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 0.001657/0.001657, allocations: 81.3 kB / 20.05 MB, free: 1.48 MB / 14.72 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 0.00147/0.00147, allocations: 164.5 kB / 23.33 MB, free: 4.469 MB / 14.72 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 1.516/1.516, allocations: 177.1 MB / 203.7 MB, free: 9.133 MB / 190.1 MB " [Timeout remaining time 178] 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 1.094/1.094, allocations: 116 MB / 376.1 MB, free: 7.504 MB / 350.1 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 2.137e-05/2.137e-05, allocations: 9.312 kB / 0.5548 GB, free: 13.64 MB / 478.1 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.TUMExercisesThermodynamicCycles.Exercise4DieselEngine.AdiabaticPerfectGas): time 0.2058/0.2058, allocations: 137.5 MB / 0.6891 GB, free: 3.566 MB / 0.5919 GB Notification: Performance of NFInst.instExpressions: time 0.4156/0.6214, allocations: 8.673 MB / 0.6976 GB, free: 6.293 MB / 0.5919 GB Notification: Performance of NFInst.updateImplicitVariability: time 0.001604/0.623, allocations: 45.34 kB / 0.6976 GB, free: 6.293 MB / 0.5919 GB Notification: Performance of NFTyping.typeComponents: time 0.001592/0.6246, allocations: 446.3 kB / 0.698 GB, free: 6.285 MB / 0.5919 GB Notification: Performance of NFTyping.typeBindings: time 0.005037/0.6296, allocations: 1.444 MB / 0.6995 GB, free: 6.242 MB / 0.5919 GB Notification: Performance of NFTyping.typeClassSections: time 0.003771/0.6334, allocations: 1.036 MB / 0.7005 GB, free: 6.215 MB / 0.5919 GB Notification: Performance of NFFlatten.flatten: time 0.00413/0.6375, allocations: 2.4 MB / 0.7028 GB, free: 5.992 MB / 0.5919 GB Notification: Performance of NFFlatten.resolveConnections: time 0.0005191/0.638, allocations: 134.6 kB / 0.7029 GB, free: 5.957 MB / 0.5919 GB Notification: Performance of NFEvalConstants.evaluate: time 0.00246/0.6405, allocations: 1.277 MB / 0.7042 GB, free: 5.836 MB / 0.5919 GB Notification: Performance of NFSimplifyModel.simplify: time 0.001334/0.6418, allocations: 0.7383 MB / 0.7049 GB, free: 5.758 MB / 0.5919 GB Notification: Performance of NFPackage.collectConstants: time 0.0001915/0.642, allocations: 85.41 kB / 0.705 GB, free: 5.758 MB / 0.5919 GB Notification: Performance of NFFlatten.collectFunctions: time 0.006021/0.648, allocations: 1.451 MB / 0.7064 GB, free: 5.648 MB / 0.5919 GB Notification: Performance of combineBinaries: time 0.002334/0.6504, allocations: 2.233 MB / 0.7086 GB, free: 4.742 MB / 0.5919 GB Notification: Performance of replaceArrayConstructors: time 0.0009654/0.6513, allocations: 1.421 MB / 0.71 GB, free: 3.98 MB / 0.5919 GB Notification: Performance of NFVerifyModel.verify: time 0.0003886/0.6517, allocations: 114.9 kB / 0.7101 GB, free: 3.98 MB / 0.5919 GB Notification: Performance of FrontEnd: time 0.0009995/0.6527, allocations: 334 kB / 0.7104 GB, free: 3.957 MB / 0.5919 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 0.004919/0.6576, allocations: 5.432 MB / 0.7157 GB, free: 2.027 MB / 0.5919 GB Notification: Performance of [SIM] FunctionAlias: time 0.001618/0.6593, allocations: 1.353 MB / 0.717 GB, free: 1.594 MB / 0.5919 GB Notification: Performance of [SIM] Early Inline: time 0.003591/0.6628, allocations: 3.774 MB / 0.7207 GB, free: 1.371 MB / 0.5919 GB Notification: Performance of [SIM] Simplify 1: time 0.0006956/0.6635, allocations: 436.3 kB / 0.7211 GB, free: 1.227 MB / 0.5919 GB Notification: Performance of [SIM] Alias: time 0.006541/0.6701, allocations: 5.185 MB / 0.7262 GB, free: 15.28 MB / 0.6075 GB Notification: Performance of [SIM] Simplify 2: time 0.0005043/0.6706, allocations: 311.5 kB / 0.7265 GB, free: 15.18 MB / 0.6075 GB Notification: Performance of [SIM] Remove Stream: time 0.0003054/0.6709, allocations: 280 kB / 0.7268 GB, free: 15.09 MB / 0.6075 GB Notification: Performance of [SIM] Detect States: time 0.0009192/0.6718, allocations: 0.786 MB / 0.7275 GB, free: 14.87 MB / 0.6075 GB Notification: Performance of [SIM] Events: time 0.0001628/0.672, allocations: 79.33 kB / 0.7276 GB, free: 14.87 MB / 0.6075 GB Notification: Performance of [SIM] Partitioning: time 0.001567/0.6735, allocations: 1.163 MB / 0.7287 GB, free: 14.59 MB / 0.6075 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: 4.463357664644718] Failed to read output from testmodel.py, exit status != 0: 0.6888328418135643 0.701734063 0.045869906 Calling exit ...