Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"[<interactive>:1:22-1:33:writable] Warning: Modelica only supports 32-bit signed integers! Transforming: 13743895347 into a real
[<interactive>:1:1-1:33:writable] Error: Class GC_set_max_heap_size not found in scope <global scope> (looking for a function or record).
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0003798/0.0003798, allocations: 0 / 0, free: 0 / 0
"
[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 0.0005021/0.0005021, allocations: 0 / 0, free: 0 / 0
"
[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 0.4247/0.4247, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 179]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo): time 0.282/0.282, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream main/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: simulate(ThermofluidStream.Media.Tests.TestXRGMedia,startTime=0,stopTime=10,tolerance=1e-06,numberOfIntervals=1000,outputFormat="mat",variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|NonlinearSystems.simulation.3..Calls|NonlinearSystems.simulation.3..Iterations|NonlinearSystems.simulation.3..Jacobians|NonlinearSystems.simulation.3..Residues|Time|basicControlValve.Cvs_UK|basicControlValve.Cvs_US|basicControlValve.Kvs|basicControlValve.L|basicControlValve.V_flow_ref|basicControlValve.clip_p_out|basicControlValve.dp|basicControlValve.dp_ref|basicControlValve.dr_corr|basicControlValve.flowCoefficient|basicControlValve.h_in|basicControlValve.h_out|basicControlValve.initM_flow|der.basicControlValve.inlet.m_flow.|basicControlValve.inlet.m_flow|basicControlValve.inlet.r|basicControlValve.inlet.state.T|basicControlValve.inlet.state.d|basicControlValve.inlet.state.h|basicControlValve.inlet.state.p|basicControlValve.inlet.state.phase|basicControlValve.k_min|basicControlValve.k_u|basicControlValve.m_acceleration_0|basicControlValve.m_flow|basicControlValve.m_flowStateSelect|basicControlValve.m_flow_0|basicControlValve.m_flow_ref|basicControlValve.m_flow_ref_set|basicControlValve.outlet.m_flow|basicControlValve.outlet.r|basicControlValve.outlet.state.T|basicControlValve.outlet.state.d|basicControlValve.outlet.state.h|basicControlValve.outlet.state.p|basicControlValve.outlet.state.phase|basicControlValve.p_in|basicControlValve.p_min|basicControlValve.p_out|basicControlValve.rho|basicControlValve.rho_ref|basicControlValve.secondsPerHour|basicControlValve.u|basicControlValve.u_in|conductionElement.A|conductionElement.L|conductionElement.M|conductionElement.Q_flow|conductionElement.T|conductionElement.T_0|conductionElement.T_e|conductionElement.T_heatPort|conductionElement.U|conductionElement.U_internal|conductionElement.V|conductionElement.clip_p_out|conductionElement.deltaE_system|der.conductionElement.h.|conductionElement.dp|conductionElement.dr_corr|conductionElement.h|conductionElement.h_0|conductionElement.h_in|conductionElement.h_in_norm|conductionElement.h_out|conductionElement.heatPort.Q_flow|conductionElement.heatPort.T|conductionElement.init|conductionElement.initM_flow|der.conductionElement.inlet.m_flow.|conductionElement.inlet.m_flow|conductionElement.inlet.r|conductionElement.inlet.state.T|conductionElement.inlet.state.d|conductionElement.inlet.state.h|conductionElement.inlet.state.p|conductionElement.inlet.state.phase|conductionElement.k|conductionElement.k_internal|conductionElement.k_par|conductionElement.m_acceleration_0|conductionElement.m_flow|conductionElement.m_flowStateSelect|conductionElement.m_flow_0|conductionElement.m_flow_assert|conductionElement.outlet.m_flow|conductionElement.outlet.r|conductionElement.outlet.state.T|conductionElement.outlet.state.d|conductionElement.outlet.state.h|conductionElement.outlet.state.p|conductionElement.outlet.state.phase|conductionElement.p_in|conductionElement.p_min|conductionElement.p_out|conductionElement.rho|conductionElement.rho_min|conductionElement.state.T|conductionElement.state.d|conductionElement.state.h|conductionElement.state.p|conductionElement.state.phase|conductionElement1.A|conductionElement1.L|conductionElement1.M|conductionElement1.Q_flow|conductionElement1.T|conductionElement1.T_0|conductionElement1.T_e|conductionElement1.T_heatPort|conductionElement1.U|conductionElement1.U_internal|conductionElement1.V|conductionElement1.clip_p_out|conductionElement1.deltaE_system|der.conductionElement1.h.|conductionElement1.dp|conductionElement1.dr_corr|conductionElement1.h|conductionElement1.h_0|conductionElement1.h_in|conductionElement1.h_in_norm|conductionElement1.h_out|conductionElement1.heatPort.Q_flow|conductionElement1.heatPort.T|conductionElement1.init|conductionElement1.initM_flow|der.conductionElement1.inlet.m_flow.