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 0.001859/0.001859, allocations: 78.81 kB / 19.18 MB, free: 2.516 MB / 14.72 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 0.0026/0.0026, allocations: 162.7 kB / 22.46 MB, free: 5.375 MB / 14.72 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 1.45/1.45, allocations: 177.1 MB / 202.8 MB, free: 9.168 MB / 190.1 MB
"
[Timeout remaining time 178]
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 0.9634/0.9634, allocations: 116.1 MB / 375.2 MB, free: 7.523 MB / 350.1 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 1.743e-06/1.743e-06, allocations: 3.938 kB / 0.5538 GB, free: 13.74 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 3.421e-05/3.595e-05, allocations: 2.281 kB / 0.5538 GB, free: 13.74 MB / 478.1 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater): time 0.07699/0.07703, allocations: 63.87 MB / 0.6161 GB, free: 13.66 MB / 0.5294 GB
Notification: Performance of NFInst.instExpressions: time 0.03246/0.1095, allocations: 19.87 MB / 0.6356 GB, free: 9.715 MB / 0.545 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001329/0.1108, allocations: 67.38 kB / 0.6356 GB, free: 9.648 MB / 0.545 GB
Notification: Performance of NFTyping.typeComponents: time 0.002395/0.1132, allocations: 0.5972 MB / 0.6362 GB, free: 9.047 MB / 0.545 GB
Notification: Performance of NFTyping.typeBindings: time 0.02526/0.1385, allocations: 7.53 MB / 0.6436 GB, free: 1.508 MB / 0.545 GB
Notification: Performance of NFTyping.typeClassSections: time 0.004279/0.1428, allocations: 1.349 MB / 0.6449 GB, free: 156 kB / 0.545 GB
Notification: Performance of NFFlatten.flatten: time 0.003056/0.1458, allocations: 1.735 MB / 0.6466 GB, free: 14.41 MB / 0.5606 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0005636/0.1464, allocations: 169.6 kB / 0.6467 GB, free: 14.23 MB / 0.5606 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.01618/0.1626, allocations: 5.759 MB / 0.6524 GB, free: 8.395 MB / 0.5606 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001094/0.1637, allocations: 414.7 kB / 0.6527 GB, free: 7.988 MB / 0.5606 GB
Notification: Performance of NFPackage.collectConstants: time 0.0002891/0.1639, allocations: 68 kB / 0.6528 GB, free: 7.922 MB / 0.5606 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.02356/0.1875, allocations: 10.36 MB / 0.6629 GB, free: 13.55 MB / 0.5762 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003613/0.1879, allocations: 191 kB / 0.6631 GB, free: 13.36 MB / 0.5762 GB
Notification: Performance of NFVerifyModel.verify: time 0.0008809/0.1887, allocations: 363 kB / 0.6635 GB, free: 13.01 MB / 0.5762 GB
Notification: Performance of NFConvertDAE.convert: time 0.02279/0.2115, allocations: 9.007 MB / 0.6723 GB, free: 3.98 MB / 0.5762 GB
Notification: Performance of FrontEnd - DAE generated: time 8.556e-06/0.2115, allocations: 4 kB / 0.6723 GB, free: 3.977 MB / 0.5762 GB
Notification: Performance of FrontEnd: time 1.683e-06/0.2115, allocations: 0 / 0.6723 GB, free: 3.977 MB / 0.5762 GB
Notification: Performance of Transformations before backend: time 6.212e-05/0.2116, allocations: 0 / 0.6723 GB, free: 3.977 MB / 0.5762 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 0.007579/0.2192, allocations: 2.283 MB / 0.6745 GB, free: 1.652 MB / 0.5762 GB
Notification: Performance of prepare preOptimizeDAE: time 4.736e-05/0.2192, allocations: 8.031 kB / 0.6745 GB, free: 1.645 MB / 0.5762 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001646/0.2209, allocations: 287.9 kB / 0.6748 GB, free: 1.363 MB / 0.5762 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001717/0.2226, allocations: 0.7453 MB / 0.6755 GB, free: 0.582 MB / 0.5762 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.000242/0.2228, allocations: 228.3 kB / 0.6757 GB, free: 328 kB / 0.5762 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001473/0.223, allocations: 76 kB / 0.6758 GB, free: 252 kB / 0.5762 