Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.001714/0.001714, allocations: 84.73 kB / 19.43 MB, free: 332 kB / 13.93 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.002309/0.002309, allocations: 161.7 kB / 22.75 MB, free: 1.656 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 1.538/1.538, allocations: 177.1 MB / 203.1 MB, free: 5.629 MB / 186.7 MB
"
[Timeout remaining time 178]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 1.063/1.063, allocations: 118.6 MB / 378.2 MB, free: 1.504 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater")
translateModel(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|_derdummy|_dummy|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.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_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.963e-06/1.963e-06, allocations: 0 / 482.9 MB, free: 8.262 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.33e-05/2.527e-05, allocations: 2.312 kB / 482.9 MB, free: 8.258 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater): time 0.03255/0.03258, allocations: 26.69 MB / 0.4977 GB, free: 5.57 MB / 426.7 MB
Notification: Performance of NFInst.instExpressions: time 0.01073/0.04331, allocations: 6.362 MB / 0.5039 GB, free: 15.91 MB / 442.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001394/0.0447, allocations: 71.31 kB / 0.5039 GB, free: 15.84 MB / 442.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.001489/0.04619, allocations: 428.7 kB / 0.5044 GB, free: 15.42 MB / 442.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.004116/0.05031, allocations: 1.156 MB / 0.5055 GB, free: 14.26 MB / 442.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.002107/0.05241, allocations: 0.6772 MB / 0.5061 GB, free: 13.58 MB / 442.7 MB
Notification: Performance of NFFlatten.flatten: time 0.002556/0.05497, allocations: 1.58 MB / 0.5077 GB, free: 11.99 MB / 442.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0003652/0.05534, allocations: 123.8 kB / 0.5078 GB, free: 11.86 MB / 442.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001717/0.05705, allocations: 0.8801 MB / 0.5087 GB, free: 10.98 MB / 442.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005897/0.05764, allocations: 362.8 kB / 0.509 GB, free: 10.62 MB / 442.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001078/0.05775, allocations: 63.94 kB / 0.5091 GB, free: 10.56 MB / 442.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.001763/0.05951, allocations: 0.5923 MB / 0.5096 GB, free: 9.965 MB / 442.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0002089/0.05972, allocations: 179 kB / 0.5098 GB, free: 9.789 MB / 442.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0003948/0.06012, allocations: 307.1 kB / 0.5101 GB, free: 9.488 MB / 442.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.002787/0.0629, allocations: 1.608 MB / 0.5117 GB, free: 7.875 MB / 442.7 MB
Notification: Performance of FrontEnd - DAE generated: time 3.557e-06/0.06291, allocations: 0 / 0.5117 GB, free: 7.875 MB / 442.7 MB
Notification: Performance of FrontEnd: time 1.262e-06/0.06291, allocations: 0 / 0.5117 GB, free: 7.875 MB / 442.7 MB
Notification: Performance of Transformations before backend: time 1.09e-05/0.06292, allocations: 0 / 0.5117 GB, free: 7.875 MB / 442.7 MB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 157
 * Number of variables: 157
Notification: Performance of Generate backend data structure: time 0.002404/0.06532, allocations: 1.332 MB / 0.513 GB, free: 6.508 MB / 442.7 MB
Notification: Performance of prepare preOptimizeDAE: time 3.715e-05/0.06536, allocations: 8.031 kB / 0.513 GB, free: 6.5 MB / 442.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0003314/0.06569, allocations: 180.1 kB / 0.5132 GB, free: 6.324 MB / 442.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001632/0.06732, allocations: 0.7993 MB / 0.5139 GB, free: 5.488 MB / 442.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002393/0.06756, allocations: 208.1 kB / 0.5141 GB, free: 5.25 MB / 442.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001129/0.06768, allocations: 68.38 kB / 0.5142 GB, free: 5.184 MB / 442.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001373/0.06905, allocations: 0.7333 MB / 0.5149 GB, free: 4.41 MB / 442.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 1.506e-05/0.06906, allocations: 192 / 0.5149 GB, free: 4.41 MB / 442.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.963e-05/0.06912, allocations: 31.94 kB / 0.515 GB, free: 4.379 MB / 442.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.89e-05/0.06914, allocations: 16 kB / 0.515 GB, free: 4.363 MB / 442.