|conductionElement1.inlet.m_flow|conductionElement1.inlet.r|conductionElement1.inlet.state.T|conductionElement1.inlet.state.d|conductionElement1.inlet.state.h|conductionElement1.inlet.state.p|conductionElement1.inlet.state.phase|conductionElement1.k|conductionElement1.k_internal|conductionElement1.k_par|conductionElement1.m_acceleration_0|conductionElement1.m_flow|conductionElement1.m_flowStateSelect|conductionElement1.m_flow_0|conductionElement1.m_flow_assert|conductionElement1.outlet.m_flow|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retizedHEX4.thermalElementB.3..outlet.state.T|discretizedHEX4.thermalElementB.3..outlet.state.d|discretizedHEX4.thermalElementB.3..outlet.state.h|discretizedHEX4.thermalElementB.3..outlet.state.p|discretizedHEX4.thermalElementB.3..outlet.state.phase|discretizedHEX4.thermalElementB.3..p_in|discretizedHEX4.thermalElementB.3..p_min|discretizedHEX4.thermalElementB.3..p_out|discretizedHEX4.thermalElementB.3..rho|discretizedHEX4.thermalElementB.3..rho_min|discretizedHEX4.thermalElementB.3..state.T|discretizedHEX4.thermalElementB.3..state.d|discretizedHEX4.thermalElementB.3..state.h|discretizedHEX4.thermalElementB.3..state.p|discretizedHEX4.thermalElementB.3..state.phase|discretizedHEX4.thermalElementB.3..x|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|dynamicPressureInflow.A|dynamicPressureInflow.A_par|dynamicPressureInflow.L|dynamicPressureInflow.clip_p_out|dynamicPressureInflow.delta_v|dynamicPressureInflow.dp|dynamicPressureInflow.dr_corr|dynamicPressureInflow.h_in|dynamicPressureInflow.h_out|dynamicPressureInflow.initM_flow|der.dynamicPressureInflow.inlet.m_flow.|dynamicPressureInflow.inlet.m_flow|dynamicPressureInflow.inlet.r|dynamicPressureInflow.inlet.state.T|dynamicPressureInflow.inlet.state.d|dynamicPressureInflow.inlet.state.h|dynamicPressureInflow.inlet.state.p|dynamicPressureInflow.inlet.state.phase|dynamicPressureInflow.m_acceleration_0|dynamicPressureInflow.m_flow|dynamicPressureInflow.m_flowStateSelect|dynamicPressureInflow.m_flow_0|dynamicPressureInflow.m_flow_reg|dynamicPressureInflow.outlet.m_flow|dynamicPressureInflow.outlet.r|dynamicPressureInflow.outlet.state.T|dynamicPressureInflow.outlet.state.d|dynamicPressureInflow.outlet.state.h|dynamicPressureInflow.outlet.state.p|dynamicPressureInflow.outlet.state.phase|dynamicPressureInflow.p_in|dynamicPressureInflow.p_min|dynamicPressureInflow.p_out|dynamicPressureInflow.rho_in|dynamicPressureInflow.rho_mean|dynamicPressureInflow.rho_out|dynamicPressureInflow.v_in|dynamicPressureInflow.v_in_par|dynamicPressureInflow.v_mean|dynamicPressureInflow.v_out|dynamicPressureOutflow.A|dynamicPressureOutflow.A_par|dynamicPressureOutflow.L|dynamicPressureOutflow.clip_p_out|dynamicPressureOutflow.delta_v|dynamicPressureOutflow.dp|dynamicPressureOutflow.dr_corr|dynamicPressureOutflow.extrapolateQuadratic|dynamicPressureOutflow.h_in|dynamicPressureOutflow.h_out|dynamicPressureOutflow.initM_flow|der.dynamicPressureOutflow.inlet.m_flow.|dynamicPressureOutflow.inlet.m_flow|dynamicPressureOutflow.inlet.r|dynamicPressureOutflow.inlet.state.T|dynamicPressureOutflow.inlet.state.d|dynamicPressureOutflow.inlet.state.h|dynamicPressureOutflow.inlet.state.p|dynamicPressureOutflow.inlet.state.phase|dynamicPressureOutflow.m_acceleration_0|dynamicPressureOutflow.m_flow|dynamicPressureOutflow.m_flowStateSelect|dynamicPressureOutflow.m_flow_0|dynamicPressureOutflow.m_flow_reg|dynamicPressureOutflow.outlet.m_flow|dynamicPressureOutflow.outlet.r|dynamicPressureOutflow.outlet.state.T|dynamicPressureOutflow.outlet.state.d|dynamicPressureOutflow.outlet.state.h|dynamicPressureOutflow.outlet.state.p|dynamicPressureOutflow.outlet.state.phase|dynamicPressureOutflow.p_in|dynamicPressureOutflow.p_min|dynamicPressureOutflow.p_out|dynamicPressureOutflow.rho_in|dynamicPressureOutflow.rho_mean|dynamicPressureOutflow.rho_out|dynamicPressureOutflow.v_in|dynamicPressureOutflow.v_mean|dynamicPressureOutflow.v_out|dynamicPressureOutflow.v_out_par|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|der.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|flowRes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dium.d|der.volumeFlex.medium.h.|der.volumeFlex.medium.p.|der.volumeFlex.medium.u.|volumeFlex.medium.h|volumeFlex.medium.p|volumeFlex.medium.p_bar|volumeFlex.medium.phase|volumeFlex.medium.preferredMediumStates|volumeFlex.medium.quality|volumeFlex.medium.sat.Tsat|volumeFlex.medium.sat.psat|volumeFlex.medium.standardOrderComponents|volumeFlex.medium.state.T|volumeFlex.medium.state.d|der.volumeFlex.medium.state.d.|volumeFlex.medium.state.h|volumeFlex.medium.state.p|volumeFlex.medium.state.phase|volumeFlex.medium.u|volumeFlex.outlet.m_flow|volumeFlex.outlet.r|volumeFlex.outlet.state.T|volumeFlex.outlet.state.d|volumeFlex.outlet.state.h|volumeFlex.outlet.state.p|volumeFlex.outlet.state.phase|volumeFlex.p_in|volumeFlex.p_ref|volumeFlex.p_start|volumeFlex.r|volumeFlex.r_damping|volumeFlex.r_in|volumeFlex.r_out|volumeFlex.state_in.T|volumeFlex.state_in.d|volumeFlex.state_in.h|volumeFlex.state_in.p|volumeFlex.state_in.phase|volumeFlex.state_out.T|volumeFlex.state_out.d|volumeFlex.state_out.h|volumeFlex.state_out.p|volumeFlex.state_out.phase",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia",simflags="-alarm=1200  -emit_protected -lv LOG_STATS")
