Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.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 0.001308/0.001308, allocations: 84.94 kB / 19.94 MB, free: 4.543 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 0.001452/0.001452, allocations: 173 kB / 23.36 MB, free: 1.133 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 0.9296/0.9296, allocations: 177.1 MB / 203.8 MB, free: 5.492 MB / 186.7 MB " [Timeout remaining time 179] 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 0.6494/0.6494, allocations: 118.6 MB / 378.9 MB, free: 1.336 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.HeatExchangers.Tests.ElementTwoPhase,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|conductionElementHEX_twoPhase.A|conductionElementHEX_twoPhase.L|conductionElementHEX_twoPhase.M|conductionElementHEX_twoPhase.Q_flow|conductionElementHEX_twoPhase.Re_exp_cond|conductionElementHEX_twoPhase.Re_exp_evap|conductionElementHEX_twoPhase.T|conductionElementHEX_twoPhase.T_0|conductionElementHEX_twoPhase.T_e|conductionElementHEX_twoPhase.T_heatPort|conductionElementHEX_twoPhase.U|conductionElementHEX_twoPhase.U_liq|conductionElementHEX_twoPhase.U_liq_nom|conductionElementHEX_twoPhase.U_min|conductionElementHEX_twoPhase.U_tp|conductionElementHEX_twoPhase.U_tp_nom|conductionElementHEX_twoPhase.U_vap|conductionElementHEX_twoPhase.U_vap_nom|conductionElementHEX_twoPhase.V|conductionElementHEX_twoPhase.clip_p_out|conductionElementHEX_twoPhase.deltaE_system|conductionElementHEX_twoPhase.delta_x|der.conductionElementHEX_twoPhase.h.|conductionElementHEX_twoPhase.dp|conductionElementHEX_twoPhase.dr_corr|conductionElementHEX_twoPhase.h|conductionElementHEX_twoPhase.h_0|conductionElementHEX_twoPhase.h_bubble|conductionElementHEX_twoPhase.h_dew|conductionElementHEX_twoPhase.h_in|conductionElementHEX_twoPhase.h_in_norm|conductionElementHEX_twoPhase.h_out|conductionElementHEX_twoPhase.heatPort.Q_flow|conductionElementHEX_twoPhase.heatPort.T|conductionElementHEX_twoPhase.init|conductionElementHEX_twoPhase.initM_flow|der.conductionElementHEX_twoPhase.inlet.m_flow.|conductionElementHEX_twoPhase.inlet.m_flow|conductionElementHEX_twoPhase.inlet.r|conductionElementHEX_twoPhase.inlet.state.T|conductionElementHEX_twoPhase.inlet.state.d|conductionElementHEX_twoPhase.inlet.state.h|conductionElementHEX_twoPhase.inlet.state.p|conductionElementHEX_twoPhase.inlet.state.phase|conductionElementHEX_twoPhase.k|conductionElementHEX_twoPhase.m_acceleration_0|conductionElementHEX_twoPhase.m_flow|conductionElementHEX_twoPhase.m_flowStateSelect|conductionElementHEX_twoPhase.m_flow_0|conductionElementHEX_twoPhase.m_flow_assert|conductionElementHEX_twoPhase.m_flow_nom|conductionElementHEX_twoPhase.nCellsParallel|conductionElementHEX_twoPhase.outlet.m_flow|conductionElementHEX_twoPhase.outlet.r|conductionElementHEX_twoPhase.outlet.state.T|conductionElementHEX_twoPhase.outlet.state.d|conductionElementHEX_twoPhase.outlet.state.h|conductionElementHEX_twoPhase.outlet.state.p|conductionElementHEX_twoPhase.outlet.state.phase|conductionElementHEX_twoPhase.p_in|conductionElementHEX_twoPhase.p_min|conductionElementHEX_twoPhase.p_out|conductionElementHEX_twoPhase.rho|conductionElementHEX_twoPhase.rho_min|conductionElementHEX_twoPhase.state.T|conductionElementHEX_twoPhase.state.d|conductionElementHEX_twoPhase.state.h|conductionElementHEX_twoPhase.state.p|conductionElementHEX_twoPhase.state.phase|conductionElementHEX_twoPhase.x|conductionElementHEX_twoPhase1.A|conductionElementHEX_twoPhase1.L|conductionElementHEX_twoPhase1.M|conductionElementHEX_twoPhase1.Q_flow|conductionElementHEX_twoPhase1.Re_exp_cond|conductionElementHEX_twoPhase1.Re_exp_evap|conductionElementHEX_twoPhase1.T|conductionElementHEX_twoPhase1.T_0|conductionElementHEX_twoPhase1.T_e|conductionElementHEX_twoPhase1.T_heatPort|conductionElementHEX_twoPhase1.U|conductionElementHEX_twoPhase1.U_liq|conductionElementHEX_twoPhase1.U_liq_nom|conductionElementHEX_twoPhase1.U_min|conductionElementHEX_twoPhase1.U_tp|conductionElementHEX_twoPhase1.U_tp_nom|conductionElementHEX_twoPhase1.U_vap|conductionElementHEX_twoPhase1.U_vap_nom|conductionElementHEX_twoPhase1.V|conductionElementHEX_twoPhase1.clip_p_out|conductionElementHEX_twoPhase1.deltaE_system|conductionElementHEX_twoPhase1.delta_x|der.conductionElementHEX_twoPhase1.h.|conductionElementHEX_twoPhase1.dp|conductionElementHEX_twoPhase1.dr_corr|conductionElementHEX_twoPhase1.h|conductionElementHEX_twoPhase1.h_0|conductionElementHEX_twoPhase1.h_bubble|conductionElementHEX_twoPhase1.h_dew|conductionElementHEX_twoPhase1.h_in|conductionElementHEX_twoPhase1.h_in_norm|conductionElementHEX_twoPhase1.h_out|conductionElementHEX_twoPhase1.heatPort.Q_flow|conductionElementHEX_twoPhase1.heatPort.T|conductionElementHEX_twoPhase1.init|conductionElementHEX_twoPhase1.initM_flow|der.conductionElementHEX_twoPhase1.inlet.m_flow.|conductionElementHEX_twoPhase1.inlet.m_flow|conductionElementHEX_twoPhase1.inlet.r|conductionElementHEX_twoPhase1.inlet.state.T|conductionElementHEX_twoPhase1.inlet.state.d|conductionElementHEX_twoPhase1.inlet.state.h|conductionElementHEX_twoPhase1.inlet.state.p|conductionElementHEX_twoPhase1.inlet.state.phase|conductionElementHEX_twoPhase1.k|conductionElementHEX_twoPhase1.m_acceleration_0|conductionElementHEX_twoPhase1.m_flow|conductionElementHEX_twoPhase1.m_flowStateSelect|conductionElementHEX_twoPhase1.m_flow_0|conductionElementHEX_twoPhase1.m_flow_assert|conductionElementHEX_twoPhase1.m_flow_nom|conductionElementHEX_twoPhase1.nCellsParallel|conductionElementHEX_twoPhase1.outlet.m_flow|conductionElementHEX_twoPhase1.outlet.r|conductionElementHEX_twoPhase1.outlet.state.T|conductionElementHEX_twoPhase1.outlet.state.d|conductionElementHEX_twoPhase1.outlet.state.h|conductionElementHEX_twoPhase1.outlet.state.p|conductionElementHEX_twoPhase1.outlet.state.phase|conductionElementHEX_twoPhase1.p_in|conductionElementHEX_twoPhase1.p_min|conductionElementHEX_twoPhase1.p_out|conductionElementHEX_twoPhase1.rho|conductionElementHEX_twoPhase1.rho_min|conductionElementHEX_twoPhase1.state.T|conductionElementHEX_twoPhase1.state.d|conductionElementHEX_twoPhase1.state.h|conductionElementHEX_twoPhase1.state.p|conductionElementHEX_twoPhase1.state.phase|conductionElementHEX_twoPhase1.x|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dp_ref_color|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.d|flowResistance.inlet.state.h|flowResistance.inlet.state.p|flowResistance.inlet.state.phase|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.d|flowResistance.outlet.state.h|flowResistance.outlet.state.p|flowResistance.outlet.state.phase|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.phi|flowResistance.pressureDropSignificantDigits|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|flowResistance1.D_h|flowResistance1.L|flowResistance1.L_value|flowResistance1.a|flowResistance1.areaCross|flowResistance1.areaCrossInput|flowResistance1.areaHydraulic|flowResistance1.b|flowResistance1.clip_p_out|flowResistance1.dp|flowResistance1.dp_ref_color|flowResistance1.dr_corr|flowResistance1.h_in|flowResistance1.h_out|flowResistance1.initM_flow|der.flowResistance1.inlet.m_flow.