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 0.001836/0.001836, allocations: 84.06 kB / 19.44 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 0.002025/0.002025, allocations: 173.3 kB / 22.77 MB, free: 1.648 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 1.565/1.565, allocations: 177.1 MB / 203.1 MB, free: 5.617 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 1.013/1.013, allocations: 118.6 MB / 378.2 MB, free: 1.484 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 1.974e-06/1.974e-06, allocations: 0 / 482.9 MB, free: 8.277 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 2.52e-05/2.717e-05, allocations: 2.312 kB / 482.9 MB, free: 8.273 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater): time 0.05378/0.05381, allocations: 29.96 MB / 0.5008 GB, free: 2.406 MB / 426.7 MB
Notification: Performance of NFInst.instExpressions: time 0.01173/0.06554, allocations: 7.261 MB / 0.5079 GB, free: 11.73 MB / 442.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001007/0.06655, allocations: 67.31 kB / 0.508 GB, free: 11.67 MB / 442.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.001245/0.06779, allocations: 428.7 kB / 0.5084 GB, free: 11.25 MB / 442.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.003096/0.07089, allocations: 1.16 MB / 0.5095 GB, free: 10.08 MB / 442.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.001871/0.07276, allocations: 0.6772 MB / 0.5102 GB, free: 9.398 MB / 442.7 MB
Notification: Performance of NFFlatten.flatten: time 0.002169/0.07493, allocations: 1.587 MB / 0.5118 GB, free: 7.809 MB / 442.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.000298/0.07523, allocations: 119.8 kB / 0.5119 GB, free: 7.68 MB / 442.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.001632/0.07686, allocations: 0.8801 MB / 0.5127 GB, free: 6.797 MB / 442.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0005864/0.07745, allocations: 358.8 kB / 0.5131 GB, free: 6.445 MB / 442.7 MB
Notification: Performance of NFPackage.collectConstants: time 0.0001118/0.07756, allocations: 60 kB / 0.5131 GB, free: 6.387 MB / 442.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.001599/0.07916, allocations: 0.604 MB / 0.5137 GB, free: 5.781 MB / 442.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0002181/0.07938, allocations: 175 kB / 0.5139 GB, free: 5.609 MB / 442.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0004337/0.07981, allocations: 303.1 kB / 0.5142 GB, free: 5.312 MB / 442.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.002757/0.08257, allocations: 1.608 MB / 0.5157 GB, free: 3.699 MB / 442.7 MB
Notification: Performance of FrontEnd - DAE generated: time 4.789e-06/0.08257, allocations: 3.938 kB / 0.5157 GB, free: 3.695 MB / 442.7 MB
Notification: Performance of FrontEnd: time 1.532e-06/0.08257, allocations: 0 / 0.5157 GB, free: 3.695 MB / 442.7 MB
Notification: Performance of Transformations before backend: time 1.369e-05/0.08259, allocations: 0 / 0.5157 GB, free: 3.695 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 0.00258/0.08517, allocations: 1.49 MB / 0.5172 GB, free: 2.164 MB / 442.7 MB
Notification: Performance of prepare preOptimizeDAE: time 4.19e-05/0.08521, allocations: 12.03 kB / 0.5172 GB, free: 2.152 MB / 442.7 MB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0003072/0.08552, allocations: 180.1 kB / 0.5174 GB, free: 1.977 MB / 442.7 MB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001646/0.08716, allocations: 0.8084 MB / 0.5182 GB, free: 1.133 MB / 442.7 MB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002381/0.0874, allocations: 208.1 kB / 0.5184 GB, free: 0.8945 MB / 442.7 MB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001105/0.08751, allocations: 64.36 kB / 0.5184 GB, free: 0.832 MB / 442.7 MB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001347/0.08886, allocations: 0.7097 MB / 0.5191 GB, free: 76 kB / 442.7 MB
Notification: Performance of preOpt findStateOrder (simulation): time 2.202e-05/0.08888, allocations: 4.188 kB / 0.5191 GB, free: 72 kB / 442.7 MB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 6.638e-05/0.08895, allocations: 31.94 kB / 0.5192 GB, free: 40 kB / 442.7 MB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.647e-05/0.08896, allocations: 12 kB / 0.5192 GB, free: 28 kB / 442.7 MB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.001123/0.09009, allocations: 468.9 kB / 0.5196 GB, free: 15.57 MB / 458.7 MB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.003911/0.094, allocations: 2.628 MB / 0.5222 GB, free: 12.84 MB / 458.7 MB