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.002311/0.2253, allocations: 0.985 MB / 0.6767 GB, free: 15.21 MB / 0.5919 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.461e-05/0.2253, allocations: 7.938 kB / 0.6768 GB, free: 15.2 MB / 0.5919 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 8.151e-05/0.2254, allocations: 36 kB / 0.6768 GB, free: 15.16 MB / 0.5919 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.051e-05/0.2254, allocations: 20 kB / 0.6768 GB, free: 15.14 MB / 0.5919 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001923/0.2273, allocations: 0.6791 MB / 0.6775 GB, free: 14.46 MB / 0.5919 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.004247/0.2316, allocations: 2.822 MB / 0.6802 GB, free: 11.52 MB / 0.5919 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001647/0.2332, allocations: 0.5268 MB / 0.6807 GB, free: 10.99 MB / 0.5919 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004237/0.2337, allocations: 189.9 kB / 0.6809 GB, free: 10.8 MB / 0.5919 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.3894/0.623, allocations: 34.81 MB / 0.7149 GB, free: 123.4 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.837e-05/0.6231, allocations: 38.56 kB / 0.715 GB, free: 123.3 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=43): time 2.395e-06/0.6231, allocations: 0 / 0.715 GB, free: 123.3 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=43): time 0.00218/0.6252, allocations: 0.754 MB / 0.7157 GB, free: 122.6 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.622e-05/0.6253, allocations: 63.06 kB / 0.7158 GB, free: 122.5 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.000554/0.6258, allocations: 0.6501 MB / 0.7164 GB, free: 121.9 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 2.616e-05/0.6259, allocations: 37.7 kB / 0.7164 GB, free: 121.8 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.000211/0.6261, allocations: 0.4923 MB / 0.7169 GB, free: 121.4 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 7.463e-05/0.6261, allocations: 145.5 kB / 0.717 GB, free: 121.3 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.000116/0.6263, allocations: 106.1 kB / 0.7171 GB, free: 121.2 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 5.149e-05/0.6263, allocations: 325.7 kB / 0.7175 GB, free: 120.9 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0002539/0.6266, allocations: 128.9 kB / 0.7176 GB, free: 120.8 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0002935/0.6269, allocations: 251.3 kB / 0.7178 GB, free: 120.5 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0005859/0.6274, allocations: 412.6 kB / 0.7182 GB, free: 120 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.116e-06/0.6274, allocations: 1.688 kB / 0.7182 GB, free: 120 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=58) (initialization): time 0.0007973/0.6282, allocations: 0.5117 MB / 0.7187 GB, free: 119.5 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 1.741e-05/0.6283, allocations: 11.83 kB / 0.7187 GB, free: 119.5 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 7.674e-06/0.6283, allocations: 4 kB / 0.7187 GB, free: 119.5 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 2.086e-05/0.6283, allocations: 4 kB / 0.7187 GB, free: 119.5 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0003834/0.6287, allocations: 116.3 kB / 0.7188 GB, free: 119.4 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.029e-05/0.6287, allocations: 8 kB / 0.7188 GB, free: 119.