|flowResistance1.inlet.m_flow|flowResistance1.inlet.r|flowResistance1.inlet.state.T|flowResistance1.inlet.state.d|flowResistance1.inlet.state.h|flowResistance1.inlet.state.p|flowResistance1.inlet.state.phase|flowResistance1.l|flowResistance1.m_acceleration_0|flowResistance1.m_flow|flowResistance1.m_flowStateSelect|flowResistance1.m_flow_0|flowResistance1.mu_in|flowResistance1.outlet.m_flow|flowResistance1.outlet.r|flowResistance1.outlet.state.T|flowResistance1.outlet.state.d|flowResistance1.outlet.state.h|flowResistance1.outlet.state.p|flowResistance1.outlet.state.phase|flowResistance1.p_in|flowResistance1.p_min|flowResistance1.p_out|flowResistance1.perimeter|flowResistance1.perimeterInput|flowResistance1.phi|flowResistance1.pressureDropSignificantDigits|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dp_ref_color|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.d|flowResistance2.inlet.state.h|flowResistance2.inlet.state.p|flowResistance2.inlet.state.phase|flowResistance2.l|flowResistance2.m_acceleration_0|flowResistance2.m_flow|flowResistance2.m_flowStateSelect|flowResistance2.m_flow_0|flowResistance2.mu_in|flowResistance2.outlet.m_flow|flowResistance2.outlet.r|flowResistance2.outlet.state.T|flowResistance2.outlet.state.d|flowResistance2.outlet.state.h|flowResistance2.outlet.state.p|flowResistance2.outlet.state.phase|flowResistance2.p_in|flowResistance2.p_min|flowResistance2.p_out|flowResistance2.perimeter|flowResistance2.perimeterInput|flowResistance2.phi|flowResistance2.pressureDropSignificantDigits|flowResistance2.r|flowResistance2.rho_in|flowResistance2.rho_min|flowResistance2.shape|flowResistance3.D_h|flowResistance3.L|flowResistance3.L_value|flowResistance3.a|flowResistance3.areaCross|flowResistance3.areaCrossInput|flowResistance3.areaHydraulic|flowResistance3.b|flowResistance3.clip_p_out|flowResistance3.dp|flowResistance3.dp_ref_color|flowResistance3.dr_corr|flowResistance3.h_in|flowResistance3.h_out|flowResistance3.initM_flow|der.flowResistance3.inlet.m_flow.|flowResistance3.inlet.m_flow|flowResistance3.inlet.r|flowResistance3.inlet.state.T|flowResistance3.inlet.state.d|flowResistance3.inlet.state.h|flowResistance3.inlet.state.p|flowResistance3.inlet.state.phase|flowResistance3.l|flowResistance3.m_acceleration_0|flowResistance3.m_flow|flowResistance3.m_flowStateSelect|flowResistance3.m_flow_0|flowResistance3.mu_in|flowResistance3.outlet.m_flow|flowResistance3.outlet.r|flowResistance3.outlet.state.T|flowResistance3.outlet.state.d|flowResistance3.outlet.state.h|flowResistance3.outlet.state.p|flowResistance3.outlet.state.phase|flowResistance3.p_in|flowResistance3.p_min|flowResistance3.p_out|flowResistance3.perimeter|flowResistance3.perimeterInput|flowResistance3.phi|flowResistance3.pressureDropSignificantDigits|flowResistance3.r|flowResistance3.rho_in|flowResistance3.rho_min|flowResistance3.shape|mCV.L|mCV.TC|mCV.V_flow|mCV.V_flow_set|mCV.clip_p_out|der.mCV.dp_int.|mCV.dp|mCV.dp_corr|mCV.dp_int|mCV.dr|mCV.dr_corr|mCV.dr_set|mCV.enableClippingOutput|mCV.eps|mCV.h_in|mCV.h_out|mCV.initM_flow|der.mCV.inlet.m_flow.|mCV.inlet.m_flow|mCV.inlet.r|mCV.inlet.state.T|mCV.inlet.state.d|mCV.inlet.state.h|mCV.inlet.state.p|mCV.inlet.state.phase|mCV.k1|mCV.k2|mCV.m_acceleration_0|mCV.m_flow|mCV.m_flowStateSelect|mCV.m_flow_0|mCV.m_flow_set|mCV.massFlow_set_par|mCV.mode|mCV.outlet.m_flow|mCV.outlet.r|mCV.outlet.state.T|mCV.outlet.state.d|mCV.outlet.state.h|mCV.outlet.state.p|mCV.outlet.state.phase|mCV.p_in|mCV.p_min|mCV.p_min_par|mCV.p_out|mCV.rho_in|mCV.setpoint|mCV.volumeFlow_set_par|mCV1.L|mCV1.TC|mCV1.V_flow|mCV1.V_flow_set|mCV1.clip_p_out|der.mCV1.dp_int.|mCV1.dp|mCV1.dp_corr|mCV1.dp_int|mCV1.dr|mCV1.dr_corr|mCV1.dr_set|mCV1.enableClippingOutput|mCV1.eps|mCV1.h_in|mCV1.h_out|mCV1.initM_flow|der.mCV1.inlet.m_flow.|mCV1.inlet.m_flow|mCV1.inlet.r|mCV1.inlet.state.T|mCV1.inlet.state.d|mCV1.inlet.state.h|mCV1.inlet.state.p|mCV1.inlet.state.phase|mCV1.k1|mCV1.k2|mCV1.m_acceleration_0|mCV1.m_flow|mCV1.m_flowStateSelect|mCV1.m_flow_0|mCV1.m_flow_set|mCV1.massFlow_set_par|mCV1.mode|mCV1.outlet.m_flow|mCV1.outlet.r|mCV1.outlet.state.T|mCV1.outlet.state.d|mCV1.outlet.state.h|mCV1.outlet.state.p|mCV1.outlet.state.phase|mCV1.p_in|mCV1.p_min|mCV1.p_min_par|mCV1.p_out|mCV1.rho_in|mCV1.setpoint|mCV1.volumeFlow_set_par|mCV2.L|mCV2.TC|mCV2.V_flow|mCV2.V_flow_set|mCV2.clip_p_out|der.mCV2.dp_int.|mCV2.dp|mCV2.dp_corr|mCV2.dp_int|mCV2.dr|mCV2.dr_corr|mCV2.dr_set|mCV2.enableClippingOutput|mCV2.eps|mCV2.h_in|mCV2.h_out|mCV2.initM_flow|der.mCV2.inlet.m_flow.|mCV2.inlet.m_flow|mCV2.inlet.r|mCV2.inlet.state.T|mCV2.inlet.state.d|mCV2.inlet.state.h|mCV2.inlet.state.p|mCV2.inlet.state.phase|mCV2.k1|mCV2.k2|mCV2.m_acceleration_0|mCV2.m_flow|mCV2.m_flowStateSelect|mCV2.m_flow_0|mCV2.m_flow_set|mCV2.massFlow_set_par|mCV2.mode|mCV2.outlet.m_flow|mCV2.outlet.r|mCV2.outlet.state.T|mCV2.outlet.state.d|mCV2.outlet.state.h|mCV2.outlet.state.p|mCV2.outlet.state.phase|mCV2.p_in|mCV2.p_min|mCV2.p_min_par|mCV2.p_out|mCV2.rho_in|mCV2.setpoint|mCV2.volumeFlow_set_par|mCV3.L|mCV3.TC|mCV3.V_flow|mCV3.V_flow_set|mCV3.clip_p_out|der.mCV3.dp_int.|mCV3.dp|mCV3.dp_corr|mCV3.dp_int|mCV3.dr|mCV3.dr_corr|mCV3.dr_set|mCV3.enableClippingOutput|mCV3.eps|mCV3.h_in|mCV3.h_out|mCV3.initM_flow|der.mCV3.inlet.m_flow.|mCV3.inlet.m_flow|mCV3.inlet.r|mCV3.inlet.state.T|mCV3.inlet.state.d|mCV3.inlet.state.h|mCV3.inlet.state.p|mCV3.inlet.state.phase|mCV3.k1|mCV3.k2|mCV3.m_acceleration_0|mCV3.m_flow|mCV3.m_flowStateSelect|mCV3.m_flow_0|mCV3.m_flow_set|mCV3.massFlow_set_par|mCV3.mode|mCV3.outlet.m_flow|mCV3.outlet.r|mCV3.outlet.state.T|mCV3.outlet.state.d|mCV3.outlet.state.h|mCV3.outlet.state.p|mCV3.outlet.state.phase|mCV3.p_in|mCV3.p_min|mCV3.p_min_par|mCV3.p_out|mCV3.rho_in|mCV3.setpoint|mCV3.volumeFlow_set_par|prescribedTemperature.T|prescribedTemperature.port.Q_flow|prescribedTemperature.port.T|prescribedTemperature1.T|prescribedTemperature1.port.Q_flow|prescribedTemperature1.port.T|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.d|sink.inlet.state.h|sink.inlet.state.p|sink.inlet.state.phase|sink.p|sink.p0|sink.p0_par|sink.r|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.d|sink1.inlet.state.h|sink1.inlet.state.p|sink1.inlet.state.phase|sink1.p|sink1.p0|sink1.p0_par|sink1.r|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.d|sink2.inlet.state.h|sink2.inlet.state.p|sink2.inlet.state.phase|sink2.p|sink2.p0|sink2.p0_par|sink2.r|sink3.L|der.sink3.inlet.m_flow.