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001263/0.07041, allocations: 0.6023 MB / 0.5156 GB, free: 3.762 MB / 442.7 MB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003308/0.07371, allocations: 2.159 MB / 0.5177 GB, free: 1.508 MB / 442.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.0007608/0.07448, allocations: 343.5 kB / 0.518 GB, free: 1.168 MB / 442.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004478/0.07492, allocations: 207.6 kB / 0.5182 GB, free: 0.9648 MB / 442.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.002259/0.07718, allocations: 0.9704 MB / 0.5191 GB, free: 15.97 MB / 458.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0001725/0.07735, allocations: 38.94 kB / 0.5192 GB, free: 15.92 MB / 458.7 MB
Notification: Performance of pre-optimization done (n=45): time 1.502e-06/0.07736, allocations: 0 / 0.5192 GB, free: 15.92 MB / 458.7 MB
Notification: Performance of matching and sorting (n=45): time 0.001377/0.07873, allocations: 0.5471 MB / 0.5197 GB, free: 15.37 MB / 458.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 6.465e-05/0.0788, allocations: 67.28 kB / 0.5198 GB, free: 15.29 MB / 458.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0008945/0.07969, allocations: 0.6694 MB / 0.5204 GB, free: 14.61 MB / 458.7 MB
Notification: Performance of collectPreVariables (initialization): time 3.855e-05/0.07973, allocations: 33.7 kB / 0.5205 GB, free: 14.57 MB / 458.7 MB
Notification: Performance of collectInitialEqns (initialization): time 0.0004154/0.08015, allocations: 464.5 kB / 0.5209 GB, free: 14.12 MB / 458.7 MB
Notification: Performance of collectInitialBindings (initialization): time 0.000155/0.0803, allocations: 166.5 kB / 0.5211 GB, free: 13.96 MB / 458.7 MB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001531/0.08045, allocations: 94.14 kB / 0.5212 GB, free: 13.86 MB / 458.7 MB
Notification: Performance of setup shared object (initialization): time 0.0001831/0.08064, allocations: 334 kB / 0.5215 GB, free: 13.53 MB / 458.7 MB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003361/0.08097, allocations: 124.9 kB / 0.5216 GB, free: 13.4 MB / 458.7 MB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004969/0.08147, allocations: 270.9 kB / 0.5218 GB, free: 13.08 MB / 458.7 MB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0008715/0.08234, allocations: 437.3 kB / 0.5223 GB, free: 12.6 MB / 458.7 MB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.841e-06/0.08235, allocations: 4 kB / 0.5223 GB, free: 12.59 MB / 458.7 MB
Notification: Performance of matching and sorting (n=62) (initialization): time 0.001157/0.08351, allocations: 0.5357 MB / 0.5228 GB, free: 12.05 MB / 458.7 MB
Notification: Performance of prepare postOptimizeDAE: time 2.142e-05/0.08353, allocations: 8 kB / 0.5228 GB, free: 12.04 MB / 458.7 MB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 8.817e-06/0.08354, allocations: 4 kB / 0.5228 GB, free: 12.04 MB / 458.7 MB
Notification: Performance of postOpt tearingSystem (initialization): time 2.101e-05/0.08356, allocations: 15.92 kB / 0.5228 GB, free: 12.02 MB / 458.7 MB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004299/0.08399, allocations: 111.8 kB / 0.5229 GB, free: 11.91 MB / 458.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 2.11e-05/0.08401, allocations: 19.86 kB / 0.5229 GB, free: 11.89 MB / 458.7 MB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0003283/0.08434, allocations: 60.08 kB / 0.523 GB, free: 11.84 MB / 458.7 MB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 5.393e-05/0.08439, allocations: 28 kB / 0.523 GB, free: 11.81 MB / 458.7 MB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 19
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (62):
 * Single equations (assignments): 62
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 0
 * Mixed (continuous/discrete) equation systems: 0
Notification: Performance of prepare postOptimizeDAE: time 0.0002923/0.08468, allocations: 197.7 kB / 0.5232 GB, free: 11.61 MB / 458.7 MB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001623/0.08484, allocations: 103.4 kB / 0.5233 GB, free: 11.5 MB / 458.7 MB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001403/0.08625, allocations: 0.7206 MB / 0.524 GB, free: 10.76 MB / 458.7 MB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 8.967e-06/0.08626, allocations: 4 kB / 0.524 GB, free: 10.75 MB / 458.7 MB
