Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas.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 0.001423/0.001423, allocations: 88.88 kB / 20.22 MB, free: 4.184 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.001536/0.001536, allocations: 173.6 kB / 23.54 MB, free: 0.8633 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 1.488/1.488, allocations: 177.1 MB / 203.9 MB, free: 5.598 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 1.011/1.011, allocations: 118.6 MB / 379 MB, free: 1.477 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.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|T1|T3|Time|_derdummy|_dummy|combustion.L|combustion.P|combustion.Q_flow|combustion.T_out_fixed|combustion.assertionLevel|combustion.clip_p_out|combustion.dT|combustion.dT_fixed|combustion.dh|combustion.dh_fixed|combustion.dp|combustion.dr_corr|combustion.du|combustion.h_in|combustion.h_out|combustion.h_out_fixed|combustion.initM_flow|der.combustion.inlet.m_flow.|combustion.inlet.m_flow|combustion.inlet.r|combustion.inlet.state.T|combustion.inlet.state.p|combustion.m_acceleration_0|combustion.m_flow|combustion.m_flowStateSelect|combustion.m_flow_0|combustion.outlet.m_flow|combustion.outlet.r|combustion.outlet.state.T|combustion.outlet.state.p|combustion.outletSpec|combustion.outletSpec_actual|combustion.outletValueSpec|combustion.p|combustion.p_in|combustion.p_inf|combustion.p_min|combustion.p_out|combustion.q|combustion.rho_in|combustion.rho_out|combustion.singularityRegime|combustion.systemSpec|combustion.u_in|combustion.u_out|combustion.v_in|combustion.v_out|combustion.w_amb|combustion.w_exp|combustion.w_exp_net|compression.L|compression.P|compression.P_nom|compression.P_out|compression.TC|compression.adiabaticModel.T_out|compression.adiabaticModel.T_out_is|compression.adiabaticModel.Z_in|compression.adiabaticModel.Z_out|compression.adiabaticModel.assertionLevel|compression.adiabaticModel.cp|compression.adiabaticModel.cpSpec|compression.adiabaticModel.cp_fixed|compression.adiabaticModel.cp_in|compression.adiabaticModel.cp_out|compression.adiabaticModel.delta_cp_rel|compression.adiabaticModel.delta_gamma_rel|compression.adiabaticModel.eta_is|compression.adiabaticModel.gamma|compression.adiabaticModel.gammaSpec|compression.adiabaticModel.gamma_fixed|compression.adiabaticModel.gamma_in|compression.adiabaticModel.gamma_out|compression.adiabaticModel.h_out|compression.adiabaticModel.isCpWithinTol|compression.adiabaticModel.isGammaWithinTol|compression.adiabaticModel.isInletIdealGas|compression.adiabaticModel.isOutletIdealGas|compression.adiabaticModel.p_out|compression.adiabaticModel.relTolCp|compression.adiabaticModel.relTolGamma|compression.adiabaticModel.relTolZ|compression.adiabaticModel.state_in.T|compression.adiabaticModel.state_in.p|compression.adiabaticModel.state_out.T|compression.adiabaticModel.state_out.p|compression.adiabaticModel.w_t|compression.adiabaticModel.w_t_is|compression.assertionLevel|compression.clip_p_out|compression.dh|compression.dp|compression.dp_fixed|compression.dp_nom|compression.dp_start|compression.dr_corr|compression.etaSpec|compression.eta_actual|compression.eta_fixed|compression.eta_is|compression.h_in|compression.h_out|compression.initM_flow|der.compression.inlet.m_flow.