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 0.001326/0.001326, allocations: 80.94 kB / 19.94 MB, free: 4.543 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001619/0.001619, allocations: 177.4 kB / 23.36 MB, free: 1.129 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.081/1.081, allocations: 177.1 MB / 203.8 MB, free: 5.477 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.7109/0.7109, allocations: 118.7 MB / 378.9 MB, free: 1.355 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|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.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.d|fullMedium.adiabaticModel.state_in.h|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.state_in.phase|fullMedium.adiabaticModel.w_t|fullMedium.adiabaticModel.w_t_is|fullMedium.assertionLevel|fullMedium.clip_p_out|fullMedium.dh|fullMedium.dp|fullMedium.dp_fixed|fullMedium.dp_nom|fullMedium.dp_start|fullMedium.dr_corr|fullMedium.etaSpec|fullMedium.eta_actual|fullMedium.eta_fixed|fullMedium.eta_is|fullMedium.h_in|fullMedium.h_out|fullMedium.initM_flow|der.fullMedium.inlet.m_flow.|fullMedium.inlet.m_flow|fullMedium.inlet.r|fullMedium.inlet.state.T|fullMedium.inlet.state.d|fullMedium.inlet.state.h|fullMedium.inlet.state.p|fullMedium.inlet.state.phase|fullMedium.m_acceleration_0|fullMedium.m_flow|fullMedium.m_flowStateSelect|fullMedium.m_flow_0|fullMedium.outlet.m_flow|fullMedium.outlet.r|fullMedium.outlet.state.T|fullMedium.outlet.state.d|fullMedium.outlet.state.h|fullMedium.outlet.state.p|fullMedium.outlet.state.phase|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletSpec_prescribed|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.TC|incompressibleFluid.adiabaticModel.T_in|incompressibleFluid.adiabaticModel.T_out_is|incompressibleFluid.adiabaticModel.assertionLevel|incompressibleFluid.adiabaticModel.deltaDensityRel|incompressibleFluid.adiabaticModel.eta_is|incompressibleFluid.adiabaticModel.h_in|incompressibleFluid.adiabaticModel.h_out|incompressibleFluid.adiabaticModel.isDensityWithinTol|incompressibleFluid.adiabaticModel.p_out|incompressibleFluid.adiabaticModel.relTolDensity|incompressibleFluid.adiabaticModel.rho_in|incompressibleFluid.adiabaticModel.rho_out|incompressibleFluid.adiabaticModel.state_in.T|incompressibleFluid.adiabaticModel.state_in.d|incompressibleFluid.adiabaticModel.state_in.h|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.state_in.phase|incompressibleFluid.adiabaticModel.w_t|incompressibleFluid.adiabaticModel.w_t_is|incompressibleFluid.assertionLevel|incompressibleFluid.clip_p_out|incompressibleFluid.dh|incompressibleFluid.dp|incompressibleFluid.dp_fixed|incompressibleFluid.dp_nom|incompressibleFluid.dp_start|incompressibleFluid.dr_corr|incompressibleFluid.etaSpec|incompressibleFluid.eta_actual|incompressibleFluid.eta_fixed|incompressibleFluid.eta_is|incompressibleFluid.h_in|incompressibleFluid.h_out|incompressibleFluid.initM_flow|der.incompressibleFluid.inlet.m_flow.|incompressibleFluid.inlet.m_flow|incompressibleFluid.inlet.r|incompressibleFluid.inlet.state.T|incompressibleFluid.inlet.state.d|incompressibleFluid.inlet.state.h|incompressibleFluid.inlet.state.p|incompressibleFluid.inlet.state.phase|incompressibleFluid.m_acceleration_0|incompressibleFluid.m_flow|incompressibleFluid.m_flowStateSelect|incompressibleFluid.m_flow_0|incompressibleFluid.outlet.m_flow|incompressibleFluid.outlet.r|incompressibleFluid.outlet.state.T|incompressibleFluid.outlet.state.d|incompressibleFluid.outlet.state.h|incompressibleFluid.outlet.state.p|incompressibleFluid.outlet.state.phase|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletSpec_prescribed|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|isothermalReference.L|isothermalReference.P|isothermalReference.P_nom|isothermalReference.TC|isothermalReference.adiabaticModel.T_in|isothermalReference.adiabaticModel.T_out_is|isothermalReference.adiabaticModel.assertionLevel|isothermalReference.adiabaticModel.deltaDensityRel|isothermalReference.adiabaticModel.eta_is|isothermalReference.adiabaticModel.h_in|isothermalReference.adiabaticModel.h_out|isothermalReference.adiabaticModel.h_out_is|isothermalReference.adiabaticModel.isDensityWithinTol|isothermalReference.adiabaticModel.p_out|isothermalReference.adiabaticModel.relTolDensity|isothermalReference.adiabaticModel.rho_in|isothermalReference.adiabaticModel.rho_out|isothermalReference.adiabaticModel.state_in.T|isothermalReference.adiabaticModel.state_in.d|isothermalReference.adiabaticModel.state_in.h|isothermalReference.adiabaticModel.state_in.p|isothermalReference.adiabaticModel.state_in.phase|isothermalReference.adiabaticModel.w_t|isothermalReference.adiabaticModel.w_t_is|isothermalReference.assertionLevel|isothermalReference.clip_p_out|isothermalReference.dh|isothermalReference.dp|isothermalReference.dp_fixed|isothermalReference.dp_nom|isothermalReference.dp_start|isothermalReference.dr_corr|isothermalReference.etaSpec|isothermalReference.eta_actual|isothermalReference.eta_fixed|isothermalReference.eta_is|isothermalReference.h_in|isothermalReference.h_out|isothermalReference.initM_flow|der.isothermalReference.inlet.m_flow.|isothermalReference.inlet.m_flow|isothermalReference.inlet.r|isothermalReference.inlet.state.T|isothermalReference.inlet.state.d|isothermalReference.inlet.state.h|isothermalReference.inlet.state.p|isothermalReference.inlet.state.phase|isothermalReference.m_acceleration_0|isothermalReference.m_flow|isothermalReference.m_flowStateSelect|isothermalReference.m_flow_0|isothermalReference.outlet.m_flow|isothermalReference.outlet.r|isothermalReference.outlet.state.T|isothermalReference.outlet.state.d|isothermalReference.outlet.state.h|isothermalReference.outlet.state.p|isothermalReference.outlet.state.phase|isothermalReference.outletSpec|isothermalReference.outletSpec_actual|isothermalReference.outletSpec_prescribed|isothermalReference.outletValueSpec|isothermalReference.pRatio|isothermalReference.pRatio_fixed|isothermalReference.p_in|isothermalReference.p_min|isothermalReference.p_out|isothermalReference.p_out_fixed|isothermalReference.singularityRegime|pressureDifference.duration|pressureDifference.height|pressureDifference.offset|pressureDifference.startTime|pressureDifference.y|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.d|sink.inlet.state.h|sink.inlet.state.p|sink.inlet.state.phase|sink.m_flow|sink.m_flowSpec|sink.m_flow_fixed|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.d|sink1.inlet.state.h|sink1.inlet.state.p|sink1.inlet.state.phase|sink1.m_flow|sink1.m_flowSpec|sink1.m_flow_fixed|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.d|sink2.inlet.state.h|sink2.inlet.state.p|sink2.inlet.state.phase|sink2.m_flow|sink2.m_flowSpec|sink2.m_flow_fixed|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|source.p0|source.p0_par|source1.L|source1.T0|source1.T0_par|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.d|source1.outlet.state.h|source1.outlet.state.p|source1.outlet.state.phase|source1.p0|source1.p0_par|source2.L|source2.T0|source2.T0_par|source2.h0|source2.h0_par|der.source2.outlet.m_flow.|source2.outlet.m_flow|source2.outlet.r|source2.outlet.state.T|source2.outlet.state.d|source2.outlet.state.h|source2.outlet.state.p|source2.outlet.state.phase|source2.p0|source2.p0_par",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.923e-06/1.923e-06, allocations: 0 / 430.8 MB, free: 13.32 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.332e-05/2.525e-05, allocations: 2.312 kB / 430.9 MB, free: 13.31 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater): time 0.1866/0.1866, allocations: 18.25 MB / 449.1 MB, free: 16.45 MB / 410.7 MB