Notification: Performance of postOpt constantLinearSystem (simulation): time 6.862e-06/0.08626, allocations: 7.938 kB / 0.524 GB, free: 10.75 MB / 458.7 MB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.001e-06/0.08627, allocations: 3.984 kB / 0.524 GB, free: 10.74 MB / 458.7 MB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0006486/0.08692, allocations: 464.9 kB / 0.5245 GB, free: 10.26 MB / 458.7 MB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 3.056e-06/0.08692, allocations: 0 / 0.5245 GB, free: 10.26 MB / 458.7 MB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.000283/0.0872, allocations: 55.97 kB / 0.5245 GB, free: 10.2 MB / 458.7 MB
Notification: Performance of postOpt tearingSystem (simulation): time 3.266e-06/0.08721, allocations: 0 / 0.5245 GB, free: 10.2 MB / 458.7 MB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.593e-05/0.08723, allocations: 12 kB / 0.5245 GB, free: 10.19 MB / 458.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 6.943e-06/0.08724, allocations: 3.938 kB / 0.5245 GB, free: 10.19 MB / 458.7 MB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.503e-06/0.08724, allocations: 0 / 0.5245 GB, free: 10.19 MB / 458.7 MB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.000795/0.08804, allocations: 398.2 kB / 0.5249 GB, free: 9.781 MB / 458.7 MB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002123/0.08825, allocations: 103.3 kB / 0.525 GB, free: 9.68 MB / 458.7 MB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 7.381e-05/0.08832, allocations: 8 kB / 0.525 GB, free: 9.672 MB / 458.7 MB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0002093/0.08853, allocations: 15.98 kB / 0.525 GB, free: 9.656 MB / 458.7 MB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.023e-05/0.08861, allocations: 23.94 kB / 0.5251 GB, free: 9.633 MB / 458.7 MB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.26e-05/0.08863, allocations: 11.94 kB / 0.5251 GB, free: 9.621 MB / 458.7 MB
Notification: Performance of sorting global known variables: time 0.0007006/0.08934, allocations: 0.4917 MB / 0.5256 GB, free: 9.117 MB / 458.7 MB
Notification: Performance of sort global known variables: time 7.1e-08/0.08934, allocations: 0 / 0.5256 GB, free: 9.117 MB / 458.7 MB
Notification: Performance of remove unused functions: time 0.0008192/0.09015, allocations: 279.3 kB / 0.5258 GB, free: 8.844 MB / 458.7 MB
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 (31):
 * Single equations (assignments): 30
 * 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 0.000727/0.09088, allocations: 409 kB / 0.5262 GB, free: 8.445 MB / 458.7 MB
Notification: Performance of simCode: created initialization part: time 0.0008151/0.0917, allocations: 325.1 kB / 0.5265 GB, free: 8.129 MB / 458.7 MB
Notification: Performance of simCode: created event and clocks part: time 1.803e-06/0.0917, allocations: 128 / 0.5265 GB, free: 8.129 MB / 458.7 MB
Notification: Performance of simCode: created simulation system equations: time 0.0003272/0.09203, allocations: 132.3 kB / 0.5267 GB, free: 8 MB / 458.7 MB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001717/0.09374, allocations: 382.4 kB / 0.527 GB, free: 7.656 MB / 458.7 MB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.002358/0.0961, allocations: 1.304 MB / 0.5283 GB, free: 6.312 MB / 458.7 MB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.000436/0.09654, allocations: 386.8 kB / 0.5287 GB, free: 5.902 MB / 458.7 MB
Notification: Performance of simCode: alias equations: time 0.0004747/0.09701, allocations: 148.6 kB / 0.5288 GB, free: 5.789 MB / 458.7 MB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001557/0.09717, allocations: 76.47 kB / 0.5289 GB, free: 5.715 MB / 458.7 MB
Notification: Performance of SimCode: time 4.61e-07/0.09717, allocations: 0 / 0.5289 GB, free: 5.715 MB / 458.7 MB
Notification: Performance of Templates: time 0.02837/0.1255, allocations: 14.7 MB / 0.5432 GB, free: 7.391 MB / 474.7 MB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _derdummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _derdummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable _dummy in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable _dummy from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable fullMedium.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable fullMedium.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable incompressibleFluid.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable incompressibleFluid.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable isothermalReference.p_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable isothermalReference.p_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
Error: Could not read variable source2.outlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat.
Warning: Get data of variable source2.outlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 6.195319582999218]