|sink3.inlet.m_flow|sink3.inlet.r|sink3.inlet.state.T|sink3.inlet.state.d|sink3.inlet.state.h|sink3.inlet.state.p|sink3.inlet.state.phase|sink3.p|sink3.p0|sink3.p0_par|sink3.r|source.L|source.T0|source.T0_par|source.h0|source.h0_par|source.h0_var|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|source1.L|source1.T0|source1.T0_par|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.d|source1.outlet.state.h|source1.outlet.state.p|source1.outlet.state.phase|source1.p0|source1.p0_par|source2.L|source2.T0|source2.T0_par|source2.h0|source2.h0_par|source2.h0_var|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|trapezoid.T_falling|trapezoid.T_rising|trapezoid.T_start|trapezoid.T_width|trapezoid.amplitude|trapezoid.count|trapezoid.falling|trapezoid.nperiod|trapezoid.offset|trapezoid.period|trapezoid.rising|trapezoid.startTime|trapezoid.width|trapezoid.y|trapezoid2.T_falling|trapezoid2.T_rising|trapezoid2.T_start|trapezoid2.T_width|trapezoid2.amplitude|trapezoid2.count|trapezoid2.falling|trapezoid2.nperiod|trapezoid2.offset|trapezoid2.period|trapezoid2.rising|trapezoid2.startTime|trapezoid2.width|trapezoid2.y|volume.A|volume.L|volume.M|volume.Q_flow|volume.T_heatPort|volume.T_start|volume.U|volume.U_med|volume.V|volume.V_par|volume.W_v|volume.d|volume.density_derp_h|volume.density_derp_h_set|der.volume.M.|der.volume.U_med.|der.volume.m_flow_in.|der.volume.m_flow_out.|volume.h_in|volume.h_out|volume.h_start|volume.inlet.m_flow|volume.inlet.r|volume.inlet.state.T|volume.inlet.state.d|volume.inlet.state.h|volume.inlet.state.p|volume.inlet.state.phase|volume.k_volume_damping|volume.m_flow_assert|volume.m_flow_in|volume.m_flow_out|volume.medium.MM|volume.medium.R_s|volume.medium.T|volume.medium.T_degC|volume.medium.X.[0-9,]+.|volume.medium.d|der.volume.medium.h.|der.volume.medium.p.|der.volume.medium.u.|volume.medium.h|volume.medium.p|volume.medium.p_bar|volume.medium.phase|volume.medium.preferredMediumStates|volume.medium.quality|volume.medium.sat.Tsat|volume.medium.sat.psat|volume.medium.standardOrderComponents|volume.medium.state.T|volume.medium.state.d|der.volume.medium.state.d.|volume.medium.state.h|volume.medium.state.p|volume.medium.state.phase|volume.medium.u|volume.outlet.m_flow|volume.outlet.r|volume.outlet.state.T|volume.outlet.state.d|volume.outlet.state.h|volume.outlet.state.p|volume.outlet.state.phase|volume.p_in|volume.p_start|volume.r|volume.r_damping|volume.r_in|volume.r_out|volume.state_in.T|volume.state_in.d|volume.state_in.h|volume.state_in.p|volume.state_in.phase|volume.state_out.T|volume.state_out.d|volume.state_out.h|volume.state_out.p|volume.state_out.phase|volume1.A|volume1.L|volume1.M|volume1.Q_flow|volume1.T_heatPort|volume1.T_start|volume1.U|volume1.U_med|volume1.V|volume1.V_par|volume1.W_v|volume1.d|volume1.density_derp_h|volume1.density_derp_h_set|der.volume1.M.|der.volume1.U_med.|der.volume1.m_flow_in.|der.volume1.m_flow_out.|volume1.h_in|volume1.h_out|volume1.h_start|volume1.heatPort.Q_flow|volume1.heatPort.T|volume1.inlet.m_flow|volume1.inlet.r|volume1.inlet.state.T|volume1.inlet.state.d|volume1.inlet.state.h|volume1.inlet.state.p|volume1.inlet.state.phase|volume1.k_volume_damping|volume1.m_flow_assert|volume1.m_flow_in|volume1.m_flow_out|volume1.medium.MM|volume1.medium.R_s|volume1.medium.T|volume1.medium.T_degC|volume1.medium.X.[0-9,]+.|volume1.medium.d|der.volume1.medium.h.|der.volume1.medium.p.|der.volume1.medium.u.|volume1.medium.h|volume1.medium.p|volume1.medium.p_bar|volume1.medium.phase|volume1.medium.preferredMediumStates|volume1.medium.quality|volume1.medium.sat.Tsat|volume1.medium.sat.psat|volume1.medium.standardOrderComponents|volume1.medium.state.T|volume1.medium.state.d|der.volume1.medium.state.d.|volume1.medium.state.h|volume1.medium.state.p|volume1.medium.state.phase|volume1.medium.u|volume1.outlet.m_flow|volume1.outlet.r|volume1.outlet.state.T|volume1.outlet.state.d|volume1.outlet.state.h|volume1.outlet.state.p|volume1.outlet.state.phase|volume1.p_in|volume1.p_start|volume1.r|volume1.r_damping|volume1.r_in|volume1.r_out|volume1.state_in.T|volume1.state_in.d|volume1.state_in.h|volume1.state_in.p|volume1.state_in.phase|volume1.state_out.T|volume1.state_out.d|volume1.state_out.h|volume1.state_out.p|volume1.state_out.phase",fileNamePrefix="ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase") translateModel(ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase,tolerance=1e-06,outputFormat="mat",numberOfIntervals=1000,variableFilter="CPUtime|EventCounter|NonlinearSystems.simulation.[0-9,]+..Calls|NonlinearSystems.simulation.[0-9,]+..Iterations|NonlinearSystems.simulation.[0-9,]+..Jacobians|NonlinearSystems.simulation.[0-9,]+..Residues|Time|conductionElementHEX_twoPhase.A|conductionElementHEX_twoPhase.L|conductionElementHEX_twoPhase.M|conductionElementHEX_twoPhase.Q_flow|conductionElementHEX_twoPhase.Re_exp_cond|conductionElementHEX_twoPhase.Re_exp_evap|conductionElementHEX_twoPhase.T|conductionElementHEX_twoPhase.T_0|conductionElementHEX_twoPhase.T_e|conductionElementHEX_twoPhase.T_heatPort|conductionElementHEX_twoPhase.U|conductionElementHEX_twoPhase.U_liq|conductionElementHEX_twoPhase.U_liq_nom|conductionElementHEX_twoPhase.U_min|conductionElementHEX_twoPhase.U_tp|conductionElementHEX_twoPhase.U_tp_nom|conductionElementHEX_twoPhase.U_vap|conductionElementHEX_twoPhase.U_vap_nom|conductionElementHEX_twoPhase.V|conductionElementHEX_twoPhase.clip_p_out|conductionElementHEX_twoPhase.deltaE_system|conductionElementHEX_twoPhase.delta_x|der.conductionElementHEX_twoPhase.h.|conductionElementHEX_twoPhase.dp|conductionElementHEX_twoPhase.dr_corr|conductionElementHEX_twoPhase.h|conductionElementHEX_twoPhase.h_0|conductionElementHEX_twoPhase.h_bubble|conductionElementHEX_twoPhase.h_dew|conductionElementHEX_twoPhase.h_in|conductionElementHEX_twoPhase.h_in_norm|conductionElementHEX_twoPhase.h_out|conductionElementHEX_twoPhase.heatPort.Q_flow|conductionElementHEX_twoPhase.heatPort.T|conductionElementHEX_twoPhase.init|conductionElementHEX_twoPhase.initM_flow|der.conductionElementHEX_twoPhase.inlet.m_flow.|conductionElementHEX_twoPhase.inlet.m_flow|conductionElementHEX_twoPhase.inlet.r|conductionElementHEX_twoPhase.inlet.state.T|conductionElementHEX_twoPhase.inlet.state.d|conductionElementHEX_twoPhase.inlet.state.h|conductionElementHEX_twoPhase.inlet.state.p|conductionElementHEX_twoPhase.inlet.state.phase|conductionElementHEX_twoPhase.k|conductionElementHEX_twoPhase.m_acceleration_0|conductionElementHEX_twoPhase.m_flow|conductionElementHEX_twoPhase.m_flowStateSelect|conductionElementHEX_twoPhase.m_flow_0|conductionElementHEX_twoPhase.m_flow_assert|conductionElementHEX_twoPhase.m_flow_nom|conductionElementHEX_twoPhase.nCellsParallel|conductionElementHEX_twoPhase.outlet.m_flow|conductionElementHEX_twoPhase.outlet.r|conductionElementHEX_twoPhase.outlet.state.T|conductionElementHEX_twoPhase.outlet.state.d|conductionElementHEX_twoPhase.outlet.state.h|conductionElementHEX_twoPhase.outlet.state.p|conductionElementHEX_twoPhase.outlet.state.phase|conductionElementHEX_twoPhase.p_in|conductionElementHEX_twoPhase.p_min|conductionElementHEX_twoPhase.p_out|conductionElementHEX_twoPhase.rho|conductionElementHEX_twoPhase.rho_min|conductionElementHEX_twoPhase.state.T|conductionElementHEX_twoPhase.state.d|conductionElementHEX_twoPhase.state.h|conductionElementHEX_twoPhase.state.p|conductionElementHEX_twoPhase.state.phase|conductionElementHEX_twoPhase.x|conductionElementHEX_twoPhase1.A|conductionElementHEX_twoPhase1.L|conductionElementHEX_twoPhase1.M|conductionElementHEX_twoPhase1.Q_flow|conductionElementHEX_twoPhase1.Re_exp_cond|conductionElementHEX_twoPhase1.Re_exp_evap|conductionElementHEX_twoPhase1.T|conductionElementHEX_twoPhase1.T_0|conductionElementHEX_twoPhase1.T_e|conductionElementHEX_twoPhase1.T_heatPort|conductionElementHEX_twoPhase1.U|conductionElementHEX_twoPhase1.U_liq|conductionElementHEX_twoPhase1.U_liq_nom|conductionElementHEX_twoPhase1.U_min|conductionElementHEX_twoPhase1.U_tp|conductionElementHEX_twoPhase1.U_tp_nom|conductionElementHEX_twoPhase1.U_vap|conductionElementHEX_twoPhase1.U_vap_nom|conductionElementHEX_twoPhase1.V|conductionElementHEX_twoPhase1.clip_p_out|conductionElementHEX_twoPhase1.deltaE_system|conductionElementHEX_twoPhase1.delta_x|der.conductionElementHEX_twoPhase1.h.