Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_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 0.0009179/0.0009179, allocations: 93.06 kB / 19.65 MB, free: 280 kB / 13.93 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.0014/0.0014, allocations: 169 kB / 23.02 MB, free: 1.551 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 0.9181/0.9181, allocations: 177.1 MB / 203.4 MB, free: 5.645 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 0.7011/0.7011, allocations: 118.6 MB / 378.6 MB, free: 1.473 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.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_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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 2.073e-06/2.073e-06, allocations: 0 / 483.6 MB, free: 8.211 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.512e-05/2.719e-05, allocations: 3.594 kB / 483.6 MB, free: 8.207 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater): time 0.009438/0.009466, allocations: 8.815 MB / 492.5 MB, free: 2.254 MB / 410.7 MB
Notification: Performance of NFInst.instExpressions: time 0.003941/0.01341, allocations: 2.376 MB / 494.8 MB, free: 0.5977 MB / 410.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001045/0.01445, allocations: 74.94 kB / 494.9 MB, free: 0.5508 MB / 410.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.0006336/0.01509, allocations: 206.1 kB / 495.1 MB, free: 440 kB / 410.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.002127/0.01721, allocations: 0.7702 MB / 495.9 MB, free: 15.92 MB / 426.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.0009866/0.0182, allocations: 362 kB / 496.2 MB, free: 15.73 MB / 426.7 MB
Notification: Performance of NFFlatten.flatten: time 0.002392/0.02059, allocations: 1.579 MB / 497.8 MB, free: 14.91 MB / 426.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0004116/0.021, allocations: 130 kB / 497.9 MB, free: 14.84 MB / 426.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001822/0.02282, allocations: 0.8015 MB / 498.7 MB, free: 14.51 MB / 426.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0007261/0.02355, allocations: 365.4 kB / 499.1 MB, free: 14.39 MB / 426.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001571/0.02371, allocations: 62.53 kB / 499.2 MB, free: 14.39 MB / 426.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.0007327/0.02444, allocations: 192.9 kB / 499.3 MB, free: 14.34 MB / 426.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0001848/0.02463, allocations: 174.6 kB / 499.5 MB, free: 14.22 MB / 426.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0005555/0.02518, allocations: 300.9 kB / 499.8 MB, free: 14.11 MB / 426.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.002043/0.02722, allocations: 1.033 MB / 0.4891 GB, free: 13.62 MB / 426.7 MB
Notification: Performance of FrontEnd - DAE generated: time 5.26e-06/0.02723, allocations: 0 / 0.4891 GB, free: 13.62 MB / 426.7 MB
Notification: Performance of FrontEnd: time 1.422e-06/0.02723, allocations: 1.094 kB / 0.4891 GB, free: 13.62 MB / 426.7 MB
Notification: Performance of Transformations before backend: time 3.062e-05/0.02726, allocations: 0 / 0.4891 GB, free: 13.62 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 0.002651/0.02991, allocations: 1.377 MB / 0.4904 GB, free: 12.66 MB / 426.7 MB
Notification: Performance of prepare preOptimizeDAE: time 4.737e-05/0.02996, allocations: 9.203 kB / 0.4905 GB, free: 12.66 MB / 426.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0003436/0.0303, allocations: 185.6 kB / 0.4906 GB, free: 12.56 MB / 426.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001702/0.032, allocations: 0.8049 MB / 0.4914 GB, free: 11.96 MB / 426.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002468/0.03225, allocations: 210.8 kB / 0.4916 GB, free: 11.73 MB / 426.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001093/0.03236, allocations: 65.12 kB / 0.4917 GB, free: 11.66 MB / 426.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001116/0.03348, allocations: 0.5901 MB / 0.4923 GB, free: 11.12 MB / 426.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 1.799e-05/0.03349, allocations: 192 / 0.4923 GB, free: 11.12 MB / 426.