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 0.0007519/0.0007519, allocations: 80.25 kB / 20.03 MB, free: 4.496 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.0008074/0.0008074, allocations: 173.9 kB / 23.33 MB, free: 1.191 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 0.8971/0.8971, allocations: 177.1 MB / 203.7 MB, free: 5.719 MB / 186.7 MB
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.6631/0.6631, allocations: 116 MB / 376.1 MB, free: 4.164 MB / 346.7 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 1.523e-06/1.523e-06, allocations: 0 / 0.5547 GB, free: 12.71 MB / 490.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.626e-05/2.778e-05, allocations: 2.312 kB / 0.5547 GB, free: 12.71 MB / 490.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.TableBased): time 0.03283/0.03286, allocations: 43.69 MB / 0.5974 GB, free: 0.8672 MB / 0.5105 GB
Notification: Performance of NFInst.instExpressions: time 0.003307/0.03617, allocations: 2.522 MB / 0.5999 GB, free: 14.34 MB / 0.5261 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0007245/0.03689, allocations: 67.38 kB / 0.5999 GB, free: 14.27 MB / 0.5261 GB
Notification: Performance of NFTyping.typeComponents: time 0.001115/0.038, allocations: 381 kB / 0.6003 GB, free: 13.89 MB / 0.5261 GB
Notification: Performance of NFTyping.typeBindings: time 0.004383/0.04239, allocations: 2.434 MB / 0.6027 GB, free: 11.45 MB / 0.5261 GB
Notification: Performance of NFTyping.typeClassSections: time 0.002119/0.04451, allocations: 1.296 MB / 0.6039 GB, free: 10.15 MB / 0.5261 GB
Notification: Performance of NFFlatten.flatten: time 0.001697/0.0462, allocations: 1.525 MB / 0.6054 GB, free: 8.617 MB / 0.5261 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003075/0.04651, allocations: 139.6 kB / 0.6056 GB, free: 8.469 MB / 0.5261 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.003757/0.05027, allocations: 2.872 MB / 0.6084 GB, free: 5.59 MB / 0.5261 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0004972/0.05077, allocations: 354.7 kB / 0.6087 GB, free: 5.242 MB / 0.5261 GB
Notification: Performance of NFPackage.collectConstants: time 8.271e-05/0.05085, allocations: 64 kB / 0.6088 GB, free: 5.18 MB / 0.5261 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.00466/0.05551, allocations: 4.51 MB / 0.6132 GB, free: 0.6602 MB / 0.5261 GB
Notification: Performance of NFScalarize.scalarize: time 0.0001724/0.05568, allocations: 167.1 kB / 0.6133 GB, free: 0.4961 MB / 0.5261 GB
Notification: Performance of NFVerifyModel.verify: time 0.0003322/0.05601, allocations: 295.1 kB / 0.6136 GB, free: 212 kB / 0.5261 GB
Notification: Performance of NFConvertDAE.convert: time 0.004658/0.06067, allocations: 2.095 MB / 0.6157 GB, free: 14.11 MB / 0.5417 GB
Notification: Performance of FrontEnd - DAE generated: time 9.899e-06/0.06068, allocations: 4 kB / 0.6157 GB, free: 14.1 MB / 0.5417 GB
Notification: Performance of FrontEnd: time 1.884e-06/0.06068, allocations: 8 kB / 0.6157 GB, free: 14.09 MB / 0.5417 GB
Notification: Performance of Transformations before backend: time 4.312e-05/0.06073, allocations: 0 / 0.6157 GB, free: 14.09 MB / 0.5417 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 0.002465/0.06319, allocations: 1.417 MB / 0.617 GB, free: 12.64 MB / 0.5417 GB
Notification: Performance of prepare preOptimizeDAE: time 3.946e-05/0.06323, allocations: 8.031 kB / 0.6171 GB, free: 12.63 MB / 0.5417 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0007562/0.06399, allocations: 208.1 kB / 0.6173 GB, free: 12.43 MB / 0.5417 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001101/0.06509, allocations: 0.767 MB / 0.618 GB, free: 11.63 MB / 0.5417 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001292/0.06522, allocations: 215.5 kB / 0.6182 GB, free: 11.38 MB / 0.5417 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 7.34e-05/0.06529, allocations: 67.95 kB / 0.6183 GB, free: 11.31 MB / 0.5417 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.000898/0.06619, allocations: 0.6937 MB / 0.6189 GB, free: 10.58 MB / 0.5417 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.384e-05/0.0662, allocations: 0 / 0.6189 GB, free: 10.58 MB / 0.5417 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 