simulate(ThermofluidStream.Media.Tests.TestXRGMedia,startTime=0,stopTime=10,tolerance=1e-06,numberOfIntervals=1000,outputFormat="mat",variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|NonlinearSystems.simulation.3..Calls|NonlinearSystems.simulation.3..Iterations|NonlinearSystems.simulation.3..Jacobians|NonlinearSystems.simulation.3..Residues|Time|basicControlValve.Cvs_UK|basicControlValve.Cvs_US|basicControlValve.Kvs|basicControlValve.L|basicControlValve.V_flow_ref|basicControlValve.clip_p_out|basicControlValve.dp|basicControlValve.dp_ref|basicControlValve.dr_corr|basicControlValve.flowCoefficient|basicControlValve.h_in|basicControlValve.h_out|basicControlValve.initM_flow|der.basicControlValve.inlet.m_flow.|basicControlValve.inlet.m_flow|basicControlValve.inlet.r|basicControlValve.inlet.state.T|basicControlValve.inlet.state.d|basicControlValve.inlet.state.h|basicControlValve.inlet.state.p|basicControlValve.inlet.state.phase|basicControlValve.k_min|basicControlValve.k_u|basicControlValve.m_acceleration_0|basicControlValve.m_flow|basicControlValve.m_flowStateSelect|basicControlValve.m_flow_0|basicControlValve.m_flow_ref|basicControlValve.m_flow_ref_set|basicControlValve.outlet.m_flow|basicControlValve.outlet.r|basicControlValve.outlet.state.T|basicControlValve.outlet.state.d|basicControlValve.outlet.state.h|basicControlValve.outlet.state.p|basicControlValve.outlet.state.phase|basicControlValve.p_in|basicControlValve.p_min|basicControlValve.p_out|basicControlValve.rho|basicControlValve.rho_ref|basicControlValve.secondsPerHour|basicControlValve.u|basicControlValve.u_in|conductionElement.A|conductionElement.L|conductionElement.M|conductionElement.Q_flow|conductionElement.T|conductionElement.T_0|conductionElement.T_e|conductionElement.T_heatPort|conductionElement.U|conductionElement.U_internal|conductionElement.V|conductionElement.clip_p_out|conductionElement.deltaE_system|der.conductionElement.h.|conductionElement.dp|conductionElement.dr_corr|conductionElement.h|conductionElement.h_0|conductionElement.h_in|conductionElement.h_in_norm|conductionElement.h_out|conductionElement.heatPort.Q_flow|conductionElement.heatPort.T|conductionElement.init|conductionElement.initM_flow|der.conductionElement.inlet.m_flow.|conductionElement.inlet.m_flow|conductionElement.inlet.r|conductionElement.inlet.state.T|conductionElement.inlet.state.d|conductionElement.inlet.state.h|conductionElement.inlet.state.p|conductionElement.inlet.state.phase|conductionElement.k|conductionElement.k_internal|conductionElement.k_par|conductionElement.m_acceleration_0|conductionElement.m_flow|conductionElement.m_flowStateSelect|conductionElement.m_flow_0|conductionElement.m_flow_assert|conductionElement.outlet.m_flow|conductionElement.outlet.r|conductionElement.outlet.state.T|conductionElement.outlet.state.d|conductionElement.outlet.state.h|conductionElement.outlet.state.p|conductionElement.outlet.state.phase|conductionElement.p_in|conductionElement.p_min|conductionElement.p_out|conductionElement.rho|conductionElement.rho_min|conductionElement.state.T|conductionElement.state.d|conductionElement.state.h|conductionElement.state.p|conductionElement.state.phase|conductionElement1.A|conductionElement1.L|conductionElement1.M|conductionElement1.Q_flow|conductionElement1.T|conductionElement1.T_0|conductionElement1.T_e|conductionElement1.T_heatPort|conductionElement1.U|conductionElement1.U_internal|conductionElement1.V|conductionElement1.clip_p_out|conductionElement1.deltaE_system|der.conductionElement1.h.|conductionElement1.dp|conductionElement1.dr_corr|conductionElement1.h|conductionElement1.h_0|conductionElement1.h_in|conductionElement1.h_in_norm|conductionElement1.h_out|conductionElement1.heatPort.Q_flow|conductionElement1.heatPort.T|conductionElement1.init|conductionElement1.initM_flow|der.conductionElement1.inlet.m_flow.|conductionElement1.inlet.m_flow|conductionElement1.inlet.r|conductionElement1.inlet.state.T|conductionElement1.inlet.state.d|conductionElement1.inlet.state.h|conductionElement1.inlet.state.p|conductionElement1.inlet.state.phase|conductionElement1.k|conductionElement1.k_internal|conductionElement1.k_par|conductionElement1.m_acceleration_0|conductionElement1.m_flow|conductionElement1.m_flowStateSelect|conductionElement1.m_flow_0|conductionElement1.m_flow_assert|conductionElement1.outlet.m_flow|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retizedHEX4.thermalElementB.3..outlet.state.T|discretizedHEX4.thermalElementB.3..outlet.state.d|discretizedHEX4.thermalElementB.3..outlet.state.h|discretizedHEX4.thermalElementB.3..outlet.state.p|discretizedHEX4.thermalElementB.3..outlet.state.phase|discretizedHEX4.thermalElementB.3..p_in|discretizedHEX4.thermalElementB.3..p_min|discretizedHEX4.thermalElementB.3..p_out|discretizedHEX4.thermalElementB.3..rho|discretizedHEX4.thermalElementB.3..rho_min|discretizedHEX4.thermalElementB.3..state.T|discretizedHEX4.thermalElementB.3..state.d|discretizedHEX4.thermalElementB.3..state.h|discretizedHEX4.thermalElementB.3..state.p|discretizedHEX4.thermalElementB.3..state.phase|discretizedHEX4.thermalElementB.3..x|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.1.|dropOfCommons.instanceNameColor.2.|dropOfCommons.instanceNameColor.3.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|dynamicPressureInflow.A|dynamicPressureInflow.A_par|dynamicPressureInflow.L|dynamicPressureInflow.clip_p_out|dynamicPressureInflow.delta_v|dynamicPressureInflow.dp|dynamicPressureInflow.dr_corr|dynamicPressureInflow.h_in|dynamicPressureInflow.h_out|dynamicPressureInflow.initM_flow|der.dynamicPressureInflow.inlet.m_flow.