Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.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 0.0008697/0.0008697, allocations: 86.05 kB / 19.87 MB, free: 4.617 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 0.001581/0.001581, allocations: 169.7 kB / 23.27 MB, free: 1.223 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 1.001/1.001, allocations: 177.1 MB / 203.7 MB, free: 5.488 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.7148/0.7148, allocations: 118.6 MB / 378.9 MB, free: 1.324 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater,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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|source2.p0|source2.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater")
translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater,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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|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.p|source2.p0|source2.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.773e-06/1.773e-06, allocations: 0 / 484.1 MB, free: 8.109 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.416e-05/2.594e-05, allocations: 5.547 kB / 484.1 MB, free: 8.105 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater): time 0.009719/0.009745, allocations: 8.701 MB / 492.8 MB, free: 2.16 MB / 410.7 MB
Notification: Performance of NFInst.instExpressions: time 0.003977/0.01372, allocations: 2.376 MB / 495.2 MB, free: 0.4961 MB / 410.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0009179/0.01464, allocations: 69.72 kB / 495.2 MB, free: 464 kB / 410.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.0007143/0.01535, allocations: 211 kB / 495.4 MB, free: 336 kB / 410.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.002527/0.01788, allocations: 0.7766 MB / 496.2 MB, free: 15.82 MB / 426.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.001097/0.01898, allocations: 366.6 kB / 496.6 MB, free: 15.62 MB / 426.7 MB
Notification: Performance of NFFlatten.flatten: time 0.002589/0.02157, allocations: 1.575 MB / 498.2 MB, free: 14.8 MB / 426.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.000401/0.02197, allocations: 131.1 kB / 498.3 MB, free: 14.73 MB / 426.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001975/0.02394, allocations: 0.8222 MB / 499.1 MB, free: 14.39 MB / 426.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0006985/0.02464, allocations: 365.7 kB / 499.5 MB, free: 14.27 MB / 426.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001546/0.0248, allocations: 55.97 kB / 499.5 MB, free: 14.27 MB / 426.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.0007603/0.02556, allocations: 195.9 kB / 499.7 MB, free: 14.23 MB / 426.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0001899/0.02575, allocations: 171 kB / 499.9 MB, free: 14.11 MB / 426.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0004785/0.02623, allocations: 299.7 kB / 0.4884 GB, free: 13.99 MB / 426.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.001586/0.02781, allocations: 1.029 MB / 0.4894 GB, free: 13.52 MB / 426.7 MB
Notification: Performance of FrontEnd - DAE generated: time 4.839e-06/0.02782, allocations: 0.75 kB / 0.4894 GB, free: 13.52 MB / 426.7 MB
Notification: Performance of FrontEnd: time 1.403e-06/0.02782, allocations: 3.938 kB / 0.4894 GB, free: 13.51 MB / 426.7 MB
Notification: Performance of Transformations before backend: time 3.439e-05/0.02785, allocations: 0 / 0.4894 GB, free: 13.51 MB / 426.7 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 157
 * Number of variables: 157
Notification: Performance of Generate backend data structure: time 0.002116/0.02997, allocations: 1.397 MB / 0.4908 GB, free: 12.52 MB / 426.7 MB
Notification: Performance of prepare preOptimizeDAE: time 4.339e-05/0.03001, allocations: 9.141 kB / 0.4908 GB, free: 12.52 MB / 426.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0002853/0.0303, allocations: 178 kB / 0.491 GB, free: 12.44 MB / 426.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001198/0.0315, allocations: 0.795 MB / 0.4918 GB, free: 11.85 MB / 426.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001417/0.03164, allocations: 206.7 kB / 0.492 GB, free: 11.61 MB / 426.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 7.519e-05/0.03171, allocations: 64.98 kB / 0.492 GB, free: 11.55 MB / 426.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.000688/0.0324, allocations: 0.5464 MB / 0.4926 GB, free: 11.05 MB / 426.