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 0.001415/0.001415, allocations: 109.5 kB / 18.95 MB, free: 1.18 MB / 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 0.002565/0.002565, allocations: 216.7 kB / 22.24 MB, free: 3.699 MB / 13.93 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 1.559/1.559, allocations: 230.6 MB / 256 MB, free: 9.602 MB / 202.7 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 1.127/1.127, allocations: 154.1 MB / 466.6 MB, free: 3.301 MB / 362.7 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 0.002748/0.002748, allocations: 83.88 kB / 0.6443 GB, free: 27.79 MB / 490.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.1576/0.1603, allocations: 88.77 MB / 0.731 GB, free: 2.82 MB / 0.5417 GB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater): time 0.08738/0.2477, allocations: 64.43 MB / 0.7939 GB, free: 2.176 MB / 0.6042 GB
Notification: Performance of NFInst.instExpressions: time 0.03183/0.2795, allocations: 19.88 MB / 0.8133 GB, free: 14.23 MB / 0.6355 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001162/0.2807, allocations: 67.31 kB / 0.8134 GB, free: 14.17 MB / 0.6355 GB
Notification: Performance of NFTyping.typeComponents: time 0.001874/0.2826, allocations: 0.5936 MB / 0.8139 GB, free: 13.57 MB / 0.6355 GB
Notification: Performance of NFTyping.typeBindings: time 0.02134/0.3039, allocations: 7.428 MB / 0.8212 GB, free: 6.137 MB / 0.6355 GB
Notification: Performance of NFTyping.typeClassSections: time 0.004167/0.3081, allocations: 1.322 MB / 0.8225 GB, free: 4.809 MB / 0.6355 GB
Notification: Performance of NFFlatten.flatten: time 0.002789/0.3109, allocations: 1.673 MB / 0.8241 GB, free: 3.129 MB / 0.6355 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003994/0.3113, allocations: 157.8 kB / 0.8243 GB, free: 2.953 MB / 0.6355 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.3561/0.6674, allocations: 5.511 MB / 0.8297 GB, free: 12.24 MB / 0.6355 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001178/0.6685, allocations: 0.4939 MB / 0.8301 GB, free: 12.24 MB / 0.6355 GB
Notification: Performance of NFPackage.collectConstants: time 0.0002189/0.6688, allocations: 74.34 kB / 0.8302 GB, free: 12.23 MB / 0.6355 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.02277/0.6915, allocations: 10.32 MB / 0.8403 GB, free: 12.21 MB / 0.6355 GB
Notification: Performance of NFScalarize.scalarize: time 0.000351/0.6919, allocations: 191.4 kB / 0.8405 GB, free: 12.21 MB / 0.6355 GB
Notification: Performance of NFVerifyModel.verify: time 0.0006809/0.6926, allocations: 452.6 kB / 0.8409 GB, free: 12.21 MB / 0.6355 GB
Notification: Performance of NFConvertDAE.convert: time 0.0192/0.7118, allocations: 7.452 MB / 0.8482 GB, free: 11.85 MB / 0.6355 GB
Notification: Performance of FrontEnd - DAE generated: time 6.352e-06/0.7118, allocations: 1.188 kB / 0.8482 GB, free: 11.85 MB / 0.6355 GB
Notification: Performance of FrontEnd: time 1.643e-06/0.7118, allocations: 4 kB / 0.8482 GB, free: 11.84 MB / 0.6355 GB
Notification: Performance of Transformations before backend: time 1.715e-05/0.7118, allocations: 0 / 0.8482 GB, free: 11.84 MB / 0.6355 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 0.006744/0.7185, allocations: 2.321 MB / 0.8504 GB, free: 10.68 MB / 0.6355 GB
Notification: Performance of prepare preOptimizeDAE: time 3.81e-05/0.7186, allocations: 9.906 kB / 0.8505 GB, free: 10.68 MB / 0.6355 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001303/0.7199, allocations: 279.9 kB / 0.8507 GB, free: 10.61 MB / 0.6355 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001544/0.7214, allocations: 0.7839 MB / 0.8515 GB, free: 10.3 MB / 0.6355 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.000151/0.7216, allocations: 223.3 kB / 0.8517 GB, free: 10.12 MB / 0.6355 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001176/0.7217, allocations: 82.94 kB / 0.8518 GB, free: 10.11 MB / 0.6355 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001891/0.7236, allocations: 0.9853 MB / 0.8527 GB, free: 9.91 MB / 0.6355 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.346e-05/0.7236, allocations: 5.5 kB / 0.8527 GB, free: 