startTime=0 stopTime=100 tolerance=1e-06 numberOfIntervals=1000 stepSize=0.1 wasm-jit simulation: simulate(ThermofluidStream.Idealized.Examples.Volumes.Reservoir,startTime=0,stopTime=100,tolerance=1e-06,numberOfIntervals=1000,outputFormat="mat",variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|Time|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..HCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..SCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..acentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalMolarVolume|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..criticalTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..deltah|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..deltas|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..dipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAccurateConductivityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAccurateViscosityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasAcentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasCriticalData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasDipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasFundamentalEquation|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasIdealGasHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasLiquidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasSolidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..hasVapourPressureCurve|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..meltingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..molarMass|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..normalBoilingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..triplePointPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.WaterIF97_ph.fluidConstants.1..triplePointTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..HCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..SCRIT0|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..acentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalMolarVolume|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..criticalTemperature|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..deltah|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..deltas|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..dipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAccurateConductivityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAccurateViscosityData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasAcentricFactor|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasCriticalData|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasDipoleMoment|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasFundamentalEquation|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasIdealGasHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasLiquidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasSolidHeatCapacity|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..hasVapourPressureCurve|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..meltingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..molarMass|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..normalBoilingPoint|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..triplePointPressure|_GlobalScope.ThermofluidStream.Media.myMedia.Water.waterConstants.1..triplePointTemperature|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|isenthalpic.L|isenthalpic.assertionLevel|isenthalpic.clip_p_out|isenthalpic.dp|isenthalpic.dpLoss|isenthalpic.dpLoss_fixed|isenthalpic.dpLoss_set|isenthalpic.dr_corr|isenthalpic.h_in|isenthalpic.h_out|isenthalpic.initM_flow|der.isenthalpic.inlet.m_flow.|isenthalpic.inlet.m_flow|isenthalpic.inlet.r|isenthalpic.inlet.state.T|isenthalpic.inlet.state.d|isenthalpic.inlet.state.h|isenthalpic.inlet.state.p|isenthalpic.inlet.state.phase|isenthalpic.isDPLossAligned|isenthalpic.isDPLossSetAligned|isenthalpic.m_acceleration_0|isenthalpic.m_flow|isenthalpic.m_flowStateSelect|isenthalpic.m_flow_0|isenthalpic.outlet.m_flow|isenthalpic.outlet.r|isenthalpic.outlet.state.T|isenthalpic.outlet.state.d|isenthalpic.outlet.state.h|isenthalpic.outlet.state.p|isenthalpic.outlet.state.phase|isenthalpic.outletSpec|isenthalpic.outletSpec_actual|isenthalpic.outletSpec_prescribed|isenthalpic.outletValueSpec|isenthalpic.p_in|isenthalpic.p_min|isenthalpic.p_out|isenthalpic.p_out_fixed|isenthalpic.prLoss|isenthalpic.prLoss_fixed|massFlowRate.L|massFlowRate.clip_p_out|massFlowRate.dp|massFlowRate.dr_corr|massFlowRate.h_in|massFlowRate.h_out|massFlowRate.initM_flow|der.massFlowRate.inlet.m_flow.|massFlowRate.inlet.m_flow|massFlowRate.inlet.r|massFlowRate.inlet.state.T|massFlowRate.inlet.state.d|massFlowRate.inlet.state.h|massFlowRate.inlet.state.p|massFlowRate.inlet.state.phase|massFlowRate.m_acceleration_0|massFlowRate.m_flow|massFlowRate.m_flowSpec|massFlowRate.m_flowStateSelect|massFlowRate.m_flow_0|massFlowRate.m_flow_actual|massFlowRate.m_flow_fixed|massFlowRate.outlet.m_flow|massFlowRate.outlet.r|massFlowRate.outlet.state.T|massFlowRate.outlet.state.d|massFlowRate.outlet.state.h|massFlowRate.outlet.state.p|massFlowRate.outlet.state.phase|massFlowRate.p_in|massFlowRate.p_min|massFlowRate.p_out|reservoir.A|reservoir.A_surf|reservoir.L|reservoir.M|reservoir.Q_flow|reservoir.T_heatPort|reservoir.T_start|reservoir.U|reservoir.U_med|reservoir.V|reservoir.W_v|reservoir.d|reservoir.density_derp_h|der.reservoir.M.|der.reservoir.U_med.|der.reservoir.V.|der.reservoir.m_flow_in.|der.reservoir.m_flow_out.|reservoir.g|reservoir.h_in|reservoir.h_out|reservoir.h_start|reservoir.height|reservoir.height_0|reservoir.height_min|reservoir.inlet.m_flow|reservoir.inlet.r|reservoir.inlet.state.T|reservoir.inlet.state.d|reservoir.inlet.state.h|reservoir.inlet.state.p|reservoir.inlet.state.phase|reservoir.k_volume_damping|reservoir.m_flow_assert|reservoir.m_flow_in|reservoir.m_flow_out|reservoir.medium.MM|reservoir.medium.R_s|reservoir.medium.T|reservoir.medium.T_degC|reservoir.medium.X.1.|reservoir.medium.d|der.reservoir.medium.u.|reservoir.medium.h|reservoir.medium.p|reservoir.medium.p_bar|reservoir.medium.phase|reservoir.medium.preferredMediumStates|reservoir.medium.sat.Tsat|reservoir.medium.sat.psat|reservoir.medium.standardOrderComponents|reservoir.medium.state.T|reservoir.medium.state.d|reservoir.medium.state.h|reservoir.medium.state.p|reservoir.medium.state.phase|reservoir.medium.u|reservoir.p_env|reservoir.p_env_par|reservoir.p_in|reservoir.p_start|reservoir.r|reservoir.r_damping|reservoir.r_in|reservoir.r_out|reservoir.state_in.T|reservoir.state_in.d|reservoir.state_in.h|reservoir.state_in.p|reservoir.state_in.phase|reservoir.state_out.T|reservoir.state_out.d|der.reservoir.state_out.d.|der.reservoir.state_out.h.|der.reservoir.state_out.p.|reservoir.state_out.h|reservoir.state_out.p|reservoir.state_out.phase|reservoirPressure.y|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|source.p0|source.p0_par",fileNamePrefix="ThermofluidStream_ThermofluidStream.Idealized.Examples.Volumes.Reservoir",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 | | | | ((massFlowRate.p_min >= 611.657 and massFlowRate.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= massFlowRate.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 | | | | ((isenthalpic.p_min >= 611.657 and isenthalpic.p_min <= 1e8)) --> "Variable violating min/max constraint: 611.657 <= isenthalpic.p_min <= 1e8, has value: 100" LOG_SUCCESS | info | The initialization finished successfully without homotopy method. LOG_ASSERT | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/Idealized/Processes/Isenthalpic.mo:53:3-56:20:writable] | | | | The following assertion has been violated at time 92.000000 | | | | ((noEvent(massFlowRate.m_flow_fixed * isenthalpic.dpLoss >= -2.220446049250313e-16))) --> "In "Reservoir.isenthalpic" the pressure rises in the direction of the flow. | | | | An isenthalpic pressure increase however violates the second law of thermodynamics." 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 | | 25 steps taken LOG_STATS | info | | 25 calls of functionODE LOG_STATS | info | | 24 evaluations of jacobian LOG_STATS | info | | 0 error test failures LOG_STATS | info | | 0 convergence test failures LOG_STATS | info | | 0 linear system solves LOG_SUCCESS | info | The simulation finished successfully.