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 1.591e-05/0.03242, allocations: 192 / 0.4926 GB, free: 11.05 MB / 426.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 3.843e-05/0.03245, allocations: 28.59 kB / 0.4926 GB, free: 11.02 MB / 426.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.332e-05/0.03247, allocations: 16 kB / 0.4926 GB, free: 11.01 MB / 426.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0003402/0.03281, allocations: 239.2 kB / 0.4928 GB, free: 10.83 MB / 426.7 MB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.002119/0.03493, allocations: 2.284 MB / 0.4951 GB, free: 8.676 MB / 426.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.00034/0.03527, allocations: 271.2 kB / 0.4953 GB, free: 8.43 MB / 426.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0001243/0.03539, allocations: 116.6 kB / 0.4954 GB, free: 8.332 MB / 426.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.001264/0.03666, allocations: 0.9444 MB / 0.4964 GB, free: 7.523 MB / 426.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 2.593e-05/0.03668, allocations: 42.61 kB / 0.4964 GB, free: 7.473 MB / 426.7 MB
Notification: Performance of pre-optimization done (n=45): time 1.563e-06/0.03668, allocations: 0 / 0.4964 GB, free: 7.473 MB / 426.7 MB
Notification: Performance of matching and sorting (n=45): time 0.0004341/0.03712, allocations: 356.5 kB / 0.4967 GB, free: 7.148 MB / 426.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.96e-05/0.03715, allocations: 55.41 kB / 0.4968 GB, free: 7.082 MB / 426.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005059/0.03765, allocations: 0.6799 MB / 0.4975 GB, free: 6.5 MB / 426.7 MB
Notification: Performance of collectPreVariables (initialization): time 2.426e-05/0.03768, allocations: 38.44 kB / 0.4975 GB, free: 6.457 MB / 426.7 MB
Notification: Performance of collectInitialEqns (initialization): time 0.0002761/0.03795, allocations: 0.5124 MB / 0.498 GB, free: 5.98 MB / 426.7 MB
Notification: Performance of collectInitialBindings (initialization): time 9.247e-05/0.03805, allocations: 162.2 kB / 0.4981 GB, free: 5.832 MB / 426.7 MB
Notification: Performance of simplifyInitialFunctions (initialization): time 9.497e-05/0.03814, allocations: 103.9 kB / 0.4982 GB, free: 5.73 MB / 426.7 MB
Notification: Performance of setup shared object (initialization): time 0.0001265/0.03827, allocations: 0.4947 MB / 0.4987 GB, free: 5.234 MB / 426.7 MB
Notification: Performance of preBalanceInitialSystem (initialization): time 8.383e-05/0.03835, allocations: 53.7 kB / 0.4988 GB, free: 5.191 MB / 426.7 MB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0001691/0.03852, allocations: 249.6 kB / 0.499 GB, free: 4.891 MB / 426.7 MB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0002703/0.03879, allocations: 335.9 kB / 0.4993 GB, free: 4.496 MB / 426.7 MB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.875e-06/0.03879, allocations: 0 / 0.4993 GB, free: 4.496 MB / 426.7 MB
Notification: Performance of matching and sorting (n=62) (initialization): time 0.000408/0.0392, allocations: 409.9 kB / 0.4997 GB, free: 4.117 MB / 426.7 MB
Notification: Performance of prepare postOptimizeDAE: time 1.959e-05/0.03922, allocations: 4 kB / 0.4997 GB, free: 4.113 MB / 426.7 MB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.052e-05/0.03923, allocations: 8 kB / 0.4997 GB, free: 4.105 MB / 426.7 MB
Notification: Performance of postOpt tearingSystem (initialization): time 1.729e-05/0.03925, allocations: 4.703 kB / 0.4997 GB, free: 4.102 MB / 426.7 MB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002334/0.03948, allocations: 114.5 kB / 0.4999 GB, free: 4.004 MB / 426.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 8.416e-06/0.03949, allocations: 12.59 kB / 0.4999 GB, free: 3.992 MB / 426.7 MB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0001639/0.03965, allocations: 53.67 kB / 0.4999 GB, free: 3.941 MB / 426.7 MB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.56e-05/0.03969, allocations: 21.59 kB / 0.4999 GB, free: 3.922 MB / 426.7 MB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 19
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (62):
 * Single equations (assignments): 62
 * 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 0.0001547/0.03984, allocations: 189.3 kB / 0.5001 GB, free: 3.727 MB / 426.7 MB