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.43e-05/0.03355, allocations: 31.94 kB / 0.4923 GB, free: 11.09 MB / 426.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 2.261e-05/0.03357, allocations: 16 kB / 0.4923 GB, free: 11.07 MB / 426.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0007281/0.0343, allocations: 302.1 kB / 0.4926 GB, free: 10.84 MB / 426.7 MB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003259/0.03756, allocations: 2.397 MB / 0.4949 GB, free: 8.586 MB / 426.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.0005925/0.03815, allocations: 291.2 kB / 0.4952 GB, free: 8.32 MB / 426.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0002668/0.03842, allocations: 137.4 kB / 0.4953 GB, free: 8.203 MB / 426.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.001705/0.04012, allocations: 0.9195 MB / 0.4962 GB, free: 7.391 MB / 426.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.459e-05/0.04016, allocations: 41.77 kB / 0.4963 GB, free: 7.34 MB / 426.7 MB
Notification: Performance of pre-optimization done (n=45): time 1.994e-06/0.04016, allocations: 0 / 0.4963 GB, free: 7.34 MB / 426.7 MB
Notification: Performance of matching and sorting (n=45): time 0.0008447/0.041, allocations: 388.9 kB / 0.4966 GB, free: 6.984 MB / 426.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 3.683e-05/0.04104, allocations: 59.86 kB / 0.4967 GB, free: 6.914 MB / 426.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.000827/0.04187, allocations: 0.6805 MB / 0.4974 GB, free: 6.332 MB / 426.7 MB
Notification: Performance of collectPreVariables (initialization): time 2.945e-05/0.0419, allocations: 33.7 kB / 0.4974 GB, free: 6.293 MB / 426.7 MB
Notification: Performance of collectInitialEqns (initialization): time 0.0006183/0.04252, allocations: 0.5097 MB / 0.4979 GB, free: 5.82 MB / 426.7 MB
Notification: Performance of collectInitialBindings (initialization): time 0.000132/0.04265, allocations: 161.5 kB / 0.4981 GB, free: 5.672 MB / 426.7 MB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001495/0.0428, allocations: 100.8 kB / 0.4982 GB, free: 5.574 MB / 426.7 MB
Notification: Performance of setup shared object (initialization): time 0.000155/0.04295, allocations: 0.4905 MB / 0.4986 GB, free: 5.082 MB / 426.7 MB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0001785/0.04313, allocations: 73.55 kB / 0.4987 GB, free: 5.02 MB / 426.7 MB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0002913/0.04342, allocations: 257.4 kB / 0.4989 GB, free: 4.711 MB / 426.7 MB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0005017/0.04392, allocations: 364.1 kB / 0.4993 GB, free: 4.289 MB / 426.7 MB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.769e-06/0.04393, allocations: 8.734 kB / 0.4993 GB, free: 4.281 MB / 426.7 MB
Notification: Performance of matching and sorting (n=62) (initialization): time 0.0007442/0.04467, allocations: 434.5 kB / 0.4997 GB, free: 3.879 MB / 426.7 MB
Notification: Performance of prepare postOptimizeDAE: time 2.094e-05/0.04469, allocations: 6.188 kB / 0.4997 GB, free: 3.875 MB / 426.7 MB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 9.278e-06/0.0447, allocations: 8.031 kB / 0.4997 GB, free: 3.867 MB / 426.7 MB
Notification: Performance of postOpt tearingSystem (initialization): time 2.541e-05/0.04473, allocations: 8 kB / 0.4997 GB, free: 3.859 MB / 426.7 MB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0003796/0.04511, allocations: 118.5 kB / 0.4999 GB, free: 3.758 MB / 426.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.77e-05/0.04513, allocations: 17.52 kB / 0.4999 GB, free: 3.742 MB / 426.7 MB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0002932/0.04542, allocations: 53.17 kB / 0.4999 GB, free: 3.691 MB / 426.7 MB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.26e-05/0.04547, allocations: 25.5 kB / 0.4999 GB, free: 3.668 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 0.0001946/0.04567, allocations: 185.1 kB / 0.5001 GB, free: 3.477 MB / 426.7 MB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001317/0.0458, allocations: 107.4 kB / 0.5002 GB, free: 3.371 MB / 426.7 MB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.0009169/0.04671, allocations: 0.5625 MB / 0.5008 GB, free: 2.875 MB / 426.7 MB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 1.036e-05/0.04672, allocations: 8.641 kB / 0.5008 GB, free: 2.867 MB / 426.7 MB
