startTime=0 stopTime=1 tolerance=1e-06 numberOfIntervals=100 stepSize=0.01 wasm-jit simulation: simulate(ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|NonlinearSystems.initialization.3..Calls|NonlinearSystems.initialization.3..Iterations|NonlinearSystems.initialization.3..Jacobians|NonlinearSystems.initialization.3..Residues|Time|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.P_out|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.d|fullMedium.adiabaticModel.state_in.h|fullMedium.adiabaticModel.state_in.p|fullMedium.adiabaticModel.state_in.phase|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.d|fullMedium.inlet.state.h|fullMedium.inlet.state.p|fullMedium.inlet.state.phase|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.d|fullMedium.outlet.state.h|fullMedium.outlet.state.p|fullMedium.outlet.state.phase|fullMedium.outletSpec|fullMedium.outletSpec_actual|fullMedium.outletValueSpec|fullMedium.pRatio|fullMedium.pRatio_fixed|fullMedium.p_in|fullMedium.p_min|fullMedium.p_out|fullMedium.p_out_fixed|fullMedium.singularityRegime|fullMedium1.L|fullMedium1.P|fullMedium1.P_in|fullMedium1.P_nom|fullMedium1.TC|fullMedium1.adiabaticModel.eta_is|fullMedium1.adiabaticModel.h_in|fullMedium1.adiabaticModel.h_out|fullMedium1.adiabaticModel.h_out_is|fullMedium1.adiabaticModel.p_out|fullMedium1.adiabaticModel.s_in|fullMedium1.adiabaticModel.state_in.T|fullMedium1.adiabaticModel.state_in.d|fullMedium1.adiabaticModel.state_in.h|fullMedium1.adiabaticModel.state_in.p|fullMedium1.adiabaticModel.state_in.phase|fullMedium1.adiabaticModel.w_t|fullMedium1.adiabaticModel.w_t_is|fullMedium1.assertionLevel|fullMedium1.clip_p_out|der.fullMedium1.dp.|fullMedium1.dh|fullMedium1.dp|fullMedium1.dp_fixed|fullMedium1.dp_nom|fullMedium1.dp_start|fullMedium1.dr_corr|fullMedium1.etaSpec|fullMedium1.eta_actual|fullMedium1.eta_fixed|fullMedium1.eta_is|fullMedium1.h_in|fullMedium1.h_out|fullMedium1.initM_flow|der.fullMedium1.inlet.m_flow.|fullMedium1.inlet.m_flow|fullMedium1.inlet.r|fullMedium1.inlet.state.T|fullMedium1.inlet.state.d|fullMedium1.inlet.state.h|fullMedium1.inlet.state.p|fullMedium1.inlet.state.phase|fullMedium1.m_acceleration_0|fullMedium1.m_flow|fullMedium1.m_flowStateSelect|fullMedium1.m_flow_0|fullMedium1.outlet.m_flow|fullMedium1.outlet.r|fullMedium1.outlet.state.T|fullMedium1.outlet.state.d|fullMedium1.outlet.state.h|fullMedium1.outlet.state.p|fullMedium1.outlet.state.phase|fullMedium1.outletSpec_actual|fullMedium1.pRatio|fullMedium1.pRatio_fixed|fullMedium1.p_in|fullMedium1.p_min|fullMedium1.p_out|fullMedium1.p_out_fixed|fullMedium1.singularityRegime|fullMedium2.L|fullMedium2.P|fullMedium2.P_in|fullMedium2.P_nom|fullMedium2.TC|fullMedium2.adiabaticModel.eta_is|fullMedium2.adiabaticModel.h_in|fullMedium2.adiabaticModel.h_out|fullMedium2.adiabaticModel.h_out_is|fullMedium2.adiabaticModel.p_out|fullMedium2.adiabaticModel.s_in|fullMedium2.adiabaticModel.state_in.T|fullMedium2.adiabaticModel.state_in.d|fullMedium2.adiabaticModel.state_in.h|fullMedium2.adiabaticModel.state_in.p|fullMedium2.adiabaticModel.state_in.phase|fullMedium2.adiabaticModel.w_t|fullMedium2.adiabaticModel.w_t_is|fullMedium2.assertionLevel|fullMedium2.clip_p_out|fullMedium2.dh|fullMedium2.dp|fullMedium2.dp_fixed|fullMedium2.dp_nom|fullMedium2.dp_start|fullMedium2.dr_corr|fullMedium2.etaSpec|fullMedium2.eta_actual|fullMedium2.eta_fixed|fullMedium2.eta_is|fullMedium2.h_in|fullMedium2.h_out|fullMedium2.initM_flow|der.fullMedium2.inlet.m_flow.|fullMedium2.inlet.m_flow|fullMedium2.inlet.r|fullMedium2.inlet.state.T|fullMedium2.inlet.state.d|fullMedium2.inlet.state.h|fullMedium2.inlet.state.p|fullMedium2.inlet.state.phase|fullMedium2.m_acceleration_0|fullMedium2.m_flow|fullMedium2.m_flowStateSelect|fullMedium2.m_flow_0|fullMedium2.outlet.m_flow|fullMedium2.outlet.r|fullMedium2.outlet.state.T|fullMedium2.outlet.state.d|fullMedium2.outlet.state.h|fullMedium2.outlet.state.p|fullMedium2.outlet.state.phase|fullMedium2.outletSpec|fullMedium2.outletSpec_actual|fullMedium2.outletValueSpec|fullMedium2.pRatio|fullMedium2.pRatio_fixed|fullMedium2.p_in|fullMedium2.p_min|fullMedium2.p_out|fullMedium2.p_out_fixed|fullMedium2.singularityRegime|fullMedium3.L|fullMedium3.P|fullMedium3.P_in|fullMedium3.P_nom|fullMedium3.TC|fullMedium3.adiabaticModel.eta_is|fullMedium3.adiabaticModel.h_in|fullMedium3.adiabaticModel.h_out|fullMedium3.adiabaticModel.h_out_is|fullMedium3.adiabaticModel.p_out|fullMedium3.adiabaticModel.s_in|fullMedium3.adiabaticModel.state_in.T|fullMedium3.adiabaticModel.state_in.d|fullMedium3.adiabaticModel.state_in.h|fullMedium3.adiabaticModel.state_in.p|fullMedium3.adiabaticModel.state_in.phase|fullMedium3.adiabaticModel.w_t|fullMedium3.adiabaticModel.w_t_is|fullMedium3.assertionLevel|fullMedium3.clip_p_out|fullMedium3.dh|fullMedium3.dp|fullMedium3.dp_fixed|fullMedium3.dp_nom|fullMedium3.dp_start|fullMedium3.dr_corr|fullMedium3.etaSpec|fullMedium3.eta_actual|fullMedium3.eta_fixed|fullMedium3.eta_is|fullMedium3.h_in|fullMedium3.h_out|fullMedium3.initM_flow|der.fullMedium3.inlet.m_flow.|fullMedium3.inlet.m_flow|fullMedium3.inlet.r|fullMedium3.inlet.state.T|fullMedium3.inlet.state.d|fullMedium3.inlet.state.h|fullMedium3.inlet.state.p|fullMedium3.inlet.state.phase|fullMedium3.m_acceleration_0|fullMedium3.m_flow|fullMedium3.m_flowStateSelect|fullMedium3.m_flow_0|fullMedium3.outlet.m_flow|fullMedium3.outlet.r|fullMedium3.outlet.state.T|fullMedium3.outlet.state.d|fullMedium3.outlet.state.h|fullMedium3.outlet.state.p|fullMedium3.outlet.state.phase|fullMedium3.outletSpec_actual|fullMedium3.pRatio|fullMedium3.pRatio_fixed|fullMedium3.p_in|fullMedium3.p_min|fullMedium3.p_out|fullMedium3.p_out_fixed|fullMedium3.singularityRegime|gain.k|gain.u|gain.y|gain1.k|gain1.u|gain1.y|gain2.k|gain2.u|gain2.y|incompressibleFluid.L|incompressibleFluid.P|incompressibleFluid.P_nom|incompressibleFluid.P_out|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.d|incompressibleFluid.adiabaticModel.state_in.h|incompressibleFluid.adiabaticModel.state_in.p|incompressibleFluid.adiabaticModel.state_in.phase|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.d|incompressibleFluid.inlet.state.h|incompressibleFluid.inlet.state.p|incompressibleFluid.inlet.state.phase|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.d|incompressibleFluid.outlet.state.h|incompressibleFluid.outlet.state.p|incompressibleFluid.outlet.state.phase|incompressibleFluid.outletSpec|incompressibleFluid.outletSpec_actual|incompressibleFluid.outletValueSpec|incompressibleFluid.pRatio|incompressibleFluid.pRatio_fixed|incompressibleFluid.p_in|incompressibleFluid.p_min|incompressibleFluid.p_out|incompressibleFluid.p_out_fixed|incompressibleFluid.singularityRegime|incompressibleFluid1.L|incompressibleFluid1.P|incompressibleFluid1.P_in|incompressibleFluid1.P_nom|incompressibleFluid1.TC|incompressibleFluid1.adiabaticModel.T_in|incompressibleFluid1.adiabaticModel.T_out_is|incompressibleFluid1.adiabaticModel.assertionLevel|incompressibleFluid1.adiabaticModel.deltaDensityRel|incompressibleFluid1.adiabaticModel.eta_is|incompressibleFluid1.adiabaticModel.h_in|incompressibleFluid1.adiabaticModel.h_out|in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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.d|source2.outlet.state.h|source2.outlet.state.p|source2.outlet.state.phase|source2.p0|source2.p0_par|source3.L|source3.T0|source3.T0_par|source3.h0|source3.h0_par|der.source3.outlet.m_flow.|source3.outlet.m_flow|source3.outlet.r|source3.outlet.state.T|source3.outlet.state.d|source3.outlet.state.h|source3.outlet.state.p|source3.outlet.state.phase|source3.p0|source3.p0_par|source4.L|source4.T0|source4.T0_par|source4.h0|source4.h0_par|der.source4.outlet.m_flow.|source4.outlet.m_flow|source4.outlet.r|source4.outlet.state.T|source4.outlet.state.d|source4.outlet.state.h|source4.outlet.state.p|source4.outlet.state.phase|source4.p0|source4.p0_par|source5.L|source5.T0|source5.T0_par|source5.h0|source5.h0_par|der.source5.outlet.m_flow.|source5.outlet.m_flow|source5.outlet.r|source5.outlet.state.T|source5.outlet.state.d|source5.outlet.state.h|source5.outlet.state.p|source5.outlet.state.phase|source5.p0|source5.p0_par|source6.L|source6.T0|source6.T0_par|source6.h0|source6.h0_par|der.source6.outlet.m_flow.