|conductionElementHEX_twoPhase1.dp|conductionElementHEX_twoPhase1.dr_corr|conductionElementHEX_twoPhase1.h|conductionElementHEX_twoPhase1.h_0|conductionElementHEX_twoPhase1.h_bubble|conductionElementHEX_twoPhase1.h_dew|conductionElementHEX_twoPhase1.h_in|conductionElementHEX_twoPhase1.h_in_norm|conductionElementHEX_twoPhase1.h_out|conductionElementHEX_twoPhase1.heatPort.Q_flow|conductionElementHEX_twoPhase1.heatPort.T|conductionElementHEX_twoPhase1.init|conductionElementHEX_twoPhase1.initM_flow|der.conductionElementHEX_twoPhase1.inlet.m_flow.|conductionElementHEX_twoPhase1.inlet.m_flow|conductionElementHEX_twoPhase1.inlet.r|conductionElementHEX_twoPhase1.inlet.state.T|conductionElementHEX_twoPhase1.inlet.state.d|conductionElementHEX_twoPhase1.inlet.state.h|conductionElementHEX_twoPhase1.inlet.state.p|conductionElementHEX_twoPhase1.inlet.state.phase|conductionElementHEX_twoPhase1.k|conductionElementHEX_twoPhase1.m_acceleration_0|conductionElementHEX_twoPhase1.m_flow|conductionElementHEX_twoPhase1.m_flowStateSelect|conductionElementHEX_twoPhase1.m_flow_0|conductionElementHEX_twoPhase1.m_flow_assert|conductionElementHEX_twoPhase1.m_flow_nom|conductionElementHEX_twoPhase1.nCellsParallel|conductionElementHEX_twoPhase1.outlet.m_flow|conductionElementHEX_twoPhase1.outlet.r|conductionElementHEX_twoPhase1.outlet.state.T|conductionElementHEX_twoPhase1.outlet.state.d|conductionElementHEX_twoPhase1.outlet.state.h|conductionElementHEX_twoPhase1.outlet.state.p|conductionElementHEX_twoPhase1.outlet.state.phase|conductionElementHEX_twoPhase1.p_in|conductionElementHEX_twoPhase1.p_min|conductionElementHEX_twoPhase1.p_out|conductionElementHEX_twoPhase1.rho|conductionElementHEX_twoPhase1.rho_min|conductionElementHEX_twoPhase1.state.T|conductionElementHEX_twoPhase1.state.d|conductionElementHEX_twoPhase1.state.h|conductionElementHEX_twoPhase1.state.p|conductionElementHEX_twoPhase1.state.phase|conductionElementHEX_twoPhase1.x|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dp_ref_color|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.d|flowResistance.inlet.state.h|flowResistance.inlet.state.p|flowResistance.inlet.state.phase|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.d|flowResistance.outlet.state.h|flowResistance.outlet.state.p|flowResistance.outlet.state.phase|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.phi|flowResistance.pressureDropSignificantDigits|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|flowResistance1.D_h|flowResistance1.L|flowResistance1.L_value|flowResistance1.a|flowResistance1.areaCross|flowResistance1.areaCrossInput|flowResistance1.areaHydraulic|flowResistance1.b|flowResistance1.clip_p_out|flowResistance1.dp|flowResistance1.dp_ref_color|flowResistance1.dr_corr|flowResistance1.h_in|flowResistance1.h_out|flowResistance1.initM_flow|der.flowResistance1.inlet.m_flow.|flowResistance1.inlet.m_flow|flowResistance1.inlet.r|flowResistance1.inlet.state.T|flowResistance1.inlet.state.d|flowResistance1.inlet.state.h|flowResistance1.inlet.state.p|flowResistance1.inlet.state.phase|flowResistance1.l|flowResistance1.m_acceleration_0|flowResistance1.m_flow|flowResistance1.m_flowStateSelect|flowResistance1.m_flow_0|flowResistance1.mu_in|flowResistance1.outlet.m_flow|flowResistance1.outlet.r|flowResistance1.outlet.state.T|flowResistance1.outlet.state.d|flowResistance1.outlet.state.h|flowResistance1.outlet.state.p|flowResistance1.outlet.state.phase|flowResistance1.p_in|flowResistance1.p_min|flowResistance1.p_out|flowResistance1.perimeter|flowResistance1.perimeterInput|flowResistance1.phi|flowResistance1.pressureDropSignificantDigits|flowResistance1.r|flowResistance1.rho_in|flowResistance1.rho_min|flowResistance1.shape|flowResistance2.D_h|flowResistance2.L|flowResistance2.L_value|flowResistance2.a|flowResistance2.areaCross|flowResistance2.areaCrossInput|flowResistance2.areaHydraulic|flowResistance2.b|flowResistance2.clip_p_out|flowResistance2.dp|flowResistance2.dp_ref_color|flowResistance2.dr_corr|flowResistance2.h_in|flowResistance2.h_out|flowResistance2.initM_flow|der.flowResistance2.inlet.m_flow.|flowResistance2.inlet.m_flow|flowResistance2.inlet.r|flowResistance2.inlet.state.T|flowResistance2.inlet.state.d|flowResistance2.inlet.state.h|flowResistance2.inlet.state.p|flowResistance2.inlet.state.phase|flowResistance2.l|flowResistance2.m_acceleration_0|flowResistance2.m_flow|flowResistance2.m_flowStateSelect|flowResistance2.m_flow_0|flowResistance2.mu_in|flowResistance2.outlet.m_flow|flowResistance2.outlet.r|flowResistance2.outlet.state.T|flowResistance2.outlet.state.d|flowResistance2.outlet.state.h|flowResistance2.outlet.state.p|flowResistance2.outlet.state.phase|flowResistance2.p_in|flowResistance2.p_min|flowResistance2.p_out|flowResistance2.perimeter|flowResistance2.perimeterInput|flowResistance2.phi|flowResistance2.pressureDropSignificantDigits|flowResistance2.r|flowResistance2.rho_in|flowResistance2.rho_min|flowResistance2.shape|flowResistance3.D_h|flowResistance3.L|flowResistance3.L_value|flowResistance3.a|flowResistance3.areaCross|flowResistance3.areaCrossInput|flowResistance3.areaHydraulic|flowResistance3.b|flowResistance3.clip_p_out|flowResistance3.dp|flowResistance3.dp_ref_color|flowResistance3.dr_corr|flowResistance3.h_in|flowResistance3.h_out|flowResistance3.initM_flow|der.flowResistance3.inlet.m_flow.|flowResistance3.inlet.m_flow|flowResistance3.inlet.r|flowResistance3.inlet.state.T|flowResistance3.inlet.state.d|flowResistance3.inlet.state.h|flowResistance3.inlet.state.p|flowResistance3.inlet.state.phase|flowResistance3.l|flowResistance3.m_acceleration_0|flowResistance3.m_flow|flowResistance3.m_flowStateSelect|flowResistance3.m_flow_0|flowResistance3.mu_in|flowResistance3.outlet.m_flow|flowResistance3.outlet.r|flowResistance3.outlet.state.T|flowResistance3.outlet.state.d|flowResistance3.outlet.state.h|flowResistance3.outlet.state.p|flowResistance3.outlet.state.phase|flowResistance3.p_in|flowResistance3.p_min|flowResistance3.p_out|flowResistance3.perimeter|flowResistance3.perimeterInput|flowResistance3.phi|flowResistance3.pressureDropSignificantDigits|flowResistance3.r|flowResistance3.rho_in|flowResistance3.rho_min|flowResistance3.shape|mCV.L|mCV.TC|mCV.V_flow|mCV.V_flow_set|mCV.clip_p_out|der.mCV.dp_int.|mCV.dp|mCV.dp_corr|mCV.dp_int|mCV.dr|mCV.dr_corr|mCV.dr_set|mCV.enableClippingOutput|mCV.eps|mCV.h_in|mCV.h_out|mCV.initM_flow|der.mCV.inlet.m_flow.