Notification: Performance of NFInst.instExpressions: time 0.01444/0.2011, allocations: 16.66 MB / 465.8 MB, free: 7.293 MB / 410.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006678/0.2017, allocations: 68.56 kB / 465.8 MB, free: 7.25 MB / 410.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.0004984/0.2022, allocations: 265.3 kB / 466.1 MB, free: 7.02 MB / 410.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.01235/0.2146, allocations: 6.947 MB / 473 MB, free: 1.25 MB / 410.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.001008/0.2156, allocations: 0.5743 MB / 473.6 MB, free: 0.6758 MB / 410.7 MB
Notification: Performance of NFFlatten.flatten: time 0.001442/0.217, allocations: 1.734 MB / 475.3 MB, free: 14.93 MB / 426.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.000317/0.2173, allocations: 178.2 kB / 475.5 MB, free: 14.75 MB / 426.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.003318/0.2207, allocations: 2.494 MB / 478 MB, free: 12.23 MB / 426.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005145/0.2212, allocations: 402.6 kB / 478.4 MB, free: 11.84 MB / 426.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001088/0.2213, allocations: 68 kB / 478.5 MB, free: 11.77 MB / 426.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.01374/0.235, allocations: 9.615 MB / 488.1 MB, free: 2.141 MB / 426.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.000203/0.2352, allocations: 191 kB / 488.3 MB, free: 1.953 MB / 426.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0003639/0.2356, allocations: 363 kB / 488.6 MB, free: 1.598 MB / 426.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.0113/0.2469, allocations: 8.09 MB / 496.7 MB, free: 9.488 MB / 442.7 MB
Notification: Performance of FrontEnd - DAE generated: time 4.328e-06/0.2469, allocations: 4 kB / 496.7 MB, free: 9.484 MB / 442.7 MB
Notification: Performance of FrontEnd: time 1.723e-06/0.2469, allocations: 4 kB / 496.7 MB, free: 9.48 MB / 442.7 MB
Notification: Performance of Transformations before backend: time 1.779e-05/0.2469, allocations: 0 / 496.7 MB, free: 9.48 MB / 442.7 MB
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 0.004041/0.251, allocations: 2.184 MB / 498.9 MB, free: 7.262 MB / 442.7 MB
Notification: Performance of prepare preOptimizeDAE: time 3.338e-05/0.251, allocations: 12.03 kB / 498.9 MB, free: 7.25 MB / 442.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0009002/0.2519, allocations: 439.9 kB / 499.3 MB, free: 6.82 MB / 442.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0009765/0.2529, allocations: 0.7511 MB / 0.4884 GB, free: 6.031 MB / 442.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001368/0.253, allocations: 224.8 kB / 0.4886 GB, free: 5.773 MB / 442.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 8.382e-05/0.2531, allocations: 80.33 kB / 0.4887 GB, free: 5.695 MB / 442.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.0009014/0.254, allocations: 0.8115 MB / 0.4895 GB, free: 4.828 MB / 442.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 1.829e-05/0.254, allocations: 3.938 kB / 0.4895 GB, free: 4.824 MB / 442.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 3.849e-05/0.2541, allocations: 36 kB / 0.4895 GB, free: 4.789 MB / 442.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.547e-05/0.2541, allocations: 20 kB / 0.4895 GB, free: 4.77 MB / 442.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0005516/0.2546, allocations: 365.5 kB / 0.4899 GB, free: 4.41 MB / 442.7 MB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.002012/0.2566, allocations: 2.371 MB / 0.4922 GB, free: 1.945 MB / 442.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.0006835/0.2573, allocations: 429.4 kB / 0.4926 GB, free: 1.523 MB / 442.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 9.408e-05/0.2574, allocations: 88.81 kB / 0.4927 GB, free: 1.434 MB / 442.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.17/0.4274, allocations: 96.61 MB / 0.587 GB, free: 0.7266 MB / 0.5261 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.538e-05/0.4275, allocations: 39.62 kB / 0.5871 GB, free: 0.6797 MB / 0.5261 GB
