free: 3.734 MB / 0.573 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004793/0.4771, allocations: 45.98 kB / 0.72 GB, free: 3.695 MB / 0.573 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 2.859e-05/0.4771, allocations: 27.36 kB / 0.72 GB, free: 3.676 MB / 0.573 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 17
 * Number of states: 0 ()
 * Number of discrete variables: 6 (source.outlet.state.phase,source2.outlet.state.phase,source1.outlet.state.phase,isothermalReference.outlet.state.phase,incompressibleFluid.outlet.state.phase,fullMedium.outlet.state.phase)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (58):
 * Single equations (assignments): 58
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of prepare postOptimizeDAE: time 0.0002452/0.4774, allocations: 219.1 kB / 0.7203 GB, free: 3.512 MB / 0.573 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 7.134e-05/0.4774, allocations: 87.44 kB / 0.7203 GB, free: 3.426 MB / 0.573 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001176/0.4786, allocations: 1.631 MB / 0.7219 GB, free: 2.332 MB / 0.573 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.002e-06/0.4786, allocations: 0 / 0.7219 GB, free: 2.332 MB / 0.573 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 3.967e-06/0.4786, allocations: 0 / 0.7219 GB, free: 2.332 MB / 0.573 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001827/0.4788, allocations: 148.9 kB / 0.7221 GB, free: 2.203 MB / 0.573 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 5.943e-05/0.4789, allocations: 27.03 kB / 0.7221 GB, free: 2.184 MB / 0.573 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001395/0.479, allocations: 22.78 kB / 0.7221 GB, free: 2.168 MB / 0.573 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 6.563e-05/0.4791, allocations: 40.83 kB / 0.7222 GB, free: 2.133 MB / 0.573 GB
Notification: Performance of postOpt createDAEmodeBDAE (simulation): time 0.0007542/0.4798, allocations: 0.8395 MB / 0.723 GB, free: 1.324 MB / 0.573 GB
Notification: Performance of postOpt symbolicJacobianDAE (simulation): time 0.00077/0.4806, allocations: 0.9805 MB / 0.7239 GB, free: 336 kB / 0.573 GB
Notification: Performance of postOpt setEvaluationStage (simulation): time 0.0002885/0.4809, allocations: 296.3 kB / 0.7242 GB, free: 44 kB / 0.573 GB
Notification: Performance of sorting global known variables: time 0.0004938/0.4814, allocations: 0.5754 MB / 0.7248 GB, free: 15.46 MB / 0.5886 GB
Notification: Performance of Backend: time 5.11e-07/0.4814, allocations: 0 / 0.7248 GB, free: 15.46 MB / 0.5886 GB
Notification: Performance of simCode: created initialization part: time 0.0117/0.4931, allocations: 2.855 MB / 0.7276 GB, free: 12.86 MB / 0.5886 GB
Notification: Performance of SimCode: time 0.002802/0.4959, allocations: 2.368 MB / 0.7299 GB, free: 10.47 MB / 0.5886 GB
Notification: Performance of Templates: time 0.066/0.5619, allocations: 70.82 MB / 0.799 GB, free: 4.055 MB / 0.6511 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 6.4169391030445695]