|mCV.inlet.m_flow|mCV.inlet.r|mCV.inlet.state.T|mCV.inlet.state.d|mCV.inlet.state.h|mCV.inlet.state.p|mCV.inlet.state.phase|mCV.k1|mCV.k2|mCV.m_acceleration_0|mCV.m_flow|mCV.m_flowStateSelect|mCV.m_flow_0|mCV.m_flow_set|mCV.massFlow_set_par|mCV.mode|mCV.outlet.m_flow|mCV.outlet.r|mCV.outlet.state.T|mCV.outlet.state.d|mCV.outlet.state.h|mCV.outlet.state.p|mCV.outlet.state.phase|mCV.p_in|mCV.p_min|mCV.p_min_par|mCV.p_out|mCV.rho_in|mCV.setpoint|mCV.volumeFlow_set_par|mCV1.L|mCV1.TC|mCV1.V_flow|mCV1.V_flow_set|mCV1.clip_p_out|der.mCV1.dp_int.|mCV1.dp|mCV1.dp_corr|mCV1.dp_int|mCV1.dr|mCV1.dr_corr|mCV1.dr_set|mCV1.enableClippingOutput|mCV1.eps|mCV1.h_in|mCV1.h_out|mCV1.initM_flow|der.mCV1.inlet.m_flow.|mCV1.inlet.m_flow|mCV1.inlet.r|mCV1.inlet.state.T|mCV1.inlet.state.d|mCV1.inlet.state.h|mCV1.inlet.state.p|mCV1.inlet.state.phase|mCV1.k1|mCV1.k2|mCV1.m_acceleration_0|mCV1.m_flow|mCV1.m_flowStateSelect|mCV1.m_flow_0|mCV1.m_flow_set|mCV1.massFlow_set_par|mCV1.mode|mCV1.outlet.m_flow|mCV1.outlet.r|mCV1.outlet.state.T|mCV1.outlet.state.d|mCV1.outlet.state.h|mCV1.outlet.state.p|mCV1.outlet.state.phase|mCV1.p_in|mCV1.p_min|mCV1.p_min_par|mCV1.p_out|mCV1.rho_in|mCV1.setpoint|mCV1.volumeFlow_set_par|mCV2.L|mCV2.TC|mCV2.V_flow|mCV2.V_flow_set|mCV2.clip_p_out|der.mCV2.dp_int.|mCV2.dp|mCV2.dp_corr|mCV2.dp_int|mCV2.dr|mCV2.dr_corr|mCV2.dr_set|mCV2.enableClippingOutput|mCV2.eps|mCV2.h_in|mCV2.h_out|mCV2.initM_flow|der.mCV2.inlet.m_flow.|mCV2.inlet.m_flow|mCV2.inlet.r|mCV2.inlet.state.T|mCV2.inlet.state.d|mCV2.inlet.state.h|mCV2.inlet.state.p|mCV2.inlet.state.phase|mCV2.k1|mCV2.k2|mCV2.m_acceleration_0|mCV2.m_flow|mCV2.m_flowStateSelect|mCV2.m_flow_0|mCV2.m_flow_set|mCV2.massFlow_set_par|mCV2.mode|mCV2.outlet.m_flow|mCV2.outlet.r|mCV2.outlet.state.T|mCV2.outlet.state.d|mCV2.outlet.state.h|mCV2.outlet.state.p|mCV2.outlet.state.phase|mCV2.p_in|mCV2.p_min|mCV2.p_min_par|mCV2.p_out|mCV2.rho_in|mCV2.setpoint|mCV2.volumeFlow_set_par|mCV3.L|mCV3.TC|mCV3.V_flow|mCV3.V_flow_set|mCV3.clip_p_out|der.mCV3.dp_int.|mCV3.dp|mCV3.dp_corr|mCV3.dp_int|mCV3.dr|mCV3.dr_corr|mCV3.dr_set|mCV3.enableClippingOutput|mCV3.eps|mCV3.h_in|mCV3.h_out|mCV3.initM_flow|der.mCV3.inlet.m_flow.|mCV3.inlet.m_flow|mCV3.inlet.r|mCV3.inlet.state.T|mCV3.inlet.state.d|mCV3.inlet.state.h|mCV3.inlet.state.p|mCV3.inlet.state.phase|mCV3.k1|mCV3.k2|mCV3.m_acceleration_0|mCV3.m_flow|mCV3.m_flowStateSelect|mCV3.m_flow_0|mCV3.m_flow_set|mCV3.massFlow_set_par|mCV3.mode|mCV3.outlet.m_flow|mCV3.outlet.r|mCV3.outlet.state.T|mCV3.outlet.state.d|mCV3.outlet.state.h|mCV3.outlet.state.p|mCV3.outlet.state.phase|mCV3.p_in|mCV3.p_min|mCV3.p_min_par|mCV3.p_out|mCV3.rho_in|mCV3.setpoint|mCV3.volumeFlow_set_par|prescribedTemperature.T|prescribedTemperature.port.Q_flow|prescribedTemperature.port.T|prescribedTemperature1.T|prescribedTemperature1.port.Q_flow|prescribedTemperature1.port.T|sink.L|der.sink.inlet.m_flow.|sink.inlet.m_flow|sink.inlet.r|sink.inlet.state.T|sink.inlet.state.d|sink.inlet.state.h|sink.inlet.state.p|sink.inlet.state.phase|sink.p|sink.p0|sink.p0_par|sink.r|sink1.L|der.sink1.inlet.m_flow.|sink1.inlet.m_flow|sink1.inlet.r|sink1.inlet.state.T|sink1.inlet.state.d|sink1.inlet.state.h|sink1.inlet.state.p|sink1.inlet.state.phase|sink1.p|sink1.p0|sink1.p0_par|sink1.r|sink2.L|der.sink2.inlet.m_flow.|sink2.inlet.m_flow|sink2.inlet.r|sink2.inlet.state.T|sink2.inlet.state.d|sink2.inlet.state.h|sink2.inlet.state.p|sink2.inlet.state.phase|sink2.p|sink2.p0|sink2.p0_par|sink2.r|sink3.L|der.sink3.inlet.m_flow.|sink3.inlet.m_flow|sink3.inlet.r|sink3.inlet.state.T|sink3.inlet.state.d|sink3.inlet.state.h|sink3.inlet.state.p|sink3.inlet.state.phase|sink3.p|sink3.p0|sink3.p0_par|sink3.r|source.L|source.T0|source.T0_par|source.h0|source.h0_par|source.h0_var|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|source1.L|source1.T0|source1.T0_par|source1.h0|source1.h0_par|der.source1.outlet.m_flow.|source1.outlet.m_flow|source1.outlet.r|source1.outlet.state.T|source1.outlet.state.d|source1.outlet.state.h|source1.outlet.state.p|source1.outlet.state.phase|source1.p0|source1.p0_par|source2.L|source2.T0|source2.T0_par|source2.h0|source2.h0_par|source2.h0_var|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|trapezoid.T_falling|trapezoid.T_rising|trapezoid.T_start|trapezoid.T_width|trapezoid.amplitude|trapezoid.count|trapezoid.falling|trapezoid.nperiod|trapezoid.offset|trapezoid.period|trapezoid.rising|trapezoid.startTime|trapezoid.width|trapezoid.y|trapezoid2.T_falling|trapezoid2.T_rising|trapezoid2.T_start|trapezoid2.T_width|trapezoid2.amplitude|trapezoid2.count|trapezoid2.falling|trapezoid2.nperiod|trapezoid2.offset|trapezoid2.period|trapezoid2.rising|trapezoid2.startTime|trapezoid2.width|trapezoid2.y|volume.A|volume.L|volume.M|volume.Q_flow|volume.T_heatPort|volume.T_start|volume.U|volume.U_med|volume.V|volume.V_par|volume.W_v|volume.d|volume.density_derp_h|volume.density_derp_h_set|der.volume.M.|der.volume.U_med.|der.volume.m_flow_in.|der.volume.m_flow_out.|volume.h_in|volume.h_out|volume.h_start|volume.inlet.m_flow|volume.inlet.r|volume.inlet.state.T|volume.inlet.state.d|volume.inlet.state.h|volume.inlet.state.p|volume.inlet.state.phase|volume.k_volume_damping|volume.m_flow_assert|volume.m_flow_in|volume.m_flow_out|volume.medium.MM|volume.medium.R_s|volume.medium.T|volume.medium.T_degC|volume.medium.X.[0-9,]+.|volume.medium.d|der.volume.medium.h.|der.volume.medium.p.|der.volume.medium.u.|volume.medium.h|volume.medium.p|volume.medium.p_bar|volume.medium.phase|volume.medium.preferredMediumStates|volume.medium.quality|volume.medium.sat.Tsat|volume.medium.sat.psat|volume.medium.standardOrderComponents|volume.medium.state.T|volume.medium.state.d|der.volume.medium.state.d.|volume.medium.state.h|volume.medium.state.p|volume.medium.state.phase|volume.medium.u|volume.outlet.m_flow|volume.outlet.r|volume.outlet.state.T|volume.outlet.state.d|volume.outlet.state.h|volume.outlet.state.p|volume.outlet.state.phase|volume.p_in|volume.p_start|volume.r|volume.r_damping|volume.r_in|volume.r_out|volume.state_in.T|volume.state_in.d|volume.state_in.h|volume.state_in.p|volume.state_in.phase|volume.state_out.T|volume.state_out.d|volume.state_out.h|volume.state_out.p|volume.state_out.phase|volume1.A|volume1.L|volume1.M|volume1.Q_flow|volume1.T_heatPort|volume1.T_start|volume1.U|volume1.U_med|volume1.V|volume1.V_par|volume1.W_v|volume1.d|volume1.density_derp_h|volume1.density_derp_h_set|der.volume1.M.|der.volume1.U_med.|der.volume1.m_flow_in.|der.volume1.m_flow_out.|volume1.h_in|volume1.h_out|volume1.h_start|volume1.heatPort.Q_flow|volume1.heatPort.T|volume1.inlet.m_flow|volume1.inlet.r|volume1.inlet.state.T|volume1.inlet.state.d|volume1.inlet.state.h|volume1.inlet.state.p|volume1.inlet.state.phase|volume1.k_volume_damping|volume1.m_flow_assert|volume1.m_flow_in|volume1.m_flow_out|volume1.medium.MM|volume1.medium.R_s|volume1.medium.T|volume1.medium.T_degC|volume1.medium.X.[0-9,]+.|volume1.medium.d|der.volume1.medium.h.|der.volume1.medium.p.|der.volume1.medium.u.|volume1.medium.h|volume1.medium.p|volume1.medium.p_bar|volume1.medium.phase|volume1.medium.preferredMediumStates|volume1.medium.quality|volume1.medium.sat.Tsat|volume1.medium.sat.psat|volume1.medium.standardOrderComponents|volume1.medium.state.T|volume1.medium.state.d|der.volume1.medium.state.d.