9.906 MB / 0.6355 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 6.674e-05/0.7237, allocations: 33.94 kB / 0.8528 GB, free: 9.906 MB / 0.6355 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.884e-05/0.7237, allocations: 20.31 kB / 0.8528 GB, free: 9.906 MB / 0.6355 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001657/0.7253, allocations: 0.6839 MB / 0.8535 GB, free: 9.906 MB / 0.6355 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003084/0.7284, allocations: 2.834 MB / 0.8562 GB, free: 8.43 MB / 0.6355 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001373/0.7298, allocations: 0.5305 MB / 0.8568 GB, free: 8.398 MB / 0.6355 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0003769/0.7302, allocations: 186.3 kB / 0.8569 GB, free: 8.391 MB / 0.6355 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.1194/0.8496, allocations: 34.83 MB / 0.8909 GB, free: 9.883 MB / 0.6511 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.935e-05/0.8496, allocations: 40.94 kB / 0.891 GB, free: 9.84 MB / 0.6511 GB
Notification: Performance of pre-optimization done (n=43): time 2.044e-06/0.8497, allocations: 4 kB / 0.891 GB, free: 9.836 MB / 0.6511 GB
Notification: Performance of matching and sorting (n=43): time 0.002697/0.8523, allocations: 0.7574 MB / 0.8917 GB, free: 9.234 MB / 0.6511 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 5.436e-05/0.8524, allocations: 55.41 kB / 0.8918 GB, free: 9.168 MB / 0.6511 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001044/0.8534, allocations: 0.6788 MB / 0.8924 GB, free: 8.629 MB / 0.6511 GB
Notification: Performance of collectPreVariables (initialization): time 4.504e-05/0.8535, allocations: 35.98 kB / 0.8925 GB, free: 8.598 MB / 0.6511 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0004137/0.8539, allocations: 0.5065 MB / 0.893 GB, free: 8.258 MB / 0.6511 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001772/0.8541, allocations: 156.2 kB / 0.8931 GB, free: 8.125 MB / 0.6511 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001655/0.8542, allocations: 99.02 kB / 0.8932 GB, free: 8.059 MB / 0.6511 GB
Notification: Performance of setup shared object (initialization): time 0.0001879/0.8544, allocations: 328.9 kB / 0.8935 GB, free: 7.738 MB / 0.6511 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003304/0.8548, allocations: 129.9 kB / 0.8937 GB, free: 7.652 MB / 0.6511 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004605/0.8552, allocations: 246 kB / 0.8939 GB, free: 7.406 MB / 0.6511 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.001057/0.8563, allocations: 430.4 kB / 0.8943 GB, free: 7.07 MB / 0.6511 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.148e-06/0.8563, allocations: 0 / 0.8943 GB, free: 7.07 MB / 0.6511 GB
Notification: Performance of matching and sorting (n=58) (initialization): time 0.001169/0.8575, allocations: 0.5097 MB / 0.8948 GB, free: 6.688 MB / 0.6511 GB
Notification: Performance of prepare postOptimizeDAE: time 2.077e-05/0.8575, allocations: 4 kB / 0.8948 GB, free: 6.684 MB / 0.6511 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 8.115e-06/0.8575, allocations: 4 kB / 0.8948 GB, free: 6.68 MB / 0.6511 GB
Notification: Performance of postOpt tearingSystem (initialization): time 2.471e-05/0.8575, allocations: 8 kB / 0.8948 GB, free: 6.672 MB / 0.6511 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004648/0.858, allocations: 109 kB / 0.8949 GB, free: 6.574 MB / 0.6511 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 2.119e-05/0.858, allocations: 13.95 kB / 0.8949 GB, free: 6.562 MB / 0.6511 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.000411/0.8584, allocations: 43.08 kB / 0.895 GB, free: 6.527 MB / 0.6511 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.341e-05/0.8585, allocations: 27.67 kB / 0.895 GB, free: 6.504 MB / 0.6511 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 0.0003672/0.8588, allocations: 219.1 kB / 0.8952 GB, free: 6.344 MB / 0.6511 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001912/0.859, allocations: 94.67 kB / 0.8953 GB, free: 6.254 MB / 0.6511 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002193/0.8612, allocations: 