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 0.001046/0.001046, allocations: 80.94 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 0.001065/0.001065, allocations: 177.4 kB / 23.36 MB, free: 1.129 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 0.9684/0.9684, allocations: 177.1 MB / 203.8 MB, free: 5.469 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 0.7254/0.7254, allocations: 118.6 MB / 378.9 MB, free: 1.355 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 1.653e-06/1.653e-06, allocations: 0 / 430.9 MB, free: 13.24 MB / 410.7 MB Notification: Performance of FrontEnd - Absyn->SCode: time 1.997e-05/2.162e-05, allocations: 6.312 kB / 430.9 MB, free: 13.23 MB / 410.7 MB Notification: Performance of NFInst.instantiate(ThermofluidStream.HeatExchangers.Tests.ElementTwoPhase): time 0.2014/0.2014, allocations: 22.4 MB / 453.3 MB, free: 14.13 MB / 410.7 MB Notification: Performance of NFInst.instExpressions: time 0.01565/0.2171, allocations: 17.18 MB / 470.5 MB, free: 2.949 MB / 410.7 MB Notification: Performance of NFInst.updateImplicitVariability: time 0.001202/0.2183, allocations: 129.7 kB / 470.6 MB, free: 2.871 MB / 410.7 MB Notification: Performance of NFTyping.typeComponents: time 0.0006848/0.219, allocations: 0.5494 MB / 471.2 MB, free: 2.387 MB / 410.7 MB Notification: Performance of NFTyping.typeBindings: time 0.006071/0.225, allocations: 3.694 MB / 474.9 MB, free: 15.05 MB / 426.7 MB Notification: Performance of NFTyping.typeClassSections: time 0.002041/0.2271, allocations: 1.157 MB / 476 MB, free: 13.9 MB / 426.7 MB Notification: Performance of NFFlatten.flatten: time 0.004819/0.2319, allocations: 4.625 MB / 480.7 MB, free: 9.254 MB / 426.7 MB Notification: Performance of NFFlatten.resolveConnections: time 0.0007634/0.2326, allocations: 452.5 kB / 481.1 MB, free: 8.762 MB / 426.7 MB Notification: Performance of NFEvalConstants.evaluate: time 0.003729/0.2364, allocations: 2.425 MB / 483.5 MB, free: 6.332 MB / 426.7 MB Notification: Performance of NFSimplifyModel.simplify: time 0.001803/0.2382, allocations: 1.188 MB / 484.7 MB, free: 5.141 MB / 426.7 MB Notification: Performance of NFPackage.collectConstants: time 0.000365/0.2385, allocations: 200 kB / 484.9 MB, free: 4.945 MB / 426.7 MB Notification: Performance of NFFlatten.collectFunctions: time 0.007846/0.2464, allocations: 6.086 MB / 491 MB, free: 14.85 MB / 442.7 MB Notification: Performance of NFScalarize.scalarize: time 0.0003548/0.2467, allocations: 0.5443 MB / 491.6 MB, free: 14.3 MB / 442.7 MB Notification: Performance of NFVerifyModel.verify: time 0.001127/0.2479, allocations: 0.9936 MB / 492.5 MB, free: 13.31 MB / 442.7 MB Notification: Performance of NFConvertDAE.convert: time 0.009407/0.2573, allocations: 7.25 MB / 499.8 MB, free: 6.043 MB / 442.7 MB Notification: Performance of FrontEnd - DAE generated: time 4.158e-06/0.2573, allocations: 1.719 kB / 499.8 MB, free: 6.043 MB / 442.7 MB Notification: Performance of FrontEnd: time 9.42e-07/0.2573, allocations: 0 / 499.8 MB, free: 6.043 MB / 442.7 MB Notification: Performance of Transformations before backend: time 6.042e-05/0.2573, allocations: 0 / 499.8 MB, free: 6.043 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 0.004389/0.2617, allocations: 3.385 MB / 0.4914 GB, free: 2.602 MB / 442.7 MB Notification: Performance of prepare preOptimizeDAE: time 2.99e-05/0.2618, allocations: 12.03 kB / 0.4914 GB, free: 2.59 MB / 442.7 MB Notification: Performance of preOpt normalInlineFunction (simulation): time 0.001807/0.2636, allocations: 0.8747 MB / 0.4923 GB, free: 1.715 MB / 442.7 MB Notification: Performance of preOpt evaluateParameters (simulation): time 0.00189/0.2655, allocations: 1.442 MB / 0.4937 GB, free: 208 kB / 442.7 MB Notification: Performance of preOpt simplifyIfEquations (simulation): time 7.475e-05/0.2655, allocations: 136.9 kB / 0.4938 GB, free: 72 kB / 442.7 MB Notification: Performance of preOpt expandDerOperator (simulation): time 0.0001855/0.2657, allocations: 203.9 kB / 0.494 GB, free: 15.87 MB / 458.7 MB Notification: Performance of preOpt clockPartitioning (simulation): time 0.001659/0.2674, allocations: 1.897 MB / 0.4958 GB, free: 13.77 MB / 458.7 MB Notification: Performance of preOpt findStateOrder (simulation): time 3.146e-05/0.2674, allocations: 5.344 kB / 0.4958 GB, free: 13.77 MB / 458.7 MB Notification: Performance of preOpt replaceEdgeChange (simulation): time 9.142e-05/0.2675, allocations: 76 kB / 0.4959 GB, free: 13.69 MB / 458.7 MB Notification: Performance of preOpt inlineArrayEqn (simulation): time 4.163e-05/0.2675, allocations: 71.91 kB / 0.496 GB, free: 13.62 MB / 458.7 MB Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0008911/0.2684, allocations: 0.661 MB / 0.4966 GB, free: 12.96 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 0.005746/0.2742, allocations: 5.616 MB / 0.5021 GB, free: 7.215 MB / 458.7 MB Notification: Performance of preOpt comSubExp (simulation): time 0.001233/0.2754, allocations: 0.8098 MB / 0.5029 GB, free: 6.41 MB / 458.7 MB Notification: Performance of preOpt resolveLoops (simulation): time 0.0003878/0.2758, allocations: 350 kB / 0.5032 GB, free: 6.066 MB / 458.7 MB Notification: Performance of preOpt evalFunc (simulation): time 0.001059/0.2769, allocations: 0.6145 MB / 0.5038 GB, free: 5.457 MB / 458.7 MB Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0008206/0.2777, allocations: 0.9913 MB / 0.5048 GB, free: 4.371 MB / 458.7 MB Notification: Performance of pre-optimization done (n=221): time 2.765e-06/0.2777, allocations: 0 / 0.5048 GB, free: 4.371 MB / 458.7 MB Notification: Performance of matching and sorting (n=229): time 0.007284/0.285, allocations: 3.42 MB / 0.5082 GB, free: 0.8828 MB / 458.7 MB Notification: Performance of inlineWhenForInitialization (initialization): time 6.267e-05/0.285, allocations: 150.2 kB / 0.5083 GB, free: 0.707 MB / 458.7 MB Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0008607/0.2859, allocations: 1.357 MB / 0.5096 GB, free: 15.3 MB / 474.7 MB Notification: Performance of collectPreVariables (initialization): time 7.859e-05/0.286, allocations: 61.64 kB / 0.5097 GB, free: 15.24 MB / 474.7 MB Notification: Performance of collectInitialEqns (initialization): time 0.000336/0.2863, allocations: 0.7328 MB / 0.5104 GB, free: 14.5 MB / 474.7 MB Notification: Performance of collectInitialBindings (initialization): time 0.0003597/0.2867, allocations: 0.7859 MB / 0.5112 GB, free: 13.71 MB / 474.7 MB Notification: Performance of simplifyInitialFunctions (initialization): time 0.0003226/0.287, allocations: 359.7 kB / 0.5115 GB, free: 13.35 MB / 474.7 MB Notification: Performance of setup shared object (initialization): time 6e-05/0.287, allocations: 301.1 kB / 0.5118 GB, free: 13.05 MB / 474.7 MB Notification: Performance of preBalanceInitialSystem (initialization): time 0.0003301/0.2874, allocations: 279.5 kB / 0.5121 GB, free: 12.77 MB / 474.7 MB Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004767/0.2879, allocations: 0.6561 MB / 0.5127 GB, free: 11.97 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 0.0009373/0.2888, allocations: 1.057 MB / 0.5137 GB, free: 10.8 MB / 474.7 MB Notification: Performance of solveInitialSystemEqSystem (initialization): time 5.139e-06/0.2888, allocations: 4 kB / 0.5137 GB, free: 10.8 MB / 474.7 MB Notification: Performance of matching and sorting (n=283) (initialization): time 0.001598/0.2904, allocations: 1.323 MB / 0.515 GB, free: 9.418 MB / 474.7 MB Notification: Performance of prepare postOptimizeDAE: time 3.947e-05/0.2904, allocations: 75.73 kB / 0.5151 GB, free: 9.332 MB / 474.7 MB Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.107e-05/0.2904, allocations: 12 kB / 0.5151 GB, free: 9.32 MB / 474.7 MB Notification: Performance of postOpt tearingSystem (initialization): time 0.004223/0.2947, allocations: 0.5911 MB / 0.5157 GB, free: 8.707 MB / 474.7 MB Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0008589/0.2955, allocations: 433.2 kB / 0.5161 GB, free: 8.285 MB / 474.7 MB Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.003536/0.2991, allocations: 8.331 MB / 0.5242 GB, free: 15.41 MB / 490.7 MB Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0006253/0.2997, allocations: 79.95 kB / 0.5243 GB, free: 15.33 MB / 490.7 MB Notification: Performance of postOpt collapseArrayExpressions (initialization): time 9.532e-05/0.2998, allocations: 63.95 kB / 0.5244 GB, free: 15.27 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 0.0003693/0.3002, allocations: 235 kB / 0.5246 GB, free: 15.04 MB / 490.7 MB Notification: Performance of postOpt lateInlineFunction (simulation): time 0.0001818/0.3003, allocations: 187.8 kB / 0.5248 GB, free: 14.85 MB / 490.7 MB Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001995/0.3023, allocations: 