Notification: Performance of preOpt comSubExp (simulation): time 0.0007616/0.09476, allocations: 364.9 kB / 0.5225 GB, free: 12.47 MB / 458.7 MB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0004468/0.0952, allocations: 206.4 kB / 0.5227 GB, free: 12.27 MB / 458.7 MB
Notification: Performance of preOpt evalFunc (simulation): time 0.002378/0.09758, allocations: 1.072 MB / 0.5238 GB, free: 11.17 MB / 458.7 MB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.933e-05/0.09762, allocations: 45.75 kB / 0.5238 GB, free: 11.11 MB / 458.7 MB
Notification: Performance of pre-optimization done (n=45): time 1.753e-06/0.09762, allocations: 0 / 0.5238 GB, free: 11.11 MB / 458.7 MB
Notification: Performance of matching and sorting (n=45): time 0.001262/0.09889, allocations: 0.5315 MB / 0.5243 GB, free: 10.58 MB / 458.7 MB
Notification: Performance of inlineWhenForInitialization (initialization): time 5.552e-05/0.09894, allocations: 59.34 kB / 0.5244 GB, free: 10.51 MB / 458.7 MB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.001089/0.1, allocations: 0.8353 MB / 0.5252 GB, free: 9.656 MB / 458.7 MB
Notification: Performance of collectPreVariables (initialization): time 4.276e-05/0.1001, allocations: 37.7 kB / 0.5252 GB, free: 9.613 MB / 458.7 MB
Notification: Performance of collectInitialEqns (initialization): time 0.000516/0.1006, allocations: 0.5344 MB / 0.5258 GB, free: 9.074 MB / 458.7 MB
Notification: Performance of collectInitialBindings (initialization): time 0.0001655/0.1008, allocations: 170.6 kB / 0.5259 GB, free: 8.906 MB / 458.7 MB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001741/0.1009, allocations: 107.8 kB / 0.526 GB, free: 8.793 MB / 458.7 MB
Notification: Performance of setup shared object (initialization): time 0.0002916/0.1012, allocations: 0.5043 MB / 0.5265 GB, free: 8.281 MB / 458.7 MB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003141/0.1015, allocations: 124.9 kB / 0.5266 GB, free: 8.16 MB / 458.7 MB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0005234/0.1021, allocations: 332.6 kB / 0.527 GB, free: 7.758 MB / 458.7 MB
Notification: Performance of analyzeInitialSystem (initialization): time 0.000874/0.1029, allocations: 491.1 kB / 0.5274 GB, free: 7.199 MB / 458.7 MB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.707e-06/0.1029, allocations: 0 / 0.5274 GB, free: 7.199 MB / 458.7 MB
Notification: Performance of matching and sorting (n=62) (initialization): time 0.00109/0.104, allocations: 0.5322 MB / 0.528 GB, free: 6.66 MB / 458.7 MB
Notification: Performance of prepare postOptimizeDAE: time 1.727e-05/0.104, allocations: 4.062 kB / 0.528 GB, free: 6.656 MB / 458.7 MB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.017e-05/0.1041, allocations: 11.94 kB / 0.528 GB, free: 6.645 MB / 458.7 MB
Notification: Performance of postOpt tearingSystem (initialization): time 2.55e-05/0.1041, allocations: 8 kB / 0.528 GB, free: 6.637 MB / 458.7 MB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0004321/0.1045, allocations: 119.8 kB / 0.5281 GB, free: 6.52 MB / 458.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 1.919e-05/0.1045, allocations: 11.94 kB / 0.5281 GB, free: 6.508 MB / 458.7 MB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.000286/0.1048, allocations: 59.61 kB / 0.5282 GB, free: 6.449 MB / 458.7 MB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 4.895e-05/0.1049, allocations: 23.94 kB / 0.5282 GB, free: 6.426 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 0.00031/0.1052, allocations: 244.5 kB / 0.5284 GB, free: 6.176 MB / 458.7 MB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.000159/0.1053, allocations: 103.4 kB / 0.5285 GB, free: 6.074 MB / 458.7 MB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001528/0.1069, allocations: 0.8564 MB / 0.5294 GB, free: 5.176 MB / 458.7 MB
Notification: Performance of postOpt inlineArrayEqn (simulation): time 9.358e-06/0.1069, allocations: 4 kB / 0.5294 GB, free: 5.172 MB / 458.7 MB