|compression.inlet.m_flow|compression.inlet.r|compression.inlet.state.T|compression.inlet.state.p|compression.m_acceleration_0|compression.m_flow|compression.m_flowStateSelect|compression.m_flow_0|compression.outlet.m_flow|compression.outlet.r|compression.outlet.state.T|compression.outlet.state.p|compression.outletSpec|compression.outletSpec_actual|compression.outletValueSpec|compression.pRatio|compression.pRatio_fixed|compression.p_in|compression.p_min|compression.p_out|compression.p_out_fixed|compression.singularityRegime|compressionRatio|density1.y|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|efficiency.displayVariablefinal|efficiency.showNumber|efficiency.significantDigits|exhaustTemperature.displayVariablefinal|exhaustTemperature.showNumber|exhaustTemperature.significantDigits|expansion.L|expansion.P|expansion.P_nom|expansion.P_out|expansion.TC|expansion.adiabaticModel.T_out|expansion.adiabaticModel.T_out_is|expansion.adiabaticModel.Z_in|expansion.adiabaticModel.Z_out|expansion.adiabaticModel.assertionLevel|expansion.adiabaticModel.cp|expansion.adiabaticModel.cpSpec|expansion.adiabaticModel.cp_fixed|expansion.adiabaticModel.cp_in|expansion.adiabaticModel.cp_out|expansion.adiabaticModel.delta_cp_rel|expansion.adiabaticModel.delta_gamma_rel|expansion.adiabaticModel.eta_is|expansion.adiabaticModel.gamma|expansion.adiabaticModel.gammaSpec|expansion.adiabaticModel.gamma_fixed|expansion.adiabaticModel.gamma_in|expansion.adiabaticModel.gamma_out|expansion.adiabaticModel.h_out|expansion.adiabaticModel.isCpWithinTol|expansion.adiabaticModel.isGammaWithinTol|expansion.adiabaticModel.isInletIdealGas|expansion.adiabaticModel.isOutletIdealGas|expansion.adiabaticModel.p_out|expansion.adiabaticModel.relTolCp|expansion.adiabaticModel.relTolGamma|expansion.adiabaticModel.relTolZ|expansion.adiabaticModel.state_in.T|expansion.adiabaticModel.state_in.p|expansion.adiabaticModel.state_out.T|expansion.adiabaticModel.state_out.p|expansion.adiabaticModel.w_t|expansion.adiabaticModel.w_t_is|expansion.assertionLevel|expansion.clip_p_out|expansion.dh|expansion.dp|expansion.dp_fixed|expansion.dp_nom|expansion.dp_start|expansion.dr_corr|expansion.etaSpec|expansion.eta_actual|expansion.eta_fixed|expansion.eta_is|expansion.h_in|expansion.h_out|expansion.initM_flow|der.expansion.inlet.m_flow.|expansion.inlet.m_flow|expansion.inlet.r|expansion.inlet.state.T|expansion.inlet.state.p|expansion.m_acceleration_0|expansion.m_flow|expansion.m_flowStateSelect|expansion.m_flow_0|expansion.outlet.m_flow|expansion.outlet.r|expansion.outlet.state.T|expansion.outlet.state.p|expansion.outletSpec|expansion.outletSpec_actual|expansion.outletSpec_prescribed|expansion.outletValueSpec|expansion.pRatio|expansion.pRatio_fixed|expansion.p_in|expansion.p_min|expansion.p_out|expansion.p_out_fixed|expansion.singularityRegime|gamma|gasExchange.L|gasExchange.P|gasExchange.P_out|gasExchange.Q_flow|gasExchange.T_out_fixed|gasExchange.assertionLevel|gasExchange.clip_p_out|gasExchange.dT|gasExchange.dT_fixed|gasExchange.dp|gasExchange.dp_start|gasExchange.dr_corr|gasExchange.du|gasExchange.h_in|gasExchange.h_out|gasExchange.initM_flow|der.gasExchange.inlet.m_flow.|gasExchange.inlet.m_flow|gasExchange.inlet.r|gasExchange.inlet.state.T|gasExchange.inlet.state.p|gasExchange.m_acceleration_0|gasExchange.m_flow|gasExchange.m_flowStateSelect|gasExchange.m_flow_0|gasExchange.outlet.m_flow|gasExchange.outlet.r|gasExchange.outlet.state.T|gasExchange.outlet.state.p|gasExchange.outletSpec|gasExchange.outletSpec_actual|gasExchange.outletValueSpec|gasExchange.p_in|gasExchange.p_min|gasExchange.p_out|gasExchange.rho|gasExchange.singularityRegime|gasExchange.systemSpec|gasExchange.u_in|gasExchange.u_out|gasExchange.w_p|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.p|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.p|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|m_flow|maximumPressure.displayVariablefinal|maximumPressure.showNumber|maximumPressure.significantDigits|netWork.displayVariablefinal|netWork.showNumber|netWork.significantDigits|p1|p2|rho1|rho2|sensorDensity1.TC|sensorDensity1.digits|sensorDensity1.direct_value|sensorDensity1.getQuantity.quantity|sensorDensity1.getQuantity.r|sensorDensity1.getQuantity.rho_min|sensorDensity1.getQuantity.state.T|sensorDensity1.getQuantity.state.p|sensorDensity1.getQuantity.value|sensorDensity1.init|sensorDensity1.inlet.m_flow|sensorDensity1.inlet.r|sensorDensity1.inlet.state.T|sensorDensity1.inlet.state.p|sensorDensity1.quantity|sensorDensity1.rho_min|sensorDensity1.value|sensorDensity1.value_0|sensorDensity1.value_out|shaftPower.E_flow_in.1.|shaftPower.E_flow_in.2.|shaftPower.E_flow_in.3.|shaftPower.E_flow_out|v1|v2",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas")
translateModel(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|T1|T3|Time|_derdummy|_dummy|combustion.L|combustion.P|combustion.Q_flow|combustion.T_out_fixed|combustion.assertionLevel|combustion.clip_p_out|combustion.dT|combustion.dT_fixed|combustion.dh|combustion.dh_fixed|combustion.dp|combustion.dr_corr|combustion.du|combustion.h_in|combustion.h_out|combustion.h_out_fixed|combustion.initM_flow|der.combustion.inlet.m_flow.|combustion.inlet.m_flow|combustion.inlet.r|combustion.inlet.state.T|combustion.inlet.state.p|combustion.m_acceleration_0|combustion.m_flow|combustion.m_flowStateSelect|combustion.m_flow_0|combustion.outlet.m_flow|combustion.outlet.r|combustion.outlet.state.T|combustion.outlet.state.p|combustion.outletSpec|combustion.outletSpec_actual|combustion.outletValueSpec|combustion.p|combustion.p_in|combustion.p_inf|combustion.p_min|combustion.p_out|combustion.q|combustion.rho_in|combustion.rho_out|combustion.singularityRegime|combustion.systemSpec|combustion.u_in|combustion.u_out|combustion.v_in|combustion.v_out|combustion.w_amb|combustion.w_exp|combustion.w_exp_net|compression.L|compression.P|compression.P_nom|compression.P_out|compression.TC|compression.adiabaticModel.T_out|compression.adiabaticModel.T_out_is|compression.adiabaticModel.Z_in|compression.adiabaticModel.Z_out|compression.adiabaticModel.assertionLevel|compression.adiabaticModel.cp|compression.adiabaticModel.cpSpec|compression.adiabaticModel.cp_fixed|compression.adiabaticModel.cp_in|compression.adiabaticModel.cp_out|compression.adiabaticModel.delta_cp_rel|compression.adiabaticModel.delta_gamma_rel|compression.adiabaticModel.eta_is|compression.adiabaticModel.gamma|compression.adiabaticModel.gammaSpec|compression.adiabaticModel.gamma_fixed|compression.adiabaticModel.gamma_in|compression.adiabaticModel.gamma_out|compression.adiabaticModel.h_out|compression.adiabaticModel.isCpWithinTol|compression.adiabaticModel.isGammaWithinTol|compression.adiabaticModel.isInletIdealGas|compression.adiabaticModel.isOutletIdealGas|compression.adiabaticModel.p_out|compression.adiabaticModel.relTolCp|compression.adiabaticModel.relTolGamma|compression.adiabaticModel.relTolZ|compression.adiabaticModel.state_in.T|compression.adiabaticModel.state_in.p|compression.adiabaticModel.state_out.T|compression.adiabaticModel.state_out.p|compression.adiabaticModel.w_t|compression.adiabaticModel.w_t_is|compression.assertionLevel|compression.clip_p_out|compression.dh|compression.dp|compression.dp_fixed|compression.dp_nom|compression.dp_start|compression.dr_corr|compression.etaSpec|compression.eta_actual|compression.eta_fixed|compression.eta_is|compression.h_in|compression.h_out|compression.initM_flow|der.compression.inlet.m_flow.