1.928 MB / 0.5267 GB, free: 12.91 MB / 490.7 MB Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.001172/0.3035, allocations: 1.25 MB / 0.5279 GB, free: 11.62 MB / 490.7 MB Notification: Performance of postOpt constantLinearSystem (simulation): time 6.402e-06/0.3035, allocations: 4 kB / 0.5279 GB, free: 11.61 MB / 490.7 MB Notification: Performance of postOpt simplifysemiLinear (simulation): time 1.792e-05/0.3035, allocations: 11.95 kB / 0.5279 GB, free: 11.6 MB / 490.7 MB Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.004143/0.3077, allocations: 3.572 MB / 0.5314 GB, free: 7.918 MB / 490.7 MB Notification: Performance of postOpt simplifyComplexFunction (simulation): time 8.255e-06/0.3077, allocations: 4 kB / 0.5314 GB, free: 7.914 MB / 490.7 MB Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0009827/0.3087, allocations: 0.4883 MB / 0.5319 GB, free: 7.426 MB / 490.7 MB Notification: Performance of postOpt tearingSystem (simulation): time 0.001287/0.3099, allocations: 0.544 MB / 0.5324 GB, free: 6.852 MB / 490.7 MB Notification: Performance of postOpt inputDerivativesUsed (simulation): time 9.457e-05/0.31, allocations: 67.95 kB / 0.5325 GB, free: 6.785 MB / 490.7 MB Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.004051/0.3141, allocations: 9.476 MB / 0.5417 GB, free: 12.7 MB / 0.4948 GB Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 5.24e-06/0.3141, allocations: 11.92 kB / 0.5417 GB, free: 12.68 MB / 0.4948 GB Notification: Performance of postOpt symbolicJacobian (simulation): time 0.002611/0.3167, allocations: 2.383 MB / 0.5441 GB, free: 10.15 MB / 0.4948 GB Notification: Performance of postOpt removeConstants (simulation): time 0.0004952/0.3172, allocations: 309.8 kB / 0.5443 GB, free: 9.844 MB / 0.4948 GB Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001548/0.3174, allocations: 67.95 kB / 0.5444 GB, free: 9.777 MB / 0.4948 GB Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.000571/0.3179, allocations: 94.62 kB / 0.5445 GB, free: 9.688 MB / 0.4948 GB Notification: Performance of postOpt findZeroCrossings (simulation): time 0.0002314/0.3182, allocations: 197.8 kB / 0.5447 GB, free: 9.492 MB / 0.4948 GB Notification: Performance of postOpt collapseArrayExpressions (simulation): time 8.576e-05/0.3182, allocations: 67.94 kB / 0.5448 GB, free: 9.426 MB / 0.4948 GB Notification: Performance of sorting global known variables: time 0.000503/0.3188, allocations: 0.7052 MB / 0.5454 GB, free: 8.695 MB / 0.4948 GB Notification: Performance of sort global known variables: time 1.81e-07/0.3188, allocations: 0 / 0.5454 GB, free: 8.695 MB / 0.4948 GB Notification: Performance of remove unused functions: time 0.002804/0.3216, allocations: 1.011 MB / 0.5464 GB, free: 7.684 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 0.008015/0.3296, allocations: 3.769 MB / 0.5501 GB, free: 3.93 MB / 0.4948 GB Notification: Performance of simCode: created initialization part: time 0.002148/0.3317, allocations: 2.621 MB / 0.5527 GB, free: 1.086 MB / 0.4948 GB Notification: Performance of simCode: created event and clocks part: time 2.544e-05/0.3317, allocations: 20.5 kB / 0.5527 GB, free: 1.066 MB / 0.4948 GB Notification: Performance of simCode: created simulation system equations: time 0.001067/0.3328, allocations: 1.462 MB / 0.5541 GB, free: 15.52 MB / 0.5105 GB Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.002606/0.3354, allocations: 1.241 MB / 0.5553 GB, free: 14.33 MB / 0.5105 GB Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.005364/0.3408, allocations: 4.811 MB / 0.56 GB, free: 9.422 MB / 0.5105 GB Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0003543/0.3411, allocations: 0.4936 MB / 0.5605 GB, free: 8.906 MB / 0.5105 GB Notification: Performance of simCode: alias equations: time 0.001003/0.3421, allocations: 453 kB / 0.5609 GB, free: 8.473 MB / 0.5105 GB Notification: Performance of simCode: all other stuff during SimCode phase: time 0.001532/0.3437, allocations: 0.9283 MB / 0.5619 GB, free: 7.523 MB / 0.5105 GB Notification: Performance of SimCode: time 2.074e-06/0.3437, allocations: 0 / 0.5619 GB, free: 7.523 MB / 0.5105 GB Notification: Performance of Templates: time 0.07598/0.4197, allocations: 70.83 MB / 0.631 GB, free: 1.684 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 -s gbode -gbm=radauIIA3 -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: 14.114818168338388]