|dynamicPressureInflow.inlet.m_flow|dynamicPressureInflow.inlet.r|dynamicPressureInflow.inlet.state.T|dynamicPressureInflow.inlet.state.d|dynamicPressureInflow.inlet.state.h|dynamicPressureInflow.inlet.state.p|dynamicPressureInflow.inlet.state.phase|dynamicPressureInflow.m_acceleration_0|dynamicPressureInflow.m_flow|dynamicPressureInflow.m_flowStateSelect|dynamicPressureInflow.m_flow_0|dynamicPressureInflow.m_flow_reg|dynamicPressureInflow.outlet.m_flow|dynamicPressureInflow.outlet.r|dynamicPressureInflow.outlet.state.T|dynamicPressureInflow.outlet.state.d|dynamicPressureInflow.outlet.state.h|dynamicPressureInflow.outlet.state.p|dynamicPressureInflow.outlet.state.phase|dynamicPressureInflow.p_in|dynamicPressureInflow.p_min|dynamicPressureInflow.p_out|dynamicPressureInflow.rho_in|dynamicPressureInflow.rho_mean|dynamicPressureInflow.rho_out|dynamicPressureInflow.v_in|dynamicPressureInflow.v_in_par|dynamicPressureInflow.v_mean|dynamicPressureInflow.v_out|dynamicPressureOutflow.A|dynamicPressureOutflow.A_par|dynamicPressureOutflow.L|dynamicPressureOutflow.clip_p_out|dynamicPressureOutflow.delta_v|dynamicPressureOutflow.dp|dynamicPressureOutflow.dr_corr|dynamicPressureOutflow.extrapolateQuadratic|dynamicPressureOutflow.h_in|dynamicPressureOutflow.h_out|dynamicPressureOutflow.initM_flow|der.dynamicPressureOutflow.inlet.m_flow.|dynamicPressureOutflow.inlet.m_flow|dynamicPressureOutflow.inlet.r|dynamicPressureOutflow.inlet.state.T|dynamicPressureOutflow.inlet.state.d|dynamicPressureOutflow.inlet.state.h|dynamicPressureOutflow.inlet.state.p|dynamicPressureOutflow.inlet.state.phase|dynamicPressureOutflow.m_acceleration_0|dynamicPressureOutflow.m_flow|dynamicPressureOutflow.m_flowStateSelect|dynamicPressureOutflow.m_flow_0|dynamicPressureOutflow.m_flow_reg|dynamicPressureOutflow.outlet.m_flow|dynamicPressureOutflow.outlet.r|dynamicPressureOutflow.outlet.state.T|dynamicPressureOutflow.outlet.state.d|dynamicPressureOutflow.outlet.state.h|dynamicPressureOutflow.outlet.state.p|dynamicPressureOutflow.outlet.state.phase|dynamicPressureOutflow.p_in|dynamicPressureOutflow.p_min|dynamicPressureOutflow.p_out|dynamicPressureOutflow.rho_in|dynamicPressureOutflow.rho_mean|dynamicPressureOutflow.rho_out|dynamicPressureOutflow.v_in|dynamicPressureOutflow.v_mean|dynamicPressureOutflow.v_out|dynamicPressureOutflow.v_out_par|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|der.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|flowRes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nk4.inlet.m_flow|sink4.inlet.r|sink4.inlet.state.T|sink4.inlet.state.d|sink4.inlet.state.h|sink4.inlet.state.p|sink4.inlet.state.phase|sink4.p|sink4.p0|sink4.p0_par|sink4.r|source.L|source.T0|source.T0_par|source.h0|source.h0_par|der.source.outlet.m_flow.|source.outlet.m_flow|source.outlet.r|source.outlet.state.T|source.outlet.state.d|source.outlet.state.h|source.outlet.state.p|source.outlet.state.phase|source.p0|source.p0_par|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|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|splitterT2_1.L|splitterT2_1.inlet.m_flow|splitterT2_1.inlet.r|splitterT2_1.inlet.state.T|splitterT2_1.inlet.state.d|splitterT2_1.inlet.state.h|splitterT2_1.inlet.state.p|splitterT2_1.inlet.state.phase|splitterT2_1.outletA.m_flow|splitterT2_1.outletA.r|splitterT2_1.outletA.state.T|splitterT2_1.outletA.state.d|splitterT2_1.outletA.state.h|splitterT2_1.outletA.state.p|splitterT2_1.outletA.state.phase|splitterT2_1.outletB.m_flow|splitterT2_1.outletB.r|splitterT2_1.outletB.state.T|splitterT2_1.outletB.state.d|splitterT2_1.outletB.state.h|splitterT2_1.outletB.state.p|splitterT2_1.outletB.state.phase|splitterT2_1.splitterN.L|splitterT2_1.splitterN.N|der.splitterT2_1.splitterN.inlet.m_flow.|splitterT2_1.splitterN.inlet.m_flow|splitterT2_1.splitterN.inlet.r|splitterT2_1.splitterN.inlet.state.T|splitterT2_1.splitterN.inlet.state.d|splitterT2_1.splitterN.inlet.state.h|splitterT2_1.splitterN.inlet.state.p|splitterT2_1.splitterN.inlet.state.phase|der.splitterT2_1.splitterN.outlets.1..m_flow.|splitterT2_1.splitterN.outlets.1..m_flow|splitterT2_1.splitterN.outlets.1..r|splitterT2_1.splitterN.outlets.1..state.T|splitterT2_1.splitterN.outlets.1..state.d|splitterT2_1.splitterN.outlets.1..state.h|splitterT2_1.splitterN.outlets.1..state.p|splitterT2_1.splitterN.outlets.1..state.phase|der.splitterT2_1.splitterN.outlets.2..m_flow.|splitterT2_1.splitterN.outlets.2..m_flow|splitterT2_1.splitterN.outlets.2..r|splitterT2_1.splitterN.outlets.2..state.T|splitterT2_1.splitterN.outlets.2..state.d|splitterT2_1.splitterN.outlets.2..state.h|splitterT2_1.splitterN.outlets.2..state.p|splitterT2_1.splitterN.outlets.2..state.phase|splitterT2_1.splitterN.r_mix|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.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.1.|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|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|volumeFlex.A|volumeFlex.K|volumeFlex.L|volumeFlex.M|volumeFlex.Q_flow|volumeFlex.T_heatPort|volumeFlex.T_start|volumeFlex.U|volumeFlex.U_med|volumeFlex.V|volumeFlex.V_ref|volumeFlex.W_v|volumeFlex.d|volumeFlex.density_derp_h|der.volumeFlex.M.|der.volumeFlex.U_med.|der.volumeFlex.V.|der.volumeFlex.m_flow_in.|der.volumeFlex.m_flow_out.