Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.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 0.002034/0.002034, allocations: 99.64 kB / 18.94 MB, free: 2.551 MB / 14.72 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.002322/0.002322, allocations: 217.6 kB / 22.25 MB, free: 4.859 MB / 14.72 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.583/1.583, allocations: 230.6 MB / 256 MB, free: 7.789 MB / 206.1 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 1.076/1.076, allocations: 150.8 MB / 463.2 MB, free: 1.414 MB / 366.1 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.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.TableBased")
translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|eta|fullMedium.L|fullMedium.P|fullMedium.P_nom|fullMedium.TC|fullMedium.adiabaticModel.eta_is|fullMedium.adiabaticModel.h_in|fullMedium.adiabaticModel.h_out|fullMedium.adiabaticModel.h_out_is|fullMedium.adiabaticModel.p_out|fullMedium.adiabaticModel.s_in|fullMedium.adiabaticModel.state_in.T|fullMedium.adiabaticModel.state_in.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.TableBased") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 0.002692/0.002692, allocations: 91.84 kB / 0.6397 GB, free: 3.168 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.1751/0.1778, allocations: 88.08 MB / 0.7257 GB, free: 10.9 MB / 0.5606 GB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased): time 0.4029/0.5806, allocations: 43.87 MB / 0.7685 GB, free: 7.199 MB / 0.5762 GB
Notification: Performance of NFInst.instExpressions: time 0.004669/0.5853, allocations: 2.514 MB / 0.771 GB, free: 6.289 MB / 0.5762 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.00111/0.5864, allocations: 69.19 kB / 0.771 GB, free: 6.246 MB / 0.5762 GB
Notification: Performance of NFTyping.typeComponents: time 0.001239/0.5876, allocations: 380.3 kB / 0.7714 GB, free: 6.078 MB / 0.5762 GB
Notification: Performance of NFTyping.typeBindings: time 0.007233/0.5949, allocations: 2.381 MB / 0.7737 GB, free: 5.332 MB / 0.5762 GB
Notification: Performance of NFTyping.typeClassSections: time 0.004048/0.5989, allocations: 1.286 MB / 0.775 GB, free: 5.043 MB / 0.5762 GB
Notification: Performance of NFFlatten.flatten: time 0.002953/0.6019, allocations: 1.479 MB / 0.7764 GB, free: 4.652 MB / 0.5762 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0004333/0.6023, allocations: 125.7 kB / 0.7765 GB, free: 4.609 MB / 0.5762 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.005946/0.6082, allocations: 2.667 MB / 0.7792 GB, free: 4.176 MB / 0.5762 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0009063/0.6091, allocations: 437.6 kB / 0.7796 GB, free: 4.016 MB / 0.5762 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001424/0.6093, allocations: 58.16 kB / 0.7796 GB, free: 4.016 MB / 0.5762 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01019/0.6195, allocations: 4.498 MB / 0.784 GB, free: 3.5 MB / 0.5762 GB
Notification: Performance of NFScalarize.scalarize: time 0.0003049/0.6198, allocations: 164.2 kB / 0.7842 GB, free: 3.387 MB / 0.5762 GB
Notification: Performance of NFVerifyModel.verify: time 0.0005996/0.6204, allocations: 370 kB / 0.7845 GB, free: 3.191 MB / 0.5762 GB
Notification: Performance of NFConvertDAE.convert: time 0.004947/0.6253, allocations: 2.044 MB / 0.7865 GB, free: 2.391 MB / 0.5762 GB
Notification: Performance of FrontEnd - DAE generated: time 7.554e-06/0.6253, allocations: 4 kB / 0.7865 GB, free: 2.387 MB / 0.5762 GB
Notification: Performance of FrontEnd: time 2.224e-06/0.6253, allocations: 0 / 0.7865 GB, free: 2.387 MB / 0.5762 GB
Notification: Performance of Transformations before backend: time 1.8e-05/0.6254, allocations: 0 / 0.7865 GB, free: 2.387 MB / 0.5762 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 157
 * Number of variables: 157
Notification: Performance of Generate backend data structure: time 0.002444/0.6278, allocations: 1.425 MB / 0.7879 GB, free: 1.434 MB / 0.5762 GB