3.632e-05/0.06624, allocations: 28 kB / 0.619 GB, free: 10.55 MB / 0.5417 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.19e-05/0.06625, allocations: 16 kB / 0.619 GB, free: 10.54 MB / 0.5417 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0007212/0.06697, allocations: 484.9 kB / 0.6195 GB, free: 10.06 MB / 0.5417 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.00249/0.06946, allocations: 2.116 MB / 0.6215 GB, free: 7.855 MB / 0.5417 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.0007947/0.07026, allocations: 390.1 kB / 0.6219 GB, free: 7.465 MB / 0.5417 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0001849/0.07044, allocations: 141.3 kB / 0.622 GB, free: 7.324 MB / 0.5417 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.0002472/0.07069, allocations: 120.2 kB / 0.6221 GB, free: 7.207 MB / 0.5417 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 2.741e-05/0.07072, allocations: 34.84 kB / 0.6222 GB, free: 7.164 MB / 0.5417 GB
Notification: Performance of pre-optimization done (n=34): time 2.605e-06/0.07072, allocations: 0 / 0.6222 GB, free: 7.164 MB / 0.5417 GB
Notification: Performance of matching and sorting (n=34): time 0.0008921/0.07161, allocations: 499.9 kB / 0.6227 GB, free: 6.672 MB / 0.5417 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.845e-05/0.07164, allocations: 55.41 kB / 0.6227 GB, free: 6.605 MB / 0.5417 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005217/0.07216, allocations: 0.6535 MB / 0.6233 GB, free: 5.938 MB / 0.5417 GB
Notification: Performance of collectPreVariables (initialization): time 2.632e-05/0.07219, allocations: 33.7 kB / 0.6234 GB, free: 5.898 MB / 0.5417 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002228/0.07241, allocations: 472.3 kB / 0.6238 GB, free: 5.434 MB / 0.5417 GB
Notification: Performance of collectInitialBindings (initialization): time 7.148e-05/0.07248, allocations: 127 kB / 0.6239 GB, free: 5.309 MB / 0.5417 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 9.457e-05/0.07258, allocations: 90.09 kB / 0.624 GB, free: 5.215 MB / 0.5417 GB
Notification: Performance of setup shared object (initialization): time 8.356e-05/0.07266, allocations: 325.9 kB / 0.6243 GB, free: 4.891 MB / 0.5417 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0001761/0.07284, allocations: 124.9 kB / 0.6245 GB, free: 4.77 MB / 0.5417 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0002211/0.07306, allocations: 201.5 kB / 0.6247 GB, free: 4.543 MB / 0.5417 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0003962/0.07345, allocations: 340.1 kB / 0.625 GB, free: 4.18 MB / 0.5417 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 2.845e-06/0.07346, allocations: 0 / 0.625 GB, free: 4.18 MB / 0.5417 GB
Notification: Performance of matching and sorting (n=51) (initialization): time 0.0005729/0.07403, allocations: 472.3 kB / 0.6254 GB, free: 3.711 MB / 0.5417 GB
Notification: Performance of prepare postOptimizeDAE: time 1.858e-05/0.07405, allocations: 6.5 kB / 0.6254 GB, free: 3.707 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 8.326e-06/0.07406, allocations: 4 kB / 0.6254 GB, free: 3.703 MB / 0.5417 GB
Notification: Performance of postOpt tearingSystem (initialization): time 1.704e-05/0.07407, allocations: 4 kB / 0.6254 GB, free: 3.699 MB / 0.5417 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002187/0.07429, allocations: 103.8 kB / 0.6255 GB, free: 3.598 MB / 0.5417 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 8.907e-06/0.0743, allocations: 4 kB / 0.6255 GB, free: 3.594 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0001814/0.07448, allocations: 51.72 kB / 0.6256 GB, free: 3.543 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.541e-05/0.07452, allocations: 24.19 kB / 0.6256 GB, free: 3.52 MB / 0.5417 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 0.0002083/0.07472, allocations: 197.6 kB / 0.6258 GB, free: 3.316 MB / 0.5417 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 7.063e-05/0.0748, allocations: 83.48 kB / 0.6259 GB, free: 3.234 MB / 0.5417 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.0007785/0.07557, allocations: 0.5904 MB / 0.6265 GB, free: 2.637 MB / 0.5417 GB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 9.548e-06/0.07558, allocations: 7.984 kB / 0.6265 GB, free: 2.629 MB / 0.5417 GB