|compression.inlet.m_flow|compression.inlet.r|compression.inlet.state.T|compression.inlet.state.p|compression.m_acceleration_0|compression.m_flow|compression.m_flowStateSelect|compression.m_flow_0|compression.outlet.m_flow|compression.outlet.r|compression.outlet.state.T|compression.outlet.state.p|compression.outletSpec|compression.outletSpec_actual|compression.outletValueSpec|compression.pRatio|compression.pRatio_fixed|compression.p_in|compression.p_min|compression.p_out|compression.p_out_fixed|compression.singularityRegime|compressionRatio|density1.y|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|efficiency.displayVariablefinal|efficiency.showNumber|efficiency.significantDigits|exhaustTemperature.displayVariablefinal|exhaustTemperature.showNumber|exhaustTemperature.significantDigits|expansion.L|expansion.P|expansion.P_nom|expansion.P_out|expansion.TC|expansion.adiabaticModel.T_out|expansion.adiabaticModel.T_out_is|expansion.adiabaticModel.Z_in|expansion.adiabaticModel.Z_out|expansion.adiabaticModel.assertionLevel|expansion.adiabaticModel.cp|expansion.adiabaticModel.cpSpec|expansion.adiabaticModel.cp_fixed|expansion.adiabaticModel.cp_in|expansion.adiabaticModel.cp_out|expansion.adiabaticModel.delta_cp_rel|expansion.adiabaticModel.delta_gamma_rel|expansion.adiabaticModel.eta_is|expansion.adiabaticModel.gamma|expansion.adiabaticModel.gammaSpec|expansion.adiabaticModel.gamma_fixed|expansion.adiabaticModel.gamma_in|expansion.adiabaticModel.gamma_out|expansion.adiabaticModel.h_out|expansion.adiabaticModel.isCpWithinTol|expansion.adiabaticModel.isGammaWithinTol|expansion.adiabaticModel.isInletIdealGas|expansion.adiabaticModel.isOutletIdealGas|expansion.adiabaticModel.p_out|expansion.adiabaticModel.relTolCp|expansion.adiabaticModel.relTolGamma|expansion.adiabaticModel.relTolZ|expansion.adiabaticModel.state_in.T|expansion.adiabaticModel.state_in.p|expansion.adiabaticModel.state_out.T|expansion.adiabaticModel.state_out.p|expansion.adiabaticModel.w_t|expansion.adiabaticModel.w_t_is|expansion.assertionLevel|expansion.clip_p_out|expansion.dh|expansion.dp|expansion.dp_fixed|expansion.dp_nom|expansion.dp_start|expansion.dr_corr|expansion.etaSpec|expansion.eta_actual|expansion.eta_fixed|expansion.eta_is|expansion.h_in|expansion.h_out|expansion.initM_flow|der.expansion.inlet.m_flow.|expansion.inlet.m_flow|expansion.inlet.r|expansion.inlet.state.T|expansion.inlet.state.p|expansion.m_acceleration_0|expansion.m_flow|expansion.m_flowStateSelect|expansion.m_flow_0|expansion.outlet.m_flow|expansion.outlet.r|expansion.outlet.state.T|expansion.outlet.state.p|expansion.outletSpec|expansion.outletSpec_actual|expansion.outletSpec_prescribed|expansion.outletValueSpec|expansion.pRatio|expansion.pRatio_fixed|expansion.p_in|expansion.p_min|expansion.p_out|expansion.p_out_fixed|expansion.singularityRegime|gamma|gasExchange.L|gasExchange.P|gasExchange.P_out|gasExchange.Q_flow|gasExchange.T_out_fixed|gasExchange.assertionLevel|gasExchange.clip_p_out|gasExchange.dT|gasExchange.dT_fixed|gasExchange.dp|gasExchange.dp_start|gasExchange.dr_corr|gasExchange.du|gasExchange.h_in|gasExchange.h_out|gasExchange.initM_flow|der.gasExchange.inlet.m_flow.