Notification: Performance of prepare preOptimizeDAE: time 3.93e-05/0.6278, allocations: 8.875 kB / 0.7879 GB, free: 1.434 MB / 0.5762 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001286/0.6291, allocations: 205.1 kB / 0.7881 GB, free: 1.355 MB / 0.5762 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001704/0.6308, allocations: 0.7121 MB / 0.7888 GB, free: 0.9219 MB / 0.5762 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001599/0.631, allocations: 207.1 kB / 0.789 GB, free: 0.7148 MB / 0.5762 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001059/0.6311, allocations: 69.19 kB / 0.7891 GB, free: 0.6875 MB / 0.5762 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.00148/0.6326, allocations: 0.6877 MB / 0.7898 GB, free: 340 kB / 0.5762 GB
Notification: Performance of preOpt findStateOrder (simulation): time 2.055e-05/0.6326, allocations: 6.891 kB / 0.7898 GB, free: 336 kB / 0.5762 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.835e-05/0.6327, allocations: 26.53 kB / 0.7898 GB, free: 316 kB / 0.5762 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.793e-05/0.6327, allocations: 15.59 kB / 0.7898 GB, free: 316 kB / 0.5762 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001103/0.6338, allocations: 477.1 kB / 0.7903 GB, free: 156 kB / 0.5762 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003763/0.6375, allocations: 2.104 MB / 0.7923 GB, free: 14.68 MB / 0.5919 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.001436/0.639, allocations: 381.3 kB / 0.7927 GB, free: 14.55 MB / 0.5919 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0003757/0.6393, allocations: 148.2 kB / 0.7928 GB, free: 14.5 MB / 0.5919 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0004688/0.6398, allocations: 112.8 kB / 0.7929 GB, free: 14.48 MB / 0.5919 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.715e-05/0.6399, allocations: 43.88 kB / 0.793 GB, free: 14.43 MB / 0.5919 GB
Notification: Performance of pre-optimization done (n=34): time 2.274e-06/0.6399, allocations: 0 / 0.793 GB, free: 14.43 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=34): time 0.0016/0.6415, allocations: 491.4 kB / 0.7934 GB, free: 14.24 MB / 0.5919 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 4.98e-05/0.6415, allocations: 59.62 kB / 0.7935 GB, free: 14.18 MB / 0.5919 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0008857/0.6424, allocations: 0.6633 MB / 0.7941 GB, free: 13.88 MB / 0.5919 GB
Notification: Performance of collectPreVariables (initialization): time 5.084e-05/0.6425, allocations: 31.39 kB / 0.7942 GB, free: 13.85 MB / 0.5919 GB
Notification: Performance of collectInitialEqns (initialization): time 0.000399/0.6429, allocations: 476.5 kB / 0.7946 GB, free: 13.48 MB / 0.5919 GB
Notification: Performance of collectInitialBindings (initialization): time 0.0001241/0.643, allocations: 119.1 kB / 0.7947 GB, free: 13.38 MB / 0.5919 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001694/0.6431, allocations: 92.88 kB / 0.7948 GB, free: 13.33 MB / 0.5919 GB
Notification: Performance of setup shared object (initialization): time 0.0001816/0.6433, allocations: 324.3 kB / 0.7951 GB, free: 13.02 MB / 0.5919 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003116/0.6436, allocations: 118.6 kB / 0.7952 GB, free: 12.98 MB / 0.5919 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004197/0.6441, allocations: 212.5 kB / 0.7954 GB, free: 12.83 MB / 0.5919 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0007326/0.6448, allocations: 343.1 kB / 0.7958 GB, free: 12.61 MB / 0.5919 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 4.488e-06/0.6448, allocations: 1.375 kB / 0.7958 GB, free: 12.61 MB / 0.5919 GB
Notification: Performance of matching and sorting (n=51) (initialization): time 0.001095/0.6459, allocations: 462.4 kB / 0.7962 GB, free: 12.38 MB / 0.5919 GB