1.627 MB / 0.8969 GB, free: 5.168 MB / 0.6511 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 2.17e-05/0.8612, allocations: 23.59 kB / 0.8969 GB, free: 5.152 MB / 0.6511 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 1.079e-05/0.8612, allocations: 4 kB / 0.8969 GB, free: 5.148 MB / 0.6511 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.873e-06/0.8613, allocations: 0.875 kB / 0.8969 GB, free: 5.148 MB / 0.6511 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.003438/0.8647, allocations: 2.411 MB / 0.8993 GB, free: 3.523 MB / 0.6511 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 5.7e-06/0.8647, allocations: 3.938 kB / 0.8993 GB, free: 3.52 MB / 0.6511 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0003591/0.8651, allocations: 79.73 kB / 0.8993 GB, free: 3.449 MB / 0.6511 GB
Notification: Performance of postOpt tearingSystem (simulation): time 9.878e-06/0.8651, allocations: 8 kB / 0.8994 GB, free: 3.441 MB / 0.6511 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.49e-05/0.8651, allocations: 11.75 kB / 0.8994 GB, free: 3.438 MB / 0.6511 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 5.871e-06/0.8651, allocations: 3.938 kB / 0.8994 GB, free: 3.434 MB / 0.6511 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.563e-06/0.8651, allocations: 0 / 0.8994 GB, free: 3.434 MB / 0.6511 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.001399/0.8665, allocations: 0.9092 MB / 0.9003 GB, free: 2.734 MB / 0.6511 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0003212/0.8668, allocations: 147.8 kB / 0.9004 GB, free: 2.605 MB / 0.6511 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001196/0.8669, allocations: 29.22 kB / 0.9004 GB, free: 2.586 MB / 0.6511 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002956/0.8672, allocations: 22.67 kB / 0.9004 GB, free: 2.57 MB / 0.6511 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 9.141e-05/0.8673, allocations: 39.73 kB / 0.9005 GB, free: 2.535 MB / 0.6511 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 3.314e-05/0.8674, allocations: 21.97 kB / 0.9005 GB, free: 2.523 MB / 0.6511 GB
Notification: Performance of sorting global known variables: time 0.0008435/0.8682, allocations: 0.5876 MB / 0.9011 GB, free: 2.07 MB / 0.6511 GB
Notification: Performance of sort global known variables: time 7e-08/0.8682, allocations: 0 / 0.9011 GB, free: 2.07 MB / 0.6511 GB
Notification: Performance of remove unused functions: time 0.006202/0.8744, allocations: 1.643 MB / 0.9027 GB, free: 0.5117 MB / 0.6511 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 0.0102/0.8846, allocations: 1.873 MB / 0.9045 GB, free: 14.86 MB / 0.6667 GB
Notification: Performance of simCode: created initialization part: time 0.001204/0.8858, allocations: 0.4929 MB / 0.905 GB, free: 14.52 MB / 0.6667 GB
Notification: Performance of simCode: created event and clocks part: time 3.637e-06/0.8858, allocations: 1 kB / 0.905 GB, free: 14.52 MB / 0.6667 GB
Notification: Performance of simCode: created simulation system equations: time 0.0005532/0.8864, allocations: 313.4 kB / 0.9053 GB, free: 14.3 MB / 0.6667 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.002095/0.8885, allocations: 387.2 kB / 0.9057 GB, free: 14.04 MB / 0.6667 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.003944/0.8924, allocations: 2.041 MB / 0.9077 GB, free: 12.18 MB / 0.6667 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.000693/0.8931, allocations: 0.5412 MB / 0.9082 GB, free: 11.62 MB / 0.6667 GB
Notification: Performance of simCode: alias equations: time 0.0006457/0.8937, allocations: 246.4 kB / 0.9084 GB, free: 11.38 MB / 0.6667 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001926/0.8939, allocations: 76.2 kB / 0.9085 GB, free: 11.32 MB / 0.6667 GB
Notification: Performance of SimCode: time 1.252e-06/0.8939, allocations: 0 / 0.9085 GB, free: 11.32 MB / 0.6667 GB
Notification: Performance of Templates: time 0.1129/1.007, allocations: 64.61 MB / 0.9716 GB, free: 11.24 MB / 0.7292 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/jenkins1/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: 11.339418106945232]