Notification: Performance of postOpt constantLinearSystem (simulation): time 4.508e-06/0.07559, allocations: 0 / 0.6265 GB, free: 2.629 MB / 0.5417 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 5.841e-06/0.07559, allocations: 0 / 0.6265 GB, free: 2.629 MB / 0.5417 GB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.00043/0.07602, allocations: 480.7 kB / 0.6269 GB, free: 2.129 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.348e-06/0.07603, allocations: 3.938 kB / 0.6269 GB, free: 2.125 MB / 0.5417 GB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0001644/0.07619, allocations: 71.95 kB / 0.627 GB, free: 2.055 MB / 0.5417 GB
Notification: Performance of postOpt tearingSystem (simulation): time 3.497e-06/0.0762, allocations: 0 / 0.627 GB, free: 2.055 MB / 0.5417 GB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 1.674e-05/0.07621, allocations: 15.98 kB / 0.627 GB, free: 2.039 MB / 0.5417 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 2.655e-06/0.07622, allocations: 3.938 kB / 0.627 GB, free: 2.035 MB / 0.5417 GB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.483e-06/0.07622, allocations: 0 / 0.627 GB, free: 2.035 MB / 0.5417 GB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0004555/0.07667, allocations: 425.3 kB / 0.6274 GB, free: 1.602 MB / 0.5417 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001388/0.07681, allocations: 107.3 kB / 0.6275 GB, free: 1.496 MB / 0.5417 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 4.355e-05/0.07685, allocations: 4 kB / 0.6275 GB, free: 1.492 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001162/0.07697, allocations: 15.98 kB / 0.6275 GB, free: 1.477 MB / 0.5417 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 5.923e-05/0.07703, allocations: 31.95 kB / 0.6276 GB, free: 1.445 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.196e-05/0.07705, allocations: 15.98 kB / 0.6276 GB, free: 1.43 MB / 0.5417 GB
Notification: Performance of sorting global known variables: time 0.000345/0.0774, allocations: 451 kB / 0.628 GB, free: 0.9961 MB / 0.5417 GB
Notification: Performance of sort global known variables: time 2.2e-07/0.0774, allocations: 0 / 0.628 GB, free: 0.9961 MB / 0.5417 GB
Notification: Performance of remove unused functions: time 0.0009473/0.07834, allocations: 374.9 kB / 0.6284 GB, free: 0.6289 MB / 0.5417 GB
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 1
 * Number of states: 0 ()
 * Number of discrete variables: 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 0.0006594/0.079, allocations: 0.5025 MB / 0.6289 GB, free: 124 kB / 0.5417 GB
Notification: Performance of simCode: created initialization part: time 0.0004959/0.0795, allocations: 311.8 kB / 0.6292 GB, free: 15.82 MB / 0.5573 GB
Notification: Performance of simCode: created event and clocks part: time 3.176e-06/0.0795, allocations: 8.125 kB / 0.6292 GB, free: 15.81 MB / 0.5573 GB
Notification: Performance of simCode: created simulation system equations: time 0.0001895/0.07969, allocations: 143.8 kB / 0.6293 GB, free: 15.67 MB / 0.5573 GB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.0007479/0.08044, allocations: 317.2 kB / 0.6296 GB, free: 15.38 MB / 0.5573 GB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.001569/0.08201, allocations: 1.269 MB / 0.6309 GB, free: 14.08 MB / 0.5573 GB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0002368/0.08225, allocations: 375.8 kB / 0.6312 GB, free: 13.68 MB / 0.5573 GB
Notification: Performance of simCode: alias equations: time 0.0004162/0.08266, allocations: 211.4 kB / 0.6314 GB, free: 13.48 MB / 0.5573 GB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001088/0.08277, allocations: 80.41 kB / 0.6315 GB, free: 13.41 MB / 0.5573 GB
Notification: Performance of SimCode: time 7.32e-07/0.08277, allocations: 0 / 0.6315 GB, free: 13.41 MB / 0.5573 GB
Notification: Performance of Templates: time 0.2273/0.31, allocations: 14.36 MB / 0.6455 GB, free: 96.48 MB / 0.5573 GB
"
[Timeout remaining time 660]
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 -s cvode -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: 4.017944762483239]