|volumeFlex.h_in|volumeFlex.h_out|volumeFlex.h_start|volumeFlex.inlet.m_flow|volumeFlex.inlet.r|volumeFlex.inlet.state.T|volumeFlex.inlet.state.d|volumeFlex.inlet.state.h|volumeFlex.inlet.state.p|volumeFlex.inlet.state.phase|volumeFlex.k_volume_damping|volumeFlex.m_flow_assert|volumeFlex.m_flow_in|volumeFlex.m_flow_out|volumeFlex.medium.MM|volumeFlex.medium.R_s|volumeFlex.medium.T|volumeFlex.medium.T_degC|volumeFlex.medium.X.1.|volumeFlex.medium.d|der.volumeFlex.medium.h.|der.volumeFlex.medium.p.|der.volumeFlex.medium.u.|volumeFlex.medium.h|volumeFlex.medium.p|volumeFlex.medium.p_bar|volumeFlex.medium.phase|volumeFlex.medium.preferredMediumStates|volumeFlex.medium.quality|volumeFlex.medium.sat.Tsat|volumeFlex.medium.sat.psat|volumeFlex.medium.standardOrderComponents|volumeFlex.medium.state.T|volumeFlex.medium.state.d|der.volumeFlex.medium.state.d.|volumeFlex.medium.state.h|volumeFlex.medium.state.p|volumeFlex.medium.state.phase|volumeFlex.medium.u|volumeFlex.outlet.m_flow|volumeFlex.outlet.r|volumeFlex.outlet.state.T|volumeFlex.outlet.state.d|volumeFlex.outlet.state.h|volumeFlex.outlet.state.p|volumeFlex.outlet.state.phase|volumeFlex.p_in|volumeFlex.p_ref|volumeFlex.p_start|volumeFlex.r|volumeFlex.r_damping|volumeFlex.r_in|volumeFlex.r_out|volumeFlex.state_in.T|volumeFlex.state_in.d|volumeFlex.state_in.h|volumeFlex.state_in.p|volumeFlex.state_in.phase|volumeFlex.state_out.T|volumeFlex.state_out.d|volumeFlex.state_out.h|volumeFlex.state_out.p|volumeFlex.state_out.phase",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia",simflags="-alarm=1200  -emit_protected -lv LOG_STATS") [Timeout 1860]
"Notification: Performance of FrontEnd - loaded program: time 9.32e-07/9.32e-07, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - Absyn->SCode: time 2.254e-05/2.347e-05, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instantiate(ThermofluidStream.Media.Tests.TestXRGMedia): time 1.213/1.213, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instExpressions: time 0.7739/1.987, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.updateImplicitVariability: time 0.01235/1.999, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeComponents: time 0.03499/2.034, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeBindings: time 0.2155/2.25, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeClassSections: time 0.2163/2.466, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.flatten: time 0.03542/2.501, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.resolveConnections: time 0.00977/2.511, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFEvalConstants.evaluate: time 0.457/2.968, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFSimplifyModel.simplify: time 0.03618/3.004, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFPackage.collectConstants: time 0.003736/3.008, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.collectFunctions: time 0.5837/3.592, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFScalarize.scalarize: time 0.01271/3.604, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFVerifyModel.verify: time 0.01965/3.624, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFConvertDAE.convert: time 0.824/4.448, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - DAE generated: time 0.01103/4.459, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd: time 5.821e-06/4.459, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Transformations before backend: time 0.0005903/4.46, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 2248
 * Number of variables: 2248
Notification: Performance of Generate backend data structure: time 0.4809/4.941, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare preOptimizeDAE: time 0.002269/4.943, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.07931/5.022, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evaluateParameters (simulation): time 0.04781/5.07, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.002228/5.072, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt expandDerOperator (simulation): time 0.00614/5.078, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt clockPartitioning (simulation): time 0.1087/5.187, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt findStateOrder (simulation): time 0.0004894/5.187, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.004165/5.192, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001386/5.193, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.1064/5.299, allocations: 0 / 0, free: 0 / 0
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 0.2181/5.518, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt comSubExp (simulation): time 0.0751/5.593, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt resolveLoops (simulation): time 0.03682/5.63, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evalFunc (simulation): time 0.2109/5.84, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0004993/5.841, allocations: 0 / 0, free: 0 / 0
Notification: Performance of pre-optimization done (n=1017): time 0.001869/5.843, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=1032): time 0.3654/6.208, allocations: 0 / 0, free: 0 / 0
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0005265/6.209, allocations: 0 / 0, free: 0 / 0
