Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_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 0.001354/0.001354, allocations: 88.72 kB / 19.44 MB, free: 356 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 0.001679/0.001679, allocations: 157.7 kB / 22.75 MB, free: 1.684 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 1.512/1.512, allocations: 177.1 MB / 203.1 MB, free: 5.609 MB / 186.7 MB
"
[Timeout remaining time 178]
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 1.099/1.099, allocations: 118.6 MB / 378.2 MB, free: 1.496 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.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_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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.994e-06/1.994e-06, allocations: 0 / 482.9 MB, free: 8.215 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.992e-05/3.191e-05, allocations: 6.953 kB / 482.9 MB, free: 8.211 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater): time 0.08706/0.08709, allocations: 63.91 MB / 0.534 GB, free: 0.9492 MB / 458.7 MB
Notification: Performance of NFInst.instExpressions: time 0.03298/0.1201, allocations: 19.89 MB / 0.5534 GB, free: 13 MB / 490.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001245/0.1213, allocations: 71.31 kB / 0.5535 GB, free: 12.93 MB / 490.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.002026/0.1233, allocations: 0.5934 MB / 0.5541 GB, free: 12.33 MB / 490.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.02299/0.1463, allocations: 7.526 MB / 0.5614 GB, free: 4.77 MB / 490.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.004332/0.1507, allocations: 1.353 MB / 0.5628 GB, free: 3.41 MB / 490.7 MB
Notification: Performance of NFFlatten.flatten: time 0.002628/0.1533, allocations: 1.742 MB / 0.5645 GB, free: 1.66 MB / 490.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0004061/0.1537, allocations: 165.8 kB / 0.5646 GB, free: 1.484 MB / 490.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.01318/0.1669, allocations: 5.78 MB / 0.5703 GB, free: 11.62 MB / 0.4948 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0007596/0.1676, allocations: 402.7 kB / 0.5706 GB, free: 11.23 MB / 0.4948 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001266/0.1678, allocations: 68 kB / 0.5707 GB, free: 11.16 MB / 0.4948 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.02445/0.1922, allocations: 10.37 MB / 0.5808 GB, free: 0.7812 MB / 0.4948 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003863/0.1926, allocations: 191 kB / 0.581 GB, free: 0.5938 MB / 0.4948 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008842/0.1935, allocations: 367 kB / 0.5814 GB, free: 240 kB / 0.4948 GB
Notification: Performance of NFConvertDAE.convert: time 0.02219/0.2157, allocations: 9.041 MB / 0.5902 GB, free: 7.172 MB / 0.5105 GB
Notification: Performance of FrontEnd - DAE generated: time 5.44e-06/0.2157, allocations: 0 / 0.5902 GB, free: 7.172 MB / 0.5105 GB
Notification: Performance of FrontEnd: time 1.453e-06/0.2157, allocations: 4 kB / 0.5902 GB, free: 7.168 MB / 0.5105 GB
Notification: Performance of Transformations before backend: time 1.393e-05/0.2157, allocations: 0 / 0.5902 GB, free: 7.168 MB / 0.5105 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 0.006215/0.2219, allocations: 2.306 MB / 0.5924 GB, free: 4.82 MB / 0.5105 GB
Notification: Performance of prepare preOptimizeDAE: time 4.986e-05/0.222, allocations: 8.031 kB / 0.5925 GB, free: 4.812 MB / 0.5105 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001681/0.2236, allocations: 455.3 kB / 0.5929 GB, free: 4.367 MB / 0.5105 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001725/0.2254, allocations: 0.8414 MB / 0.5937 GB, free: 3.488 MB / 0.5105 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002434/0.2256, allocations: 228.7 kB / 0.5939 GB, free: 3.227 MB / 0.5105 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001457/0.2258, allocations: 88.38 kB / 0.594 GB, free: 3.141 MB / 0.5105 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002246/0.228, allocations: 0.9853 MB / 0.595 GB, free: 2.102 MB / 0.5105 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.837e-05/0.228, allocations: 0 / 0.595 GB, free: 2.102 MB / 0.5105 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 