Notification: Performance of pre-optimization done (n=43): time 2.575e-06/0.4275, allocations: 0 / 0.5871 GB, free: 0.6797 MB / 0.5261 GB
Notification: Performance of matching and sorting (n=43): time 0.001147/0.4286, allocations: 0.5225 MB / 0.5876 GB, free: 156 kB / 0.5261 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.833e-05/0.4286, allocations: 55.41 kB / 0.5876 GB, free: 88 kB / 0.5261 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005179/0.4292, allocations: 0.6209 MB / 0.5882 GB, free: 15.45 MB / 0.5417 GB
Notification: Performance of collectPreVariables (initialization): time 3.182e-05/0.4292, allocations: 33.7 kB / 0.5883 GB, free: 15.41 MB / 0.5417 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001989/0.4294, allocations: 401.8 kB / 0.5887 GB, free: 15.02 MB / 0.5417 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001007/0.4295, allocations: 158.6 kB / 0.5888 GB, free: 14.86 MB / 0.5417 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 9.63e-05/0.4296, allocations: 94.08 kB / 0.5889 GB, free: 14.76 MB / 0.5417 GB
Notification: Performance of setup shared object (initialization): time 8.903e-05/0.4297, allocations: 325.9 kB / 0.5892 GB, free: 14.44 MB / 0.5417 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 6.697e-05/0.4297, allocations: 48.97 kB / 0.5892 GB, free: 14.39 MB / 0.5417 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.000121/0.4299, allocations: 175.5 kB / 0.5894 GB, free: 14.17 MB / 0.5417 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0004952/0.4304, allocations: 262 kB / 0.5897 GB, free: 13.86 MB / 0.5417 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.556e-06/0.4304, allocations: 0 / 0.5897 GB, free: 13.86 MB / 0.5417 GB
Notification: Performance of matching and sorting (n=58) (initialization): time 0.0002866/0.4306, allocations: 288.6 kB / 0.5899 GB, free: 13.57 MB / 0.5417 GB
Notification: Performance of prepare postOptimizeDAE: time 1.842e-05/0.4307, allocations: 8 kB / 0.5899 GB, free: 13.56 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 9.558e-06/0.4307, allocations: 4 kB / 0.59 GB, free: 13.56 MB / 0.5417 GB
Notification: Performance of postOpt tearingSystem (initialization): time 1.709e-05/0.4307, allocations: 11.94 kB / 0.59 GB, free: 13.55 MB / 0.5417 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002281/0.4309, allocations: 109.1 kB / 0.5901 GB, free: 13.44 MB / 0.5417 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 5.61e-06/0.4309, allocations: 4 kB / 0.5901 GB, free: 13.44 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0001855/0.4311, allocations: 48.12 kB / 0.5901 GB, free: 13.39 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 2.525e-05/0.4311, allocations: 20 kB / 0.5901 GB, free: 13.37 MB / 0.5417 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 (fullMedium.outlet.state.phase,incompressibleFluid.outlet.state.phase,isothermalReference.outlet.state.phase,source1.outlet.state.phase,source2.outlet.state.phase,source.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 0.0001711/0.4313, allocations: 151.7 kB / 0.5903 GB, free: 13.21 MB / 0.5417 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 6.562e-05/0.4314, allocations: 63.92 kB / 0.5903 GB, free: 13.15 MB / 0.5417 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.0007378/0.4321, allocations: 0.9023 MB / 0.5912 GB, free: 12.24 MB / 0.5417 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 1.835e-05/0.4321, allocations: 23.91 kB / 0.5912 GB, free: 12.21 MB / 0.5417 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 1.633e-06/0.4321, allocations: 0 / 0.5912 GB, free: 12.21 MB / 0.5417 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 5.39e-06/0.4321, allocations: 0 / 0.5912 GB, free: 12.21 MB / 0.5417 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.001324/0.4335, allocations: 1.317 MB / 0.5925 GB, free: 10.88 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.188e-06/0.4335, allocations: 0 / 0.5925 GB, free: 10.88 MB / 0.5417 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0001629/0.4336, allocations: 83.83 kB / 0.5926 GB, free: 10.79 MB / 0.5417 GB