Notification: Performance of prepare postOptimizeDAE: time 1.919e-05/0.6459, allocations: 9.562 kB / 0.7962 GB, free: 12.37 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 8.206e-06/0.6459, allocations: 2.812 kB / 0.7962 GB, free: 12.37 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (initialization): time 2.095e-05/0.6459, allocations: 4.062 kB / 0.7962 GB, free: 12.37 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004411/0.6464, allocations: 104.6 kB / 0.7963 GB, free: 12.34 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.094e-05/0.6464, allocations: 5.5 kB / 0.7963 GB, free: 12.34 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0004714/0.6469, allocations: 53.31 kB / 0.7964 GB, free: 12.3 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 6.024e-05/0.6469, allocations: 20.12 kB / 0.7964 GB, free: 12.3 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 10
 * 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 (51):
 * Single equations (assignments): 51
 * 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 0.0003991/0.6473, allocations: 188.3 kB / 0.7966 GB, free: 12.14 MB / 0.5919 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001557/0.6475, allocations: 87.81 kB / 0.7967 GB, free: 12.09 MB / 0.5919 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001403/0.6489, allocations: 0.597 MB / 0.7973 GB, free: 11.77 MB / 0.5919 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 9.117e-06/0.6489, allocations: 3.125 kB / 0.7973 GB, free: 11.77 MB / 0.5919 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.709e-06/0.6489, allocations: 0 / 0.7973 GB, free: 11.77 MB / 0.5919 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.32e-05/0.6489, allocations: 13.53 kB / 0.7973 GB, free: 11.77 MB / 0.5919 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0008098/0.6497, allocations: 476.8 kB / 0.7977 GB, free: 11.43 MB / 0.5919 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.98e-06/0.6497, allocations: 0 / 0.7977 GB, free: 11.43 MB / 0.5919 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0003456/0.6501, allocations: 76.17 kB / 0.7978 GB, free: 11.41 MB / 0.5919 GB
Notification: Performance of postOpt tearingSystem (simulation): time 6.202e-06/0.6501, allocations: 1.125 kB / 0.7978 GB, free: 11.41 MB / 0.5919 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.752e-05/0.6501, allocations: 7.969 kB / 0.7978 GB, free: 11.4 MB / 0.5919 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 7.344e-06/0.6501, allocations: 9.984 kB / 0.7978 GB, free: 11.39 MB / 0.5919 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.004e-06/0.6501, allocations: 0 / 0.7978 GB, free: 11.39 MB / 0.5919 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.00091/0.651, allocations: 422.4 kB / 0.7982 GB, free: 11.16 MB / 0.5919 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002647/0.6513, allocations: 110.5 kB / 0.7983 GB, free: 11.07 MB / 0.5919 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 8.002e-05/0.6514, allocations: 10.03 kB / 0.7983 GB, free: 11.07 MB / 0.5919 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002514/0.6516, allocations: 16.36 kB / 0.7983 GB, free: 11.06 MB / 0.5919 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 9.676e-05/0.6517, allocations: 29.8 kB / 0.7984 GB, free: 11.04 MB / 0.5919 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 4.167e-05/0.6518, allocations: 26.3 kB / 0.7984 GB, free: 11.02 MB / 0.5919 GB
Notification: Performance of sorting global known variables: time 0.0005971/0.6524, allocations: 451.1 kB / 0.7988 GB, free: 10.77 MB / 0.5919 GB
Notification: Performance of sort global known variables: time 8e-08/0.6524, allocations: 0 / 0.7988 GB, free: 10.77 MB / 0.5919 GB
Notification: Performance of remove unused functions: time 0.001196/0.6536, allocations: 375.8 kB / 0.7992 GB, free: 10.65 MB / 0.5919 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (38):
 * Single equations (assignments): 37
 * 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 0.001018/0.6546, allocations: 490.2 kB / 0.7997 GB, free: 10.41 MB / 0.5919 GB
Notification: Performance of simCode: created initialization part: time 0.0008839/0.6555, allocations: 300.1 kB / 0.7999 GB, free: 10.29 MB / 0.5919 GB