7.997e-05/0.2281, allocations: 32 kB / 0.595 GB, free: 2.07 MB / 0.5105 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.867e-05/0.2281, allocations: 20 kB / 0.595 GB, free: 2.051 MB / 0.5105 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001904/0.23, allocations: 0.6869 MB / 0.5957 GB, free: 1.363 MB / 0.5105 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.004454/0.2345, allocations: 2.869 MB / 0.5985 GB, free: 14.38 MB / 0.5261 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001657/0.2361, allocations: 0.522 MB / 0.599 GB, free: 13.85 MB / 0.5261 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004523/0.2366, allocations: 186.4 kB / 0.5992 GB, free: 13.67 MB / 0.5261 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.1588/0.3954, allocations: 34.83 MB / 0.6332 GB, free: 10.8 MB / 0.5573 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 6.595e-05/0.3955, allocations: 42.5 kB / 0.6332 GB, free: 10.75 MB / 0.5573 GB
Notification: Performance of pre-optimization done (n=43): time 2.565e-06/0.3955, allocations: 0 / 0.6332 GB, free: 10.75 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=43): time 0.002813/0.3983, allocations: 0.8188 MB / 0.634 GB, free: 9.922 MB / 0.5573 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 5.836e-05/0.3984, allocations: 59.41 kB / 0.6341 GB, free: 9.852 MB / 0.5573 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0009902/0.3994, allocations: 0.6693 MB / 0.6347 GB, free: 9.172 MB / 0.5573 GB
Notification: Performance of collectPreVariables (initialization): time 5.197e-05/0.3994, allocations: 37.7 kB / 0.6348 GB, free: 9.129 MB / 0.5573 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0004954/0.3999, allocations: 0.5079 MB / 0.6353 GB, free: 8.613 MB / 0.5573 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001776/0.4001, allocations: 154.7 kB / 0.6354 GB, free: 8.461 MB / 0.5573 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.000179/0.4003, allocations: 94.14 kB / 0.6355 GB, free: 8.363 MB / 0.5573 GB
Notification: Performance of setup shared object (initialization): time 0.0002051/0.4005, allocations: 326 kB / 0.6358 GB, free: 8.039 MB / 0.5573 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003535/0.4008, allocations: 120.9 kB / 0.6359 GB, free: 7.922 MB / 0.5573 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004885/0.4013, allocations: 259.4 kB / 0.6362 GB, free: 7.613 MB / 0.5573 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0008846/0.4022, allocations: 417.8 kB / 0.6366 GB, free: 7.152 MB / 0.5573 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.947e-06/0.4022, allocations: 0 / 0.6366 GB, free: 7.152 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=58) (initialization): time 0.001274/0.4035, allocations: 0.5351 MB / 0.6371 GB, free: 6.609 MB / 0.5573 GB
Notification: Performance of prepare postOptimizeDAE: time 2.386e-05/0.4035, allocations: 8 kB / 0.6371 GB, free: 6.602 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.489e-05/0.4035, allocations: 4 kB / 0.6371 GB, free: 6.598 MB / 0.5573 GB
Notification: Performance of postOpt tearingSystem (initialization): time 2.97e-05/0.4035, allocations: 4 kB / 0.6371 GB, free: 6.594 MB / 0.5573 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004747/0.404, allocations: 111.9 kB / 0.6372 GB, free: 6.484 MB / 0.5573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.841e-05/0.404, allocations: 8.406 kB / 0.6372 GB, free: 6.477 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.00036/0.4044, allocations: 51.72 kB / 0.6373 GB, free: 6.426 MB / 0.5573 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.327e-05/0.4045, allocations: 23.98 kB / 0.6373 GB, free: 6.402 MB / 0.5573 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 0.0004121/0.4049, allocations: 221.6 kB / 0.6375 GB, free: 6.176 MB / 0.5573 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002045/0.4051, allocations: 103.4 kB / 0.6376 GB, free: 6.074 MB / 0.5573 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002508/0.4076, allocations: 1.644 MB / 0.6392 GB, free: 4.426 MB / 0.5573 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 3.723e-05/0.4076, allocations: 19.98 kB / 0.6392 GB, free: 4.406 MB / 0.5573 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 7.754e-06/0.4076, allocations: 3.984 kB / 0.6393 GB, free: 4.402 MB / 0.5573 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.954e-06/0.4076, allocations: 0 / 0.6393 GB, free: 4.402 MB / 0.5573 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.004237/0.4119, allocations: 2.422 MB / 0.6416 GB, free: 1.941 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 7.924e-06/0.4119, allocations: 0 / 0.6416 GB, free: 1.941 MB / 0.5573 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.000377/0.4123, allocations: 83.89 kB / 0.6417 GB, free: 1.859 MB / 0.5573 GB