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.02634/6.235, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectPreVariables (initialization): time 0.005054/6.24, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialEqns (initialization): time 0.008399/6.248, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialBindings (initialization): time 0.007383/6.256, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simplifyInitialFunctions (initialization): time 0.01343/6.269, allocations: 0 / 0, free: 0 / 0
Notification: Performance of setup shared object (initialization): time 0.0002043/6.269, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preBalanceInitialSystem (initialization): time 0.03276/6.302, allocations: 0 / 0, free: 0 / 0
Notification: Performance of partitionIndependentBlocks (initialization): time 0.03792/6.34, allocations: 0 / 0, free: 0 / 0
Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: flowResistance8.m_flow = flowResistance8.m_flow_0 (discretizedHEX2.m_flow_0_B = flowResistance8.m_flow_0)
Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: discretizedHEX.inletA.m_flow = discretizedHEX.m_flow_0_A (discretizedHEX4.m_flow_0_B + discretizedHEX2.m_flow_0_B = discretizedHEX.m_flow_0_A)
Warning: It was not possible to determine if the initialization problem is consistent, because of not evaluable parameters/start values during compile time: discretizedHEX4.thermalElementA[3].deltaE_system = $START.discretizedHEX4.thermalElementA[3].deltaE_system (0.0 = $START.discretizedHEX4.thermalElementA[3].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: discretizedHEX4.thermalElementA[2].deltaE_system = $START.discretizedHEX4.thermalElementA[2].deltaE_system (0.0 = $START.discretizedHEX4.thermalElementA[2].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: discretizedHEX4.thermalElementA[1].deltaE_system = $START.discretizedHEX4.thermalElementA[1].deltaE_system (0.0 = $START.discretizedHEX4.thermalElementA[1].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: discretizedHEX4.thermalElementB[3].deltaE_system = $START.discretizedHEX4.thermalElementB[3].deltaE_system (0.0 = $START.discretizedHEX4.thermalElementB[3].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: discretizedHEX4.thermalElementB[2].deltaE_system = $START.discretizedHEX4.thermalElementB[2].deltaE_system (0.0 = $START.discretizedHEX4.thermalElementB[2].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: discretizedHEX4.thermalElementB[1].deltaE_system = $START.discretizedHEX4.thermalElementB[1].deltaE_system (0.0 = $START.discretizedHEX4.thermalElementB[1].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: discretizedHEX2.thermalElementA[3].deltaE_system = $START.discretizedHEX2.thermalElementA[3].deltaE_system (0.0 = $START.discretizedHEX2.thermalElementA[3].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: discretizedHEX2.thermalElementA[2].deltaE_system = $START.discretizedHEX2.thermalElementA[2].deltaE_system (0.0 = $START.discretizedHEX2.thermalElementA[2].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: discretizedHEX2.thermalElementA[1].deltaE_system = $START.discretizedHEX2.thermalElementA[1].deltaE_system (0.0 = $START.discretizedHEX2.thermalElementA[1].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: discretizedHEX2.thermalElementB[3].deltaE_system = $START.discretizedHEX2.thermalElementB[3].deltaE_system (0.0 = $START.discretizedHEX2.thermalElementB[3].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: discretizedHEX2.thermalElementB[2].deltaE_system = $START.discretizedHEX2.thermalElementB[2].deltaE_system (0.0 = $START.discretizedHEX2.thermalElementB[2].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: discretizedHEX2.thermalElementB[1].deltaE_system = $START.discretizedHEX2.thermalElementB[1].deltaE_system (0.0 = $START.discretizedHEX2.thermalElementB[1].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: discretizedHEX1.thermalElementA[3].deltaE_system = $START.discretizedHEX1.thermalElementA[3].deltaE_system (0.0 = $START.discretizedHEX1.thermalElementA[3].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: discretizedHEX1.thermalElementA[2].deltaE_system = $START.discretizedHEX1.thermalElementA[2].deltaE_system (0.0 = $START.discretizedHEX1.thermalElementA[2].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: discretizedHEX1.thermalElementA[1].deltaE_system = $START.discretizedHEX1.thermalElementA[1].deltaE_system (0.0 = $START.discretizedHEX1.thermalElementA[1].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: discretizedHEX1.thermalElementB[3].deltaE_system = $START.discretizedHEX1.thermalElementB[3].deltaE_system (0.0 = $START.discretizedHEX1.thermalElementB[3].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: discretizedHEX1.thermalElementB[2].deltaE_system = $START.discretizedHEX1.thermalElementB[2].deltaE_system (0.0 = $START.discretizedHEX1.thermalElementB[2].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: discretizedHEX1.thermalElementB[1].deltaE_system = $START.discretizedHEX1.thermalElementB[1].deltaE_system (0.0 = $START.discretizedHEX1.thermalElementB[1].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: discretizedHEX.thermalElementA[3].deltaE_system = $START.discretizedHEX.thermalElementA[3].deltaE_system (0.0 = $START.discretizedHEX.thermalElementA[3].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: discretizedHEX.thermalElementA[2].deltaE_system = $START.discretizedHEX.thermalElementA[2].deltaE_system (0.0 = $START.discretizedHEX.thermalElementA[2].