|volume1.medium.state.h|volume1.medium.state.p|volume1.medium.state.phase|volume1.medium.u|volume1.outlet.m_flow|volume1.outlet.r|volume1.outlet.state.T|volume1.outlet.state.d|volume1.outlet.state.h|volume1.outlet.state.p|volume1.outlet.state.phase|volume1.p_in|volume1.p_start|volume1.r|volume1.r_damping|volume1.r_in|volume1.r_out|volume1.state_in.T|volume1.state_in.d|volume1.state_in.h|volume1.state_in.p|volume1.state_in.phase|volume1.state_out.T|volume1.state_out.d|volume1.state_out.h|volume1.state_out.p|volume1.state_out.phase",fileNamePrefix="ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase") [Timeout 660] "Notification: Performance of FrontEnd - loaded program: time 1.263e-06/1.263e-06, allocations: 0 / 430.9 MB, free: 13.26 MB / 410.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 9.648e-06/1.091e-05, allocations: 2.312 kB / 430.9 MB, free: 13.25 MB / 410.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase): time 0.1599/0.1599, allocations: 22.37 MB / 453.2 MB, free: 14.17 MB / 410.7 MB Notification: Performance of NFInst.instExpressions: time 0.01273/0.1726, allocations: 17.18 MB / 470.4 MB, free: 3.012 MB / 410.7 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.0008517/0.1735, allocations: 128 kB / 470.5 MB, free: 2.934 MB / 410.7 MB Notification: Performance of NFTyping.typeComponents: time 0.0007324/0.1742, allocations: 0.5587 MB / 471.1 MB, free: 2.441 MB / 410.7 MB Notification: Performance of NFTyping.typeBindings: time 0.00489/0.1791, allocations: 3.818 MB / 474.9 MB, free: 15 MB / 426.7 MB Notification: Performance of NFTyping.typeClassSections: time 0.001686/0.1808, allocations: 1.184 MB / 476.1 MB, free: 13.82 MB / 426.7 MB Notification: Performance of NFFlatten.flatten: time 0.002985/0.1838, allocations: 4.616 MB / 480.7 MB, free: 9.18 MB / 426.7 MB Notification: Performance of NFFlatten.resolveConnections: time 0.000513/0.1843, allocations: 465.7 kB / 481.2 MB, free: 8.676 MB / 426.7 MB Notification: Performance of NFEvalConstants.evaluate: time 0.002162/0.1864, allocations: 2.426 MB / 483.6 MB, free: 6.246 MB / 426.7 MB Notification: Performance of NFSimplifyModel.simplify: time 0.0009908/0.1874, allocations: 1.18 MB / 484.8 MB, free: 5.062 MB / 426.7 MB Notification: Performance of NFPackage.collectConstants: time 0.0002105/0.1876, allocations: 204 kB / 485 MB, free: 4.863 MB / 426.7 MB Notification: Performance of NFFlatten.collectFunctions: time 0.005425/0.1931, allocations: 5.954 MB / 490.9 MB, free: 14.9 MB / 442.7 MB Notification: Performance of NFScalarize.scalarize: time 0.0003382/0.1934, allocations: 0.5443 MB / 491.5 MB, free: 14.35 MB / 442.7 MB Notification: Performance of NFVerifyModel.verify: time 0.0007871/0.1942, allocations: 0.9858 MB / 492.5 MB, free: 13.36 MB / 442.7 MB Notification: Performance of NFConvertDAE.convert: time 0.007227/0.2014, allocations: 7.254 MB / 499.7 MB, free: 6.094 MB / 442.7 MB Notification: Performance of FrontEnd - DAE generated: time 3.296e-06/0.2014, allocations: 1.719 kB / 499.7 MB, free: 6.094 MB / 442.7 MB Notification: Performance of FrontEnd: time 8.81e-07/0.2014, allocations: 0 / 499.7 MB, free: 6.094 MB / 442.7 MB Notification: Performance of Transformations before backend: time 1.788e-05/0.2014, allocations: 0 / 499.7 MB, free: 6.094 MB / 442.7 MB Notification: Model statistics after passing the front-end and creating the data structures used by the back-end: * Number of equations: 520 * Number of variables: 520 Notification: Performance of Generate backend data structure: time 0.003889/0.2053, allocations: 3.393 MB / 0.4913 GB, free: 2.645 MB / 442.7 MB Notification: Performance of prepare preOptimizeDAE: time 3.051e-05/0.2054, allocations: 12.95 kB / 0.4913 GB, free: 2.633 MB / 442.7 MB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001586/0.2069, allocations: 0.8699 MB / 0.4922 GB, free: 1.762 MB / 442.7 MB Notification: Performance of preOpt evaluateParameters (simulation): time 0.001605/0.2085, allocations: 1.441 MB / 0.4936 GB, free: 260 kB / 442.7 MB Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0002864/0.2088, allocations: 135.6 kB / 0.4937 GB, free: 124 kB / 442.7 MB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001936/0.209, allocations: 208.7 kB / 0.4939 GB, free: 15.91 MB / 458.7 MB Notification: Performance of preOpt clockPartitioning (simulation): time 0.001574/0.2106, allocations: 1.89 MB / 0.4958 GB, free: 13.82 MB / 458.7 MB Notification: Performance of preOpt findStateOrder (simulation): time 3.14e-05/0.2106, allocations: 7.938 kB / 0.4958 GB, free: 13.82 MB / 458.7 MB Notification: Performance of preOpt replaceEdgeChange (simulation): time 9.696e-05/0.2107, allocations: 81.09 kB / 0.4959 GB, free: 13.74 MB / 458.7 MB Notification: Performance of preOpt inlineArrayEqn (simulation): time 3.82e-05/0.2108, allocations: 67.91 kB / 0.4959 GB, free: 13.67 MB / 458.7 MB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0008493/0.2116, allocations: 0.6622 MB / 0.4966 GB, free: 13.01 MB / 458.7 MB Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts. Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.00538/0.217, allocations: 5.619 MB / 0.5021 GB, free: 7.262 MB / 458.7 MB Notification: Performance of preOpt comSubExp (simulation): time 0.001168/0.2182, allocations: 0.8073 MB / 0.5028 GB, free: 6.461 MB / 458.7 MB Notification: Performance of preOpt resolveLoops (simulation): time 0.0003569/0.2185, allocations: 347.8 kB / 0.5032 GB, free: 6.117 MB / 458.7 MB Notification: Performance of preOpt evalFunc (simulation): time 0.001008/0.2195, allocations: 0.6191 MB / 0.5038 GB, free: 5.504 MB / 458.7 MB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0007785/0.2203, allocations: 0.9905 MB / 0.5047 GB, free: 4.418 MB / 458.7 MB Notification: Performance of pre-optimization done (n=221): time 3.216e-06/0.2203, allocations: 1.344 kB / 0.5047 GB, free: 4.418 MB / 458.7 MB Notification: Performance of matching and sorting (n=229): time 0.007228/0.2275, allocations: 3.416 MB / 0.5081 GB, free: 0.9375 MB / 458.7 MB Notification: Performance of inlineWhenForInitialization (initialization): time 5.72e-05/0.2276, allocations: 153.9 kB / 0.5082 GB, free: 0.7617 MB / 458.7 MB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0008475/0.2284, allocations: 1.357 MB / 0.5096 GB, free: 15.36 MB / 474.7 MB Notification: Performance of collectPreVariables (initialization): time 7.942e-05/0.2285, allocations: 57.7 kB / 0.5096 GB, free: 15.3 MB / 474.7 MB Notification: Performance of collectInitialEqns (initialization): time 0.0003347/0.2289, allocations: 0.7328 MB / 0.5103 GB, free: 14.56 MB / 474.7 MB Notification: Performance of collectInitialBindings (initialization): time 0.0003719/0.2292, allocations: 0.7898 MB / 0.5111 GB, free: 13.76 MB / 474.7 MB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003316/0.2296, allocations: 351.7 kB / 0.5114 GB, free: 13.41 MB / 474.7 MB Notification: Performance of setup shared object (initialization): time 5.851e-05/0.2296, allocations: 305.1 kB / 0.5117 GB, free: 13.11 MB / 474.7 MB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003406/0.23, allocations: 279.5 kB / 0.512 GB, free: 12.82 MB / 474.7 MB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004917/0.2304, allocations: 0.6561 MB / 0.5126 GB, free: 12.03 MB / 474.7 MB Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: conductionElementHEX_twoPhase.deltaE_system = $START.conductionElementHEX_twoPhase.deltaE_system (0.0 = $START.conductionElementHEX_twoPhase.deltaE_system) Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: conductionElementHEX_twoPhase1.deltaE_system = $START.conductionElementHEX_twoPhase1.deltaE_system (0.0 = $START.conductionElementHEX_twoPhase1.deltaE_system) Notification: Performance of analyzeInitialSystem (initialization): time 0.000975/0.2314, allocations: 1.061 MB / 0.5137 GB, free: 10.86 MB / 474.7 MB Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.199e-06/0.2314, allocations: 4 kB / 0.5137 GB, free: 10.86 MB / 474.7 MB Notification: Performance of matching and sorting (n=283) (initialization): time 0.001646/0.2331, allocations: 1.324 MB / 0.515 GB, free: 9.473 MB / 474.7 MB Notification: Performance of prepare postOptimizeDAE: time 3.887e-05/0.2331, allocations: 72.11 kB / 0.515 GB, free: 9.391 MB / 474.7 MB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.094e-05/0.2331, allocations: 8 kB / 0.515 GB, free: 9.383 MB / 474.7 MB Notification: Performance of postOpt tearingSystem (initialization): time 0.004391/0.2375, allocations: 0.5946 MB / 0.5156 GB, free: 8.766 MB / 474.7 MB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0007234/0.2382, allocations: 355.5 kB / 0.516 GB, free: 8.418 MB / 474.7 MB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003465/0.2417, allocations: 8.324 MB / 0.5241 GB, free: 15.54 MB / 490.7 MB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0005433/0.2422, allocations: 80.08 kB / 0.5242 GB, free: 15.46 MB / 490.7 MB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 8.944e-05/0.2423, allocations: 66.45 kB / 0.5242 GB, free: 15.4 MB / 490.7 MB Warning: The initial conditions are over specified. The following 2 initial equations are redundant, so they are removed from the initialization system: conductionElementHEX_twoPhase.deltaE_system = $START.conductionElementHEX_twoPhase.deltaE_system conductionElementHEX_twoPhase1.deltaE_system = $START.conductionElementHEX_twoPhase1.deltaE_system. Notification: Model statistics after passing the back-end for initialization: * Number of independent subsystems: 32 * Number of states: 0 () * Number of discrete variables: 28 (trapezoid2.count,$PRE.trapezoid2.count,trapezoid2.T_start,$PRE.trapezoid2.T_start,flowResistance.outlet.state.phase,source2.outlet.state.phase,mCV2.outlet.state.phase,volume.inlet.state.phase,source.outlet.state.phase,mCV.outlet.state.phase,conductionElementHEX_twoPhase.state.phase,conductionElementHEX_twoPhase.outlet.state.phase,$whenCondition1,volume.medium.phase,flowResistance2.outlet.state.phase,source3.outlet.state.phase,mCV3.outlet.state.phase,volume1.inlet.state.phase,trapezoid.count,$PRE.trapezoid.count,trapezoid.T_start,$PRE.trapezoid.T_start,source1.outlet.state.phase,mCV1.outlet.state.phase,conductionElementHEX_twoPhase1.state.phase,conductionElementHEX_twoPhase1.outlet.state.phase,$whenCondition2,volume1.medium.phase) * Number of discrete states: 0 () * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for initialization (199): * Single equations (assignments): 173 * Array equations: 0 * Algorithm blocks: 2 * Record equations: 16 * When equations: 0 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 8 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 6 systems {(1,4,100.0%), (1,2,100.0%), (1,2,100.0%), (1,4,100.0%), (1,2,100.0%), (1,2,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 2 systems {(1,1), (1,1)} Notification: Performance of prepare postOptimizeDAE: time 0.0003566/0.2427, allocations: 234.7 kB / 0.5245 GB, free: 15.17 MB / 490.7 MB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0002098/0.2429, allocations: 199.7 kB / 0.5246 GB, free: 14.98 MB / 490.7 MB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.002093/0.245, allocations: 1.921 MB / 0.5265 GB, free: 13.04 MB / 490.7 MB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.001259/0.2463, allocations: 1.246 MB / 0.5277 GB, free: 11.75 MB / 490.7 MB Notification: Performance of postOpt constantLinearSystem (simulation): time 7.153e-06/0.2463, allocations: 7.938 kB / 0.5277 GB, free: 11.75 MB / 490.7 MB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.613e-05/0.2463, allocations: 11.95 kB / 0.5278 GB, free: 11.73 MB / 490.7 MB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.004192/0.2505, allocations: 3.576 MB / 0.5312 GB, free: 8.047 MB / 490.7 MB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 6.642e-06/0.2505, allocations: 4 kB / 0.5313 GB, free: 8.043 MB / 490.7 MB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0008734/0.2514, allocations: 415.9 kB / 0.5316 GB, free: 7.637 MB / 490.7 MB Notification: Performance of postOpt tearingSystem (simulation): time 0.001301/0.2527, allocations: 0.5397 MB / 0.5322 GB, free: 7.062 MB / 490.7 MB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 8.775e-05/0.2527, allocations: 67.95 kB / 0.5322 GB, free: 6.996 MB / 490.7 MB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.003743/0.2565, allocations: 9.478 MB / 0.5415 GB, free: 12.9 MB / 0.4948 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 3.928e-06/0.2565, allocations: 8 kB / 0.5415 GB, free: 12.89 MB / 0.4948 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.00248/0.259, allocations: 2.386 MB / 0.5438 GB, free: 10.36 MB / 0.4948 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0004385/0.2594, allocations: 313.4 kB / 0.5441 GB, free: 10.05 MB / 0.4948 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.000167/0.2596, allocations: 59.95 kB / 0.5442 GB, free: 9.992 MB / 0.4948 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0005949/0.2602, allocations: 97.03 kB / 0.5443 GB, free: 9.898 MB / 0.4948 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0001908/0.2604, allocations: 197.8 kB / 0.5445 GB, free: 9.703 MB / 0.4948 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 8.252e-05/0.2604, allocations: 67.95 kB / 0.5445 GB, free: 9.637 MB / 0.4948 GB Notification: Performance of sorting global known variables: time 0.0004911/0.2609, allocations: 0.7052 MB / 0.5452 GB, free: 8.906 MB / 0.4948 GB Notification: Performance of sort global known variables: time 8e-08/0.2609, allocations: 0 / 0.5452 GB, free: 8.906 MB / 0.4948 GB Notification: Performance of remove unused functions: time 0.002044/0.263, allocations: 1.014 MB / 0.5462 GB, free: 7.891 MB / 0.4948 GB Notification: Model statistics after passing the back-end for simulation: * Number of independent subsystems: 18 * Number of states: 16 (conductionElementHEX_twoPhase.h,mCV.dp_int,volume.M,volume.U_med,mCV2.inlet.m_flow,mCV2.dp_int,flowResistance.inlet.m_flow,flowResistance1.inlet.m_flow,conductionElementHEX_twoPhase1.h,mCV1.dp_int,volume1.M,volume1.U_med,mCV3.inlet.m_flow,mCV3.dp_int,flowResistance2.inlet.m_flow,flowResistance3.inlet.m_flow) * Number of discrete variables: 38 (conductionElementHEX_twoPhase.state.phase,conductionElementHEX_twoPhase.outlet.state.phase,mCV.outlet.state.phase,flowResistance.outlet.state.phase,source.outlet.state.phase,mCV2.outlet.state.phase,volume.inlet.state.phase,source2.outlet.state.phase,$cse17.phase,$cse21.phase,$cse22.phase,$cse23.phase,$cse24,$cse28.phase,$cse29.phase,$cse30.phase,$cse31.phase,$whenCondition1,trapezoid2.T_start,trapezoid2.count,conductionElementHEX_twoPhase1.state.phase,conductionElementHEX_twoPhase1.outlet.state.phase,mCV1.outlet.state.phase,flowResistance2.outlet.state.phase,mCV3.outlet.state.phase,volume1.inlet.state.phase,$cse1.phase,$cse5.phase,$cse7.phase,$cse8,$cse12.phase,$cse14.phase,$cse15.phase,$whenCondition2,trapezoid.T_start,trapezoid.count,source3.outlet.state.phase,source1.outlet.state.phase) * Number of discrete states: 2 (trapezoid.count,trapezoid2.count) * Number of clocked states: 0 () * Top-level inputs: 0 Notification: Strong component statistics for simulation (235): * Single equations (assignments): 207 * Array equations: 0 * Algorithm blocks: 0 * Record equations: 14 * When equations: 4 * If-equations: 0 * Equation systems (not torn): 0 * Torn equation systems: 10 * Mixed (continuous/discrete) equation systems: 0 Notification: Torn system details for strict tearing set: * Linear torn systems (#iteration vars, #inner vars, density): 6 systems {(1,4,100.0%), (1,2,100.0%), (1,2,100.0%), (1,4,100.0%), (1,2,100.0%), (1,2,100.0%)} * Non-linear torn systems (#iteration vars, #inner vars): 4 systems {(1,1), (1,3), (1,1), (1,3)} Notification: Performance of Backend phase and start with SimCode phase: time 0.007902/0.2709, allocations: 3.766 MB / 0.5499 GB, free: 4.141 MB / 0.4948 GB Notification: Performance of simCode: created initialization part: time 0.001827/0.2727, allocations: 2.613 MB / 0.5524 GB, free: 1.301 MB / 0.4948 GB Notification: Performance of simCode: created event and clocks part: time 2.601e-05/0.2727, allocations: 24.5 kB / 0.5525 GB, free: 1.277 MB / 0.4948 GB Notification: Performance of simCode: created simulation system equations: time 0.001054/0.2738, allocations: 1.462 MB / 0.5539 GB, free: 15.73 MB / 0.5105 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.002548/0.2763, allocations: 1.238 MB / 0.5551 GB, free: 14.55 MB / 0.5105 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.005116/0.2814, allocations: 4.817 MB / 0.5598 GB, free: 9.629 MB / 0.5105 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0003597/0.2818, allocations: 0.4897 MB / 0.5603 GB, free: 9.117 MB / 0.5105 GB Notification: Performance of simCode: alias equations: time 0.0008214/0.2826, allocations: 455.2 kB / 0.5607 GB, free: 8.684 MB / 0.5105 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.00156/0.2842, allocations: 0.9244 MB / 0.5616 GB, free: 7.738 MB / 0.5105 GB Notification: Performance of SimCode: time 8.82e-07/0.2842, allocations: 0 / 0.5616 GB, free: 7.738 MB / 0.5105 GB Notification: Performance of Templates: time 0.06958/0.3538, allocations: 70.53 MB / 0.6305 GB, free: 2.195 MB / 0.573 GB " [Timeout remaining time 660] make -j1 -f ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.makefile [Timeout 660] (rm -f ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe ; mkfifo ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe >> ../files/ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.sim & ./ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase -abortSlowSimulation -alarm=240 -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase.pipe 2>&1) [Timeout 240] diffSimulationResults("ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660] "Error: Could not read variable CPUtime in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable conductionElementHEX_twoPhase.Re_exp_cond in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable conductionElementHEX_twoPhase.Re_exp_cond from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable conductionElementHEX_twoPhase.Re_exp_evap in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable conductionElementHEX_twoPhase.Re_exp_evap from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable conductionElementHEX_twoPhase.U_min in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable conductionElementHEX_twoPhase.U_min from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable conductionElementHEX_twoPhase1.Re_exp_cond in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable conductionElementHEX_twoPhase1.Re_exp_cond from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable conductionElementHEX_twoPhase1.Re_exp_evap in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable conductionElementHEX_twoPhase1.Re_exp_evap from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable conductionElementHEX_twoPhase1.U_min in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable conductionElementHEX_twoPhase1.U_min from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable mCV.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable mCV.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable mCV1.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable mCV1.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable mCV2.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable mCV2.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable mCV3.eps in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable mCV3.eps from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable sink1.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable sink1.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable volume.der(m_flow_in) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable volume.der(m_flow_in) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable volume.der(m_flow_out) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable volume.der(m_flow_out) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable volume.medium.state.der(d) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable volume.medium.state.der(d) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable volume1.der(m_flow_in) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable volume1.der(m_flow_in) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable volume1.der(m_flow_out) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable volume1.der(m_flow_out) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! Error: Could not read variable volume1.medium.state.der(d) in file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat. Warning: Get data of variable volume1.medium.state.der(d) from file ThermofluidStream_ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase_res.mat failed! " [Timeout remaining time 660] Reference file matches [Calling sys.exit(0), Time elapsed: 13.851519502233714]