|gasExchange.inlet.m_flow|gasExchange.inlet.r|gasExchange.inlet.state.T|gasExchange.inlet.state.p|gasExchange.m_acceleration_0|gasExchange.m_flow|gasExchange.m_flowStateSelect|gasExchange.m_flow_0|gasExchange.outlet.m_flow|gasExchange.outlet.r|gasExchange.outlet.state.T|gasExchange.outlet.state.p|gasExchange.outletSpec|gasExchange.outletSpec_actual|gasExchange.outletValueSpec|gasExchange.p_in|gasExchange.p_min|gasExchange.p_out|gasExchange.rho|gasExchange.singularityRegime|gasExchange.systemSpec|gasExchange.u_in|gasExchange.u_out|gasExchange.w_p|inverseBlockConstraints.u1|inverseBlockConstraints.u2|inverseBlockConstraints.y1|inverseBlockConstraints.y2|loopBreaker.L|loopBreaker.T_out|loopBreaker.T_out_fixed|loopBreaker.XiSpec|loopBreaker.assertionLevel|loopBreaker.dh|loopBreaker.dm_flow|loopBreaker.dp|loopBreaker.h_out|loopBreaker.h_out_fixed|loopBreaker.inlet.m_flow|loopBreaker.inlet.r|loopBreaker.inlet.state.T|loopBreaker.inlet.state.p|loopBreaker.m_flowSpec|loopBreaker.m_flow_in|loopBreaker.m_flow_in_par|der.loopBreaker.outlet.m_flow.|loopBreaker.outlet.m_flow|loopBreaker.outlet.r|loopBreaker.outlet.state.T|loopBreaker.outlet.state.p|loopBreaker.pSpec|loopBreaker.p_out|loopBreaker.p_out_fixed|loopBreaker.thermalSpec|loopBreaker.thermalValueSpec|loopBreaker.tol_Xi|loopBreaker.tol_h|loopBreaker.tol_m_flow|loopBreaker.tol_p|m_flow|maximumPressure.displayVariablefinal|maximumPressure.showNumber|maximumPressure.significantDigits|netWork.displayVariablefinal|netWork.showNumber|netWork.significantDigits|p1|p2|rho1|rho2|sensorDensity1.TC|sensorDensity1.digits|sensorDensity1.direct_value|sensorDensity1.getQuantity.quantity|sensorDensity1.getQuantity.r|sensorDensity1.getQuantity.rho_min|sensorDensity1.getQuantity.state.T|sensorDensity1.getQuantity.state.p|sensorDensity1.getQuantity.value|sensorDensity1.init|sensorDensity1.inlet.m_flow|sensorDensity1.inlet.r|sensorDensity1.inlet.state.T|sensorDensity1.inlet.state.p|sensorDensity1.quantity|sensorDensity1.rho_min|sensorDensity1.value|sensorDensity1.value_0|sensorDensity1.value_out|shaftPower.E_flow_in.1.|shaftPower.E_flow_in.2.|shaftPower.E_flow_in.3.|shaftPower.E_flow_out|v1|v2",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas") [Timeout 660]
"Notification: Performance of FrontEnd - Absyn->SCode: time 1.729e-05/1.729e-05, allocations: 2.312 kB / 483.7 MB, free: 8.266 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas): time 0.2235/0.2235, allocations: 137.6 MB / 0.6068 GB, free: 6.914 MB / 0.5261 GB
Notification: Performance of NFInst.instExpressions: time 0.02/0.2435, allocations: 8.718 MB / 0.6153 GB, free: 14.17 MB / 0.5417 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001329/0.2448, allocations: 51.5 kB / 0.6153 GB, free: 14.12 MB / 0.5417 GB
Notification: Performance of NFTyping.typeComponents: time 0.001823/0.2467, allocations: 440.5 kB / 0.6158 GB, free: 13.69 MB / 0.5417 GB
Notification: Performance of NFTyping.typeBindings: time 0.005993/0.2527, allocations: 1.463 MB / 0.6172 GB, free: 12.21 MB / 0.5417 GB
Notification: Performance of NFTyping.typeClassSections: time 0.002952/0.2556, allocations: 1.039 MB / 0.6182 GB, free: 11.17 MB / 0.5417 GB
Notification: Performance of NFFlatten.flatten: time 0.003186/0.2588, allocations: 2.433 MB / 0.6206 GB, free: 8.73 MB / 0.5417 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.000403/0.2592, allocations: 136 kB / 0.6207 GB, free: 8.578 MB / 0.5417 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.002065/0.2613, allocations: 1.297 MB / 0.622 GB, free: 7.277 MB / 0.5417 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.001313/0.2626, allocations: 0.7481 MB / 0.6227 GB, free: 6.527 MB / 0.5417 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001566/0.2627, allocations: 88 kB / 0.6228 GB, free: 6.441 MB / 0.5417 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.003329/0.2661, allocations: 1.446 MB / 0.6242 GB, free: 4.992 MB / 0.5417 GB
Notification: Performance of combineBinaries: time 0.002576/0.2686, allocations: 2.283 MB / 0.6264 GB, free: 2.688 MB / 0.5417 GB