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: discretizedHEX.thermalElementA[1].deltaE_system = $START.discretizedHEX.thermalElementA[1].deltaE_system (0.0 = $START.discretizedHEX.thermalElementA[1].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: discretizedHEX.thermalElementB[3].deltaE_system = $START.discretizedHEX.thermalElementB[3].deltaE_system (0.0 = $START.discretizedHEX.thermalElementB[3].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: discretizedHEX.thermalElementB[2].deltaE_system = $START.discretizedHEX.thermalElementB[2].deltaE_system (0.0 = $START.discretizedHEX.thermalElementB[2].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: discretizedHEX.thermalElementB[1].deltaE_system = $START.discretizedHEX.thermalElementB[1].deltaE_system (0.0 = $START.discretizedHEX.thermalElementB[1].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: conductionElement1.deltaE_system = $START.conductionElement1.deltaE_system (0.0 = $START.conductionElement1.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: conductionElement.deltaE_system = $START.conductionElement.deltaE_system (0.0 = $START.conductionElement.deltaE_system)
Notification: Performance of analyzeInitialSystem (initialization): time 0.462/6.802, allocations: 0 / 0, free: 0 / 0
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001753/6.802, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=1213) (initialization): time 0.1096/6.912, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare postOptimizeDAE: time 0.0002439/6.912, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.09498/7.007, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (initialization): time 0.04965/7.057, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.01835/7.075, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.119/7.194, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.01228/7.206, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.003921/7.21, allocations: 0 / 0, free: 0 / 0
Warning: The initial conditions are over specified. The following 28 initial equations are redundant, so they are removed from the initialization system:
         flowResistance8.m_flow = flowResistance8.m_flow_0
         discretizedHEX.inletA.m_flow = discretizedHEX.m_flow_0_A
         discretizedHEX4.thermalElementA[3].deltaE_system = $START.discretizedHEX4.thermalElementA[3].deltaE_system
         discretizedHEX4.thermalElementA[2].deltaE_system = $START.discretizedHEX4.thermalElementA[2].deltaE_system
         discretizedHEX4.thermalElementA[1].deltaE_system = $START.discretizedHEX4.thermalElementA[1].deltaE_system
         discretizedHEX4.thermalElementB[3].deltaE_system = $START.discretizedHEX4.thermalElementB[3].deltaE_system
         discretizedHEX4.thermalElementB[2].deltaE_system = $START.discretizedHEX4.thermalElementB[2].deltaE_system
         discretizedHEX4.thermalElementB[1].deltaE_system = $START.discretizedHEX4.thermalElementB[1].deltaE_system
         discretizedHEX2.thermalElementA[3].deltaE_system = $START.discretizedHEX2.thermalElementA[3].deltaE_system
         discretizedHEX2.thermalElementA[2].deltaE_system = $START.discretizedHEX2.thermalElementA[2].deltaE_system
         discretizedHEX2.thermalElementA[1].deltaE_system = $START.discretizedHEX2.thermalElementA[1].deltaE_system
         discretizedHEX2.thermalElementB[3].deltaE_system = $START.discretizedHEX2.thermalElementB[3].deltaE_system
         discretizedHEX2.thermalElementB[2].deltaE_system = $START.discretizedHEX2.thermalElementB[2].deltaE_system
         discretizedHEX2.thermalElementB[1].deltaE_system = $START.discretizedHEX2.thermalElementB[1].deltaE_system
         discretizedHEX1.thermalElementA[3].deltaE_system = $START.discretizedHEX1.thermalElementA[3].deltaE_system
         discretizedHEX1.thermalElementA[2].deltaE_system = $START.discretizedHEX1.thermalElementA[2].deltaE_system
         discretizedHEX1.thermalElementA[1].deltaE_system = $START.discretizedHEX1.thermalElementA[1].deltaE_system
         discretizedHEX1.thermalElementB[3].deltaE_system = $START.discretizedHEX1.thermalElementB[3].deltaE_system
         discretizedHEX1.thermalElementB[2].deltaE_system = $START.discretizedHEX1.thermalElementB[2].deltaE_system
         discretizedHEX1.thermalElementB[1].deltaE_system = $START.discretizedHEX1.thermalElementB[1].deltaE_system
         discretizedHEX.thermalElementA[3].deltaE_system = $START.discretizedHEX.thermalElementA[3].deltaE_system
         discretizedHEX.thermalElementA[2].deltaE_system = $START.discretizedHEX.thermalElementA[2].deltaE_system
         discretizedHEX.thermalElementA[1].deltaE_system = $START.discretizedHEX.thermalElementA[1].deltaE_system
         discretizedHEX.thermalElementB[3].deltaE_system = $START.discretizedHEX.thermalElementB[3].deltaE_system
         discretizedHEX.thermalElementB[2].deltaE_system = $START.discretizedHEX.thermalElementB[2].deltaE_system
         discretizedHEX.thermalElementB[1].deltaE_system = $START.discretizedHEX.thermalElementB[1].deltaE_system
         conductionElement1.deltaE_system = $START.conductionElement1.deltaE_system
         conductionElement.deltaE_system = $START.conductionElement.deltaE_system.