Notification: Performance of simCode: created event and clocks part: time 5.881e-06/0.6555, allocations: 5.844 kB / 0.7999 GB, free: 10.29 MB / 0.5919 GB
Notification: Performance of simCode: created simulation system equations: time 0.0003712/0.6558, allocations: 149.7 kB / 0.8001 GB, free: 10.22 MB / 0.5919 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001471/0.6573, allocations: 292.3 kB / 0.8004 GB, free: 10.09 MB / 0.5919 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.002872/0.6602, allocations: 1.308 MB / 0.8016 GB, free: 9.277 MB / 0.5919 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0004661/0.6606, allocations: 375.1 kB / 0.802 GB, free: 9.055 MB / 0.5919 GB
Notification: Performance of simCode: alias equations: time 0.0007406/0.6614, allocations: 229.3 kB / 0.8022 GB, free: 8.949 MB / 0.5919 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001978/0.6616, allocations: 69.5 kB / 0.8023 GB, free: 8.93 MB / 0.5919 GB
Notification: Performance of SimCode: time 9.92e-07/0.6616, allocations: 0 / 0.8023 GB, free: 8.93 MB / 0.5919 GB
Notification: Performance of Templates: time 0.02871/0.6903, allocations: 15.56 MB / 0.8175 GB, free: 0.9141 MB / 0.5919 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,Time,_derdummy,_dummy,dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.instanceNameColor[1],dropOfCommons.instanceNameColor[2],dropOfCommons.instanceNameColor[3],dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,eta,fullMedium.L,fullMedium.P,fullMedium.P_nom,fullMedium.TC,fullMedium.adiabaticModel.eta_is,fullMedium.adiabaticModel.h_in,fullMedium.adiabaticModel.h_out,fullMedium.adiabaticModel.h_out_is,fullMedium.adiabaticModel.p_out,fullMedium.adiabaticModel.s_in,fullMedium.adiabaticModel.state_in.T,fullMedium.adiabaticModel.state_in.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

Variables in the result:dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,eta,fullMedium.L,fullMedium.P,fullMedium.P_in_internal,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.clip_p_out,fullMedium.dh,fullMedium.dp,fullMedium.dr_corr,fullMedium.etaSpec,fullMedium.eta_actual,fullMedium.eta_fixed,fullMedium.eta_is,fullMedium.h_in,fullMedium.h_out,fullMedium.initM_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.p_in,fullMedium.p_min,fullMedium.p_out,fullMedium.singularityRegime,incompressibleFluid.L,incompressibleFluid.P,incompressibleFluid.P_in_internal,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.clip_p_out,incompressibleFluid.dh,incompressibleFluid.dp,incompressibleFluid.dr_corr,incompressibleFluid.etaSpec,incompressibleFluid.eta_actual,incompressibleFluid.eta_fixed,incompressibleFluid.eta_is,incompressibleFluid.h_in,incompressibleFluid.h_out,incompressibleFluid.initM_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.p_in,incompressibleFluid.p_min,incompressibleFluid.p_out,incompressibleFluid.singularityRegime,isothermalReference.L,isothermalReference.P,isothermalReference.P_in_internal,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.clip_p_out,isothermalReference.dh,isothermalReference.dp,isothermalReference.dr_corr,isothermalReference.etaSpec,isothermalReference.eta_actual,isothermalReference.eta_fixed,isothermalReference.eta_is,isothermalReference.h_in,isothermalReference.h_out,isothermalReference.initM_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.p_in,isothermalReference.p_min,isothermalReference.p_out,isothermalReference.singularityRegime,pressureDifference.duration,pressureDifference.height,pressureDifference.offset,pressureDifference.startTime,pressureDifference.y,sink.L,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,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,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,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,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,source2.outlet.m_flow,source2.outlet.r,source2.outlet.state.T,source2.outlet.state.p,source2.p0,source2.p0_par,time
[Calling sys.exit(0), Time elapsed: 7.380303084850311]