Notification: Performance of replaceArrayConstructors: time 0.001511/0.2701, allocations: 1.456 MB / 0.6279 GB, free: 1.223 MB / 0.5417 GB
Notification: Performance of NFVerifyModel.verify: time 0.0002509/0.2704, allocations: 116 kB / 0.628 GB, free: 1.109 MB / 0.5417 GB
Notification: Performance of FrontEnd: time 0.0009907/0.2714, allocations: 339.1 kB / 0.6283 GB, free: 0.7773 MB / 0.5417 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 218 (208)
 * Number of variables: 218 (216)
Notification: Performance of [SIM] Bindings: time 0.00685/0.2782, allocations: 5.498 MB / 0.6337 GB, free: 11.08 MB / 0.5573 GB
Notification: Performance of [SIM] FunctionAlias: time 0.001985/0.2802, allocations: 1.4 MB / 0.635 GB, free: 9.742 MB / 0.5573 GB
Notification: Performance of [SIM] Early Inline: time 0.00774/0.288, allocations: 5.399 MB / 0.6403 GB, free: 4.34 MB / 0.5573 GB
Notification: Performance of [SIM] Simplify 1: time 0.0008626/0.2888, allocations: 445.5 kB / 0.6407 GB, free: 3.844 MB / 0.5573 GB
Notification: Performance of [SIM] Alias: time 0.2344/0.5232, allocations: 5.41 MB / 0.646 GB, free: 27.37 MB / 0.5573 GB
Notification: Performance of [SIM] Simplify 2: time 0.000486/0.5237, allocations: 301.1 kB / 0.6463 GB, free: 27.29 MB / 0.5573 GB
Notification: Performance of [SIM] Remove Stream: time 0.0002934/0.524, allocations: 275 kB / 0.6466 GB, free: 27.19 MB / 0.5573 GB
Notification: Performance of [SIM] Detect States: time 0.0006266/0.5246, allocations: 0.6747 MB / 0.6472 GB, free: 27.04 MB / 0.5573 GB
Notification: Performance of [SIM] Events: time 0.0002421/0.5248, allocations: 255.1 kB / 0.6475 GB, free: 27.04 MB / 0.5573 GB
Notification: Performance of [SIM] Partitioning: time 0.001341/0.5262, allocations: 1.107 MB / 0.6485 GB, free: 26.77 MB / 0.5573 GB
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	final Real expansion.adiabaticModel.isCpWithinTol = CAST(Real, sign(expansion.adiabaticModel.relTolCp - expansion.adiabaticModel.delta_cp_rel))
### Equation:
	[SCAL] (1) expansion.adiabaticModel.isCpWithinTol = sign(expansion.adiabaticModel.relTolCp - expansion.adiabaticModel.delta_cp_rel); ($RES_AUX_267)
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	final Real expansion.adiabaticModel.isGammaWithinTol = CAST(Real, sign(expansion.adiabaticModel.relTolGamma - expansion.adiabaticModel.delta_gamma_rel))
### Equation:
	[SCAL] (1) expansion.adiabaticModel.isGammaWithinTol = sign(expansion.adiabaticModel.relTolGamma - expansion.adiabaticModel.delta_gamma_rel); ($RES_AUX_262)
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	final Real compression.adiabaticModel.isCpWithinTol = CAST(Real, sign(compression.adiabaticModel.relTolCp - compression.adiabaticModel.delta_cp_rel))
### Equation:
	[SCAL] (1) compression.adiabaticModel.isCpWithinTol = sign(compression.adiabaticModel.relTolCp - compression.adiabaticModel.delta_cp_rel); ($RES_AUX_243)
Error: NBCausalize.checkSystemVariabilities failed. The following strong component has conflicting types: Real != Integer
BLOCK: Single Strong Component (status = Solve.UNPROCESSED, size = 1)
-----------------------------------------------------------------------
### Variable:
	final Real compression.adiabaticModel.isGammaWithinTol = CAST(Real, sign(compression.adiabaticModel.relTolGamma - compression.adiabaticModel.delta_gamma_rel))
### Equation:
	[SCAL] (1) compression.adiabaticModel.isGammaWithinTol = sign(compression.adiabaticModel.relTolGamma - compression.adiabaticModel.delta_gamma_rel); ($RES_AUX_238)
"
[Timeout remaining time 659]
[Calling sys.exit(0), Time elapsed: 3.894199390007998]