Notification: Performance of postOpt constantLinearSystem (simulation): time 6.573e-06/0.1069, allocations: 3.938 kB / 0.5294 GB, free: 5.168 MB / 458.7 MB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 8.035e-06/0.1069, allocations: 3.984 kB / 0.5294 GB, free: 5.164 MB / 458.7 MB
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.0008195/0.1077, allocations: 0.5822 MB / 0.5299 GB, free: 4.547 MB / 458.7 MB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.675e-06/0.1077, allocations: 0 / 0.5299 GB, free: 4.547 MB / 458.7 MB
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0002563/0.108, allocations: 59.91 kB / 0.53 GB, free: 4.488 MB / 458.7 MB
Notification: Performance of postOpt tearingSystem (simulation): time 2.584e-06/0.108, allocations: 0 / 0.53 GB, free: 4.488 MB / 458.7 MB
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 1.95e-05/0.108, allocations: 8 kB / 0.53 GB, free: 4.48 MB / 458.7 MB
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 4.588e-06/0.108, allocations: 4 kB / 0.53 GB, free: 4.477 MB / 458.7 MB
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.172e-06/0.108, allocations: 0 / 0.53 GB, free: 4.477 MB / 458.7 MB
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0007627/0.1088, allocations: 405.2 kB / 0.5304 GB, free: 4.059 MB / 458.7 MB
Notification: Performance of postOpt removeConstants (simulation): time 0.0002192/0.109, allocations: 99.33 kB / 0.5305 GB, free: 3.961 MB / 458.7 MB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 8.003e-05/0.1091, allocations: 11.95 kB / 0.5305 GB, free: 3.949 MB / 458.7 MB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001836/0.1092, allocations: 8 kB / 0.5305 GB, free: 3.941 MB / 458.7 MB
Notification: Performance of postOpt findZeroCrossings (simulation): time 8.939e-05/0.1093, allocations: 23.95 kB / 0.5305 GB, free: 3.918 MB / 458.7 MB
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.692e-05/0.1094, allocations: 19.94 kB / 0.5305 GB, free: 3.898 MB / 458.7 MB
Notification: Performance of sorting global known variables: time 0.0007648/0.1101, allocations: 0.562 MB / 0.5311 GB, free: 3.324 MB / 458.7 MB
Notification: Performance of sort global known variables: time 6e-08/0.1101, allocations: 0 / 0.5311 GB, free: 3.324 MB / 458.7 MB
Notification: Performance of remove unused functions: time 0.0007861/0.1109, allocations: 283.2 kB / 0.5314 GB, free: 3.047 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 0.0006624/0.1116, allocations: 392.9 kB / 0.5317 GB, free: 2.664 MB / 458.7 MB
Notification: Performance of simCode: created initialization part: time 0.0007819/0.1123, allocations: 349.3 kB / 0.5321 GB, free: 2.32 MB / 458.7 MB
Notification: Performance of simCode: created event and clocks part: time 1.583e-06/0.1124, allocations: 0 / 0.5321 GB, free: 2.32 MB / 458.7 MB
Notification: Performance of simCode: created simulation system equations: time 0.0003051/0.1127, allocations: 139.6 kB / 0.5322 GB, free: 2.18 MB / 458.7 MB
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001756/0.1144, allocations: 386.7 kB / 0.5326 GB, free: 1.828 MB / 458.7 MB
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.002345/0.1168, allocations: 1.314 MB / 0.5339 GB, free: 484 kB / 458.7 MB
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0004374/0.1172, allocations: 382.8 kB / 0.5342 GB, free: 68 kB / 458.7 MB
Notification: Performance of simCode: alias equations: time 0.0004685/0.1177, allocations: 151.5 kB / 0.5344 GB, free: 15.95 MB / 474.7 MB
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0001504/0.1178, allocations: 72.41 kB / 0.5344 GB, free: 15.88 MB / 474.7 MB
Notification: Performance of SimCode: time 6.71e-07/0.1178, allocations: 0 / 0.5344 GB, free: 15.88 MB / 474.7 MB
Notification: Performance of Templates: time 0.03024/0.1481, allocations: 14.71 MB / 0.5488 GB, free: 1.535 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=240  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater.pipe 2>&1) [Timeout 240]
diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.AdiabaticThermodynamicModels.ConstantPropertyLiquidWater_ref.mat","/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: 6.25141851499211]