Notification: Performance of postOpt lateInlineFunction (simulation): time 8.536e-05/0.03993, allocations: 107.4 kB / 0.5002 GB, free: 3.621 MB / 426.7 MB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.000627/0.04056, allocations: 0.555 MB / 0.5008 GB, free: 3.125 MB / 426.7 MB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 6.753e-06/0.04056, allocations: 0 / 0.5008 GB, free: 3.125 MB / 426.7 MB
Notification: Performance of postOpt constantLinearSystem (simulation): time 1.783e-06/0.04057, allocations: 4 kB / 0.5008 GB, free: 3.121 MB / 426.7 MB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 5.892e-06/0.04057, allocations: 3.938 kB / 0.5008 GB, free: 3.117 MB / 426.7 MB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0008097/0.04138, allocations: 0.8164 MB / 0.5016 GB, free: 2.242 MB / 426.7 MB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.469e-06/0.04139, allocations: 0 / 0.5016 GB, free: 2.242 MB / 426.7 MB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0001296/0.04151, allocations: 71.89 kB / 0.5016 GB, free: 2.172 MB / 426.7 MB
Notification: Performance of postOpt tearingSystem (simulation): time 5.33e-06/0.04152, allocations: 4 kB / 0.5016 GB, free: 2.168 MB / 426.7 MB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 1.304e-05/0.04153, allocations: 11.94 kB / 0.5016 GB, free: 2.156 MB / 426.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 3.437e-06/0.04154, allocations: 4 kB / 0.5017 GB, free: 2.152 MB / 426.7 MB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 3.086e-06/0.04154, allocations: 3.984 kB / 0.5017 GB, free: 2.148 MB / 426.7 MB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0003254/0.04187, allocations: 485.5 kB / 0.5021 GB, free: 1.629 MB / 426.7 MB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001139/0.04198, allocations: 107.3 kB / 0.5022 GB, free: 1.523 MB / 426.7 MB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 3.833e-05/0.04202, allocations: 19.98 kB / 0.5022 GB, free: 1.504 MB / 426.7 MB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001107/0.04213, allocations: 15.98 kB / 0.5023 GB, free: 1.488 MB / 426.7 MB
Notification: Performance of postOpt findZeroCrossings (simulation): time 5.073e-05/0.04218, allocations: 23.95 kB / 0.5023 GB, free: 1.465 MB / 426.7 MB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 1.414e-05/0.04219, allocations: 12 kB / 0.5023 GB, free: 1.453 MB / 426.7 MB
Notification: Performance of sorting global known variables: time 0.0002711/0.04246, allocations: 438.7 kB / 0.5027 GB, free: 1.031 MB / 426.7 MB
Notification: Performance of sort global known variables: time 1e-07/0.04246, allocations: 3.938 kB / 0.5027 GB, free: 1.027 MB / 426.7 MB
Notification: Performance of remove unused functions: time 0.0005503/0.04301, allocations: 223.4 kB / 0.5029 GB, free: 0.8086 MB / 426.7 MB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 7
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (37):
 * Single equations (assignments): 36
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 1
 * 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 0.000274/0.04329, allocations: 174.7 kB / 0.5031 GB, free: 0.6328 MB / 426.7 MB
Notification: Performance of simCode: created initialization part: time 0.0002846/0.04357, allocations: 221.9 kB / 0.5033 GB, free: 424 kB / 426.7 MB
Notification: Performance of simCode: created event and clocks part: time 1.683e-06/0.04357, allocations: 8.062 kB / 0.5033 GB, free: 416 kB / 426.7 MB
Notification: Performance of simCode: created simulation system equations: time 0.0001038/0.04368, allocations: 99.19 kB / 0.5034 GB, free: 312 kB / 426.7 MB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.0009609/0.04464, allocations: 395.6 kB / 0.5038 GB, free: 15.95 MB / 442.7 MB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.001831/0.04647, allocations: 1.323 MB / 0.5051 GB, free: 14.56 MB / 442.7 MB
Notification: Performance of simCode: some other stuff during SimCode phase: time 9.867e-05/0.04657, allocations: 154.7 kB / 0.5052 GB, free: 14.39 MB / 442.7 MB
Notification: Performance of simCode: alias equations: time 0.0003547/0.04692, allocations: 139.5 kB / 0.5054 GB, free: 14.27 MB / 442.7 MB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0004092/0.04733, allocations: 321.9 kB / 0.5057 GB, free: 13.95 MB / 442.7 MB
Notification: Performance of SimCode: time 1.142e-06/0.04733, allocations: 0 / 0.5057 GB, free: 13.95 MB / 442.7 MB
Notification: Performance of Templates: time 0.01646/0.06379, allocations: 13.04 MB / 0.5184 GB, free: 1.324 MB / 442.7 MB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater -abortSlowSimulation -alarm=240  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 3.7500119539909065]