Notification: Performance of postOpt tearingSystem (simulation): time 5.851e-06/0.4123, allocations: 4 kB / 0.6417 GB, free: 1.855 MB / 0.5573 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.851e-05/0.4123, allocations: 12 kB / 0.6417 GB, free: 1.844 MB / 0.5573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 7.023e-06/0.4123, allocations: 4 kB / 0.6417 GB, free: 1.84 MB / 0.5573 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.272e-06/0.4123, allocations: 0 / 0.6417 GB, free: 1.84 MB / 0.5573 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.001642/0.4139, allocations: 0.9263 MB / 0.6426 GB, free: 0.8945 MB / 0.5573 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.000326/0.4143, allocations: 147 kB / 0.6428 GB, free: 0.75 MB / 0.5573 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001015/0.4144, allocations: 23.78 kB / 0.6428 GB, free: 0.7266 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0003001/0.4147, allocations: 27.98 kB / 0.6428 GB, free: 0.6992 MB / 0.5573 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001058/0.4148, allocations: 36.36 kB / 0.6428 GB, free: 0.6641 MB / 0.5573 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 3.223e-05/0.4148, allocations: 16 kB / 0.6429 GB, free: 0.6484 MB / 0.5573 GB
Notification: Performance of sorting global known variables: time 0.0009039/0.4157, allocations: 0.592 MB / 0.6434 GB, free: 48 kB / 0.5573 GB
Notification: Performance of sort global known variables: time 8e-08/0.4157, allocations: 0 / 0.6434 GB, free: 48 kB / 0.5573 GB
Notification: Performance of remove unused functions: time 0.232/0.6477, allocations: 1.64 MB / 0.645 GB, free: 163.7 MB / 0.5573 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 0 ()
 * Number of discrete variables: 10 ($cse2.phase,$cse2.region,$cse4.phase,$cse4.region,$cse5.phase,$cse5.region,$cse6.phase,$cse6.region,$cse9.phase,$cse9.region)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (50):
 * Single equations (assignments): 45
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 5
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of Backend phase and start with SimCode phase: time 0.006995/0.6547, allocations: 2.07 MB / 0.6471 GB, free: 163.7 MB / 0.5573 GB
Notification: Performance of simCode: created initialization part: time 0.001015/0.6557, allocations: 0.4928 MB / 0.6475 GB, free: 163.6 MB / 0.5573 GB
Notification: Performance of simCode: created event and clocks part: time 3.797e-06/0.6557, allocations: 0 / 0.6475 GB, free: 163.6 MB / 0.5573 GB
Notification: Performance of simCode: created simulation system equations: time 0.0004287/0.6561, allocations: 315.3 kB / 0.6478 GB, free: 163.6 MB / 0.5573 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001799/0.6579, allocations: 399.5 kB / 0.6482 GB, free: 163.6 MB / 0.5573 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.002636/0.6605, allocations: 2.055 MB / 0.6502 GB, free: 162.5 MB / 0.5573 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0004293/0.661, allocations: 0.5383 MB / 0.6508 GB, free: 162.4 MB / 0.5573 GB
Notification: Performance of simCode: alias equations: time 0.0004513/0.6614, allocations: 250.8 kB / 0.651 GB, free: 162.4 MB / 0.5573 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001428/0.6616, allocations: 81.53 kB / 0.6511 GB, free: 162.3 MB / 0.5573 GB
Notification: Performance of SimCode: time 8.51e-07/0.6616, allocations: 0 / 0.6511 GB, free: 162.3 MB / 0.5573 GB
Notification: Performance of Templates: time 0.07208/0.7336, allocations: 63.27 MB / 0.7129 GB, free: 117.1 MB / 0.5573 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_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_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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 10.461959087988362]