Notification: Performance of postOpt constantLinearSystem (simulation): time 5.64e-06/0.04673, allocations: 3.938 kB / 0.5008 GB, free: 2.863 MB / 426.7 MB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 7.133e-06/0.04674, allocations: 2.203 kB / 0.5008 GB, free: 2.863 MB / 426.7 MB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.001408/0.04815, allocations: 0.9426 MB / 0.5017 GB, free: 1.902 MB / 426.7 MB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 8.385e-06/0.04815, allocations: 8.125 kB / 0.5017 GB, free: 1.895 MB / 426.7 MB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0002327/0.04839, allocations: 75.89 kB / 0.5018 GB, free: 1.82 MB / 426.7 MB
Notification: Performance of postOpt tearingSystem (simulation): time 4.549e-06/0.04839, allocations: 0 / 0.5018 GB, free: 1.82 MB / 426.7 MB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.024e-05/0.04841, allocations: 8 kB / 0.5018 GB, free: 1.812 MB / 426.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 5.42e-06/0.04842, allocations: 4 kB / 0.5018 GB, free: 1.809 MB / 426.7 MB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 3.597e-06/0.04842, allocations: 4 kB / 0.5018 GB, free: 1.805 MB / 426.7 MB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0005252/0.04895, allocations: 497.5 kB / 0.5023 GB, free: 1.273 MB / 426.7 MB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001837/0.04913, allocations: 111.3 kB / 0.5024 GB, free: 1.164 MB / 426.7 MB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 6.775e-05/0.0492, allocations: 11.95 kB / 0.5024 GB, free: 1.152 MB / 426.7 MB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002221/0.04942, allocations: 15.98 kB / 0.5024 GB, free: 1.137 MB / 426.7 MB
Notification: Performance of postOpt findZeroCrossings (simulation): time 7.676e-05/0.0495, allocations: 31.95 kB / 0.5024 GB, free: 1.105 MB / 426.7 MB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.184e-05/0.04952, allocations: 12 kB / 0.5024 GB, free: 1.094 MB / 426.7 MB
Notification: Performance of sorting global known variables: time 0.000517/0.05003, allocations: 462.9 kB / 0.5029 GB, free: 0.6484 MB / 426.7 MB
Notification: Performance of sort global known variables: time 8e-08/0.05003, allocations: 0 / 0.5029 GB, free: 0.6484 MB / 426.7 MB
Notification: Performance of remove unused functions: time 0.0007822/0.05082, allocations: 223.4 kB / 0.5031 GB, free: 440 kB / 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 0.0003023/0.05112, allocations: 182.9 kB / 0.5033 GB, free: 248 kB / 426.7 MB
Notification: Performance of simCode: created initialization part: time 0.0003948/0.05151, allocations: 241.2 kB / 0.5035 GB, free: 4 kB / 426.7 MB
Notification: Performance of simCode: created event and clocks part: time 2.725e-06/0.05152, allocations: 4 kB / 0.5035 GB, free: 0 / 426.7 MB
Notification: Performance of simCode: created simulation system equations: time 0.0001421/0.05166, allocations: 116.2 kB / 0.5036 GB, free: 15.88 MB / 442.7 MB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.0009729/0.05263, allocations: 388.6 kB / 0.504 GB, free: 15.54 MB / 442.7 MB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.00211/0.05474, allocations: 1.327 MB / 0.5053 GB, free: 14.14 MB / 442.7 MB
Notification: Performance of simCode: some other stuff during SimCode phase: time 9.568e-05/0.05484, allocations: 154.7 kB / 0.5054 GB, free: 13.97 MB / 442.7 MB
Notification: Performance of simCode: alias equations: time 0.0003293/0.05517, allocations: 145 kB / 0.5056 GB, free: 13.85 MB / 442.7 MB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001053/0.05527, allocations: 72.48 kB / 0.5056 GB, free: 13.78 MB / 442.7 MB
Notification: Performance of SimCode: time 7.21e-07/0.05527, allocations: 0 / 0.5056 GB, free: 13.78 MB / 442.7 MB
Notification: Performance of Templates: time 0.01469/0.06996, allocations: 11.78 MB / 0.5171 GB, free: 2.359 MB / 442.7 MB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater -abortSlowSimulation -alarm=240  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 3.788913533091545]