|source6.outlet.m_flow|source6.outlet.r|source6.outlet.state.T|source6.outlet.state.d|source6.outlet.state.h|source6.outlet.state.p|source6.outlet.state.phase|source6.p0|source6.p0_par|source7.L|source7.T0|source7.T0_par|source7.h0|source7.h0_par|der.source7.outlet.m_flow.|source7.outlet.m_flow|source7.outlet.r|source7.outlet.state.T|source7.outlet.state.d|source7.outlet.state.h|source7.outlet.state.p|source7.outlet.state.phase|source7.p0|source7.p0_par|source8.L|source8.T0|source8.T0_par|source8.h0|source8.h0_par|der.source8.outlet.m_flow.|source8.outlet.m_flow|source8.outlet.r|source8.outlet.state.T|source8.outlet.state.d|source8.outlet.state.h|source8.outlet.state.p|source8.outlet.state.phase|source8.p0|source8.p0_par|source9.L|source9.T0|source9.T0_par|source9.h0|source9.h0_par|der.source9.outlet.m_flow.|source9.outlet.m_flow|source9.outlet.r|source9.outlet.state.T|source9.outlet.state.d|source9.outlet.state.h|source9.outlet.state.p|source9.outlet.state.phase|source9.p0|source9.p0_par",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Tests.Processes.Adiabatic.PumpConstant",simflags="-alarm=1200 -emit_protected -lv LOG_STATS") LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((isothermalReference3.p_min >= 611.657 and isothermalReference3.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= isothermalReference3.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((incompressibleFluid3.p_min >= 611.657 and incompressibleFluid3.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= incompressibleFluid3.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((fullMedium3.p_min >= 611.657 and fullMedium3.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= fullMedium3.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((isothermalReference2.p_min >= 611.657 and isothermalReference2.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= isothermalReference2.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((isothermalReference1.p_min >= 611.657 and isothermalReference1.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= isothermalReference1.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((isothermalReference.p_min >= 611.657 and isothermalReference.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= isothermalReference.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((incompressibleFluid2.p_min >= 611.657 and incompressibleFluid2.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= incompressibleFluid2.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((incompressibleFluid1.p_min >= 611.657 and incompressibleFluid1.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= incompressibleFluid1.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((fullMedium2.p_min >= 611.657 and fullMedium2.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= fullMedium2.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((fullMedium1.p_min >= 611.657 and fullMedium1.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= fullMedium1.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((incompressibleFluid.p_min >= 611.657 and incompressibleFluid.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= incompressibleFluid.p_min <= 1e8, has value: 100" LOG_ASSERT | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Interfaces/SISOFlow.mo:27:3-28:58:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((fullMedium.p_min >= 611.657 and fullMedium.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= fullMedium.p_min <= 1e8, has value: 100" LOG_SUCCESS | info | The initialization finished successfully without homotopy method. LOG_STATS | info | ### STATISTICS ### LOG_STATS | info | events LOG_STATS | info | | 0 state events LOG_STATS | info | | 0 time events LOG_STATS | info | solver: dassl-events LOG_STATS | info | | 134 steps taken LOG_STATS | info | | 163 calls of functionODE LOG_STATS | info | | 44 evaluations of jacobian LOG_STATS | info | | 2 error test failures LOG_STATS | info | | 0 convergence test failures LOG_STATS | info | | 0 linear system solves LOG_SUCCESS | info | The simulation finished successfully.