Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_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 0.0006179/0.0006179, allocations: 80.25 kB / 20.05 MB, free: 4.465 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 0.0007363/0.0007363, allocations: 173.9 kB / 23.36 MB, free: 1.156 MB / 18.57 MB " [Timeout remaining time 180] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.8475/0.8475, allocations: 177.2 MB / 203.7 MB, free: 5.707 MB / 186.7 MB " [Timeout remaining time 179] loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180] "Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.6951/0.6951, allocations: 116 MB / 376.2 MB, free: 4.16 MB / 346.7 MB " [Timeout remaining time 179] Using package ThermofluidStream with version 1.3.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo) Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo) Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo) Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo) Running command: translateModel(ThermofluidStream.Idealized.Examples.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_dev_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_dev_ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas") [Timeout 660] "Notification: Performance of FrontEnd - Absyn->SCode: time 2.123e-05/2.123e-05, allocations: 2.312 kB / 0.5548 GB, free: 12.65 MB / 490.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas): time 0.5168/0.5168, allocations: 137.5 MB / 0.6891 GB, free: 6.598 MB / 0.5573 GB Notification: Performance of NFInst.instExpressions: time 0.008475/0.5252, allocations: 8.686 MB / 0.6976 GB, free: 5.816 MB / 0.5573 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001331/0.5266, allocations: 49.75 kB / 0.6977 GB, free: 5.785 MB / 0.5573 GB Notification: Performance of NFTyping.typeComponents: time 0.001114/0.5277, allocations: 434.7 kB / 0.6981 GB, free: 5.609 MB / 0.5573 GB Notification: Performance of NFTyping.typeBindings: time 0.003515/0.5312, allocations: 1.454 MB / 0.6995 GB, free: 5.023 MB / 0.5573 GB Notification: Performance of NFTyping.typeClassSections: time 0.00222/0.5334, allocations: 1.033 MB / 0.7005 GB, free: 4.578 MB / 0.5573 GB Notification: Performance of NFFlatten.flatten: time 0.002769/0.5362, allocations: 2.396 MB / 0.7028 GB, free: 3.438 MB / 0.5573 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0003932/0.5366, allocations: 145.7 kB / 0.703 GB, free: 3.355 MB / 0.5573 GB Notification: Performance of NFEvalConstants.evaluate: time 0.001515/0.5381, allocations: 1.271 MB / 0.7042 GB, free: 2.871 MB / 0.5573 GB Notification: Performance of NFSimplifyModel.simplify: time 0.0007485/0.5389, allocations: 0.7396 MB / 0.7049 GB, free: 2.684 MB / 0.5573 GB Notification: Performance of NFPackage.collectConstants: time 8.855e-05/0.5389, allocations: 86.69 kB / 0.705 GB, free: 2.68 MB / 0.5573 GB Notification: Performance of NFFlatten.collectFunctions: time 0.002519/0.5415, allocations: 1.446 MB / 0.7064 GB, free: 2.215 MB / 0.5573 GB Notification: Performance of combineBinaries: time 0.0009138/0.5424, allocations: 2.233 MB / 0.7086 GB, free: 0.75 MB / 0.5573 GB Notification: Performance of replaceArrayConstructors: time 0.0004888/0.5429, allocations: 1.427 MB / 0.71 GB, free: 15.83 MB / 0.573 GB Notification: Performance of NFVerifyModel.verify: time 0.0001811/0.543, allocations: 119 kB / 0.7101 GB, free: 15.83 MB / 0.573 GB Notification: Performance of FrontEnd: time 0.0006882/0.5437, allocations: 327.1 kB / 0.7104 GB, free: 15.64 MB / 0.573 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 0.003906/0.5476, allocations: 5.425 MB / 0.7157 GB, free: 11.99 MB / 0.573 GB Notification: Performance of [SIM] FunctionAlias: time 0.001252/0.5489, allocations: 1.358 MB / 0.7171 GB, free: 11.03 MB / 0.573 GB Notification: Performance of [SIM] Early Inline: time 0.002664/0.5516, allocations: 3.791 MB / 0.7208 GB, free: 8.164 MB / 0.573 GB Notification: Performance of [SIM] Simplify 1: time 0.0005032/0.5521, allocations: 437.5 kB / 0.7212 GB, free: 7.875 MB / 0.573 GB Notification: Performance of [SIM] Alias: time 0.005136/0.5572, allocations: 5.191 MB / 0.7263 GB, free: 3.922 MB / 0.573 GB Notification: Performance of [SIM] Simplify 2: time 0.0003589/0.5576, allocations: 314.6 kB / 0.7266 GB, free: 3.723 MB / 0.573 GB Notification: Performance of [SIM] Remove Stream: time 0.0001902/0.5577, allocations: 285.5 kB / 0.7268 GB, free: 3.48 MB / 0.573 GB Notification: Performance of [SIM] Detect States: time 0.0007171/0.5585, allocations: 0.8035 MB / 0.7276 GB, free: 2.785 MB / 0.573 GB Notification: Performance of [SIM] Events: time 0.0001233/0.5586, allocations: 89.12 kB / 0.7277 GB, free: 2.727 MB / 0.573 GB Notification: Performance of [SIM] Partitioning: time 0.0009506/0.5595, allocations: 1.163 MB / 0.7288 GB, free: 1.98 MB / 0.573 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: 2.9830775381997228] Failed to read output from testmodel.py, exit status != 0: 0.5692555047571659 0.578853548 0.033429436 Calling exit ...