Notification: Performance of postOpt tearingSystem (simulation): time 4.408e-06/0.4336, allocations: 4 kB / 0.5926 GB, free: 10.79 MB / 0.5417 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 1.329e-05/0.4336, allocations: 4.875 kB / 0.5926 GB, free: 10.79 MB / 0.5417 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 7.524e-06/0.4337, allocations: 11.92 kB / 0.5926 GB, free: 10.77 MB / 0.5417 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.062e-06/0.4337, allocations: 0 / 0.5926 GB, free: 10.77 MB / 0.5417 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0004422/0.4341, allocations: 0.5772 MB / 0.5932 GB, free: 10.18 MB / 0.5417 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001386/0.4342, allocations: 129.1 kB / 0.5933 GB, free: 10.05 MB / 0.5417 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 5.245e-05/0.4343, allocations: 27.84 kB / 0.5933 GB, free: 10.02 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001214/0.4344, allocations: 23.61 kB / 0.5934 GB, free: 10 MB / 0.5417 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 5.507e-05/0.4345, allocations: 32.44 kB / 0.5934 GB, free: 9.973 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 1.625e-05/0.4345, allocations: 11.98 kB / 0.5934 GB, free: 9.961 MB / 0.5417 GB
Notification: Performance of sorting global known variables: time 0.0002883/0.4348, allocations: 380.4 kB / 0.5938 GB, free: 9.578 MB / 0.5417 GB
Notification: Performance of sort global known variables: time 4e-08/0.4348, allocations: 0 / 0.5938 GB, free: 9.578 MB / 0.5417 GB
Notification: Performance of remove unused functions: time 0.003677/0.4384, allocations: 1.629 MB / 0.5954 GB, free: 7.945 MB / 0.5417 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 0.005252/0.4437, allocations: 2.019 MB / 0.5973 GB, free: 5.949 MB / 0.5417 GB
Notification: Performance of simCode: created initialization part: time 0.0004618/0.4442, allocations: 261.1 kB / 0.5976 GB, free: 5.688 MB / 0.5417 GB
Notification: Performance of simCode: created event and clocks part: time 3.476e-05/0.4442, allocations: 8 kB / 0.5976 GB, free: 5.68 MB / 0.5417 GB
Notification: Performance of simCode: created simulation system equations: time 0.000173/0.4444, allocations: 183.1 kB / 0.5978 GB, free: 5.5 MB / 0.5417 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001014/0.4454, allocations: 392.9 kB / 0.5981 GB, free: 5.152 MB / 0.5417 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.002737/0.4481, allocations: 1.928 MB / 0.6 GB, free: 3.18 MB / 0.5417 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0001496/0.4483, allocations: 214.4 kB / 0.6002 GB, free: 2.953 MB / 0.5417 GB
Notification: Performance of simCode: alias equations: time 0.0004522/0.4487, allocations: 250.2 kB / 0.6005 GB, free: 2.719 MB / 0.5417 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0004439/0.4492, allocations: 285.1 kB / 0.6007 GB, free: 2.438 MB / 0.5417 GB
Notification: Performance of SimCode: time 1.813e-06/0.4492, allocations: 0 / 0.6007 GB, free: 2.438 MB / 0.5417 GB
Notification: Performance of Templates: time 0.2505/0.6997, allocations: 68.93 MB / 0.6681 GB, free: 201.5 MB / 0.6042 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=240  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.LiquidWater_ref.mat","",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: 6.613883331883699]