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0003112/0.629, allocations: 49.31 kB / 0.7189 GB, free: 119.3 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.924e-05/0.629, allocations: 22.27 kB / 0.7189 GB, free: 119.3 MB / 0.5919 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 0.0002544/0.6293, allocations: 225.2 kB / 0.7191 GB, free: 119.1 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 9.074e-05/0.6294, allocations: 87.44 kB / 0.7192 GB, free: 119 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001424/0.6308, allocations: 1.634 MB / 0.7208 GB, free: 117.4 MB / 0.5919 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 1.7e-05/0.6308, allocations: 19.97 kB / 0.7208 GB, free: 117.4 MB / 0.5919 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.689e-06/0.6308, allocations: 0 / 0.7208 GB, free: 117.4 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.903e-06/0.6308, allocations: 3.984 kB / 0.7208 GB, free: 117.4 MB / 0.5919 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.00222/0.633, allocations: 2.404 MB / 0.7232 GB, free: 115 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.609e-06/0.6331, allocations: 0 / 0.7232 GB, free: 115 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0002964/0.6333, allocations: 91.88 kB / 0.7233 GB, free: 114.9 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (simulation): time 4.017e-06/0.6334, allocations: 0 / 0.7233 GB, free: 114.9 MB / 0.5919 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.311e-05/0.6334, allocations: 14.12 kB / 0.7233 GB, free: 114.9 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 3.647e-06/0.6334, allocations: 7.938 kB / 0.7233 GB, free: 114.9 MB / 0.5919 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.262e-06/0.6334, allocations: 0 / 0.7233 GB, free: 114.9 MB / 0.5919 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0009139/0.6343, allocations: 0.9026 MB / 0.7242 GB, free: 113.9 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001733/0.6345, allocations: 141.5 kB / 0.7243 GB, free: 113.8 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 8.459e-05/0.6346, allocations: 30.8 kB / 0.7243 GB, free: 113.8 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002692/0.6348, allocations: 31.86 kB / 0.7244 GB, free: 113.8 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 7.719e-05/0.6349, allocations: 35.2 kB / 0.7244 GB, free: 113.7 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.455e-05/0.6349, allocations: 19.98 kB / 0.7244 GB, free: 113.7 MB / 0.5919 GB
Notification: Performance of sorting global known variables: time 0.000487/0.6354, allocations: 0.5715 MB / 0.725 GB, free: 113.1 MB / 0.5919 GB
Notification: Performance of sort global known variables: time 9e-08/0.6354, allocations: 0 / 0.725 GB, free: 113.1 MB / 0.5919 GB
Notification: Performance of remove unused functions: time 0.0035/0.6389, allocations: 1.641 MB / 0.7266 GB, free: 111.7 MB / 0.5919 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 0.005937/0.6448, allocations: 2.077 MB / 0.7286 GB, free: 109.8 MB / 0.5919 GB
Notification: Performance of simCode: created initialization part: time 0.0009193/0.6458, allocations: 499.5 kB / 0.7291 GB, free: 109.4 MB / 0.5919 GB
Notification: Performance of simCode: created event and clocks part: time 3.707e-06/0.6458, allocations: 0 / 0.7291 GB, free: 109.4 MB / 0.5919 GB
Notification: Performance of simCode: created simulation system equations: time 0.0003835/0.6462, allocations: 321.3 kB / 0.7294 GB, free: 109 MB / 0.5919 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001736/0.6479, allocations: 356.2 kB / 0.7297 GB, free: 108.7 MB / 0.5919 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.002515/0.6504, allocations: 1.979 MB / 0.7317 GB, free: 106.7 MB / 0.5919 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0003597/0.6508, allocations: 0.5267 MB / 0.7322 GB, free: 106.2 MB / 0.5919 GB
Notification: Performance of simCode: alias equations: time 0.000458/0.6512, allocations: 248.8 kB / 0.7324 GB, free: 105.9 MB / 0.5919 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001589/0.6514, allocations: 76.48 kB / 0.7325 GB, free: 105.9 MB / 0.5919 GB
Notification: Performance of SimCode: time 9.62e-07/0.6514, allocations: 0 / 0.7325 GB, free: 105.9 MB / 0.5919 GB
Notification: Performance of Templates: time 0.06507/0.7164, allocations: 62.62 MB / 0.7936 GB, free: 43.55 MB / 0.5919 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: 10.167501244693995]