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 123
 * Number of states: 0 ()
 * Number of discrete variables: 77 (volumeFlex.medium.phase,volume.medium.phase,receiver.medium.phase,volume.state_in.phase,conductionElement1.state.phase,conductionElement1.outlet.state.phase,basicControlValve.outlet.state.phase,source3.outlet.state.phase,flowResistance7.outlet.state.phase,sink.inlet.state.phase,dynamicPressureOutflow.outlet.state.phase,source2.outlet.state.phase,splitterT2_1.splitterN.outlets[2].state.phase,junctionT2_1.outlet.state.phase,conductionElement.state.phase,flowResistance5.outlet.state.phase,flowResistance5.inlet.state.phase,flowResistance4.outlet.state.phase,receiver.outlet.state.phase,receiver.inlet.state.phase,volumeFlex.inlet.state.phase,source1.outlet.state.phase,sink2.inlet.state.phase,discretizedHEX4.outletA.state.phase,discretizedHEX4.inletA.state.phase,discretizedHEX4.outletB.state.phase,discretizedHEX4.inletB.state.phase,discretizedHEX4.thermalElementA[3].state.phase,discretizedHEX4.thermalElementA[2].state.phase,discretizedHEX4.thermalElementA[2].outlet.state.phase,discretizedHEX4.thermalElementA[1].state.phase,discretizedHEX4.thermalElementA[1].outlet.state.phase,discretizedHEX4.thermalElementB[3].state.phase,discretizedHEX4.thermalElementB[2].state.phase,discretizedHEX4.thermalElementB[2].outlet.state.phase,discretizedHEX4.thermalElementB[1].state.phase,discretizedHEX4.thermalElementB[1].outlet.state.phase,counterFlowNTU.outletB.state.phase,counterFlowNTU.inletB.state.phase,counterFlowNTU.outletA.state.phase,counterFlowNTU.inletA.state.phase,discretizedHEX2.inletA.state.phase,discretizedHEX2.thermalElementA[3].state.phase,discretizedHEX2.thermalElementA[2].state.phase,discretizedHEX2.thermalElementA[2].outlet.state.phase,discretizedHEX2.thermalElementA[1].state.phase,discretizedHEX2.thermalElementA[1].outlet.state.phase,discretizedHEX2.thermalElementB[3].state.phase,discretizedHEX2.thermalElementB[2].state.phase,discretizedHEX2.thermalElementB[2].outlet.state.phase,discretizedHEX2.thermalElementB[1].state.phase,discretizedHEX2.thermalElementB[1].outlet.state.phase,discretizedHEX1.outletA.state.phase,discretizedHEX1.inletA.state.phase,discretizedHEX1.outletB.state.phase,discretizedHEX1.thermalElementA[3].state.phase,discretizedHEX1.thermalElementA[2].state.phase,discretizedHEX1.thermalElementA[2].outlet.state.phase,discretizedHEX1.thermalElementA[1].state.phase,discretizedHEX1.thermalElementA[1].outlet.state.phase,discretizedHEX1.thermalElementB[3].state.phase,discretizedHEX1.thermalElementB[2].state.phase,discretizedHEX1.thermalElementB[2].outlet.state.phase,discretizedHEX1.thermalElementB[1].state.phase,discretizedHEX1.thermalElementB[1].outlet.state.phase,discretizedHEX.inletA.state.phase,discretizedHEX.outletB.state.phase,discretizedHEX.thermalElementA[3].state.phase,discretizedHEX.thermalElementA[2].state.phase,discretizedHEX.thermalElementA[2].outlet.state.phase,discretizedHEX.thermalElementA[1].state.phase,discretizedHEX.thermalElementA[1].outlet.state.phase,discretizedHEX.thermalElementB[3].state.phase,discretizedHEX.thermalElementB[2].state.phase,discretizedHEX.thermalElementB[2].outlet.state.phase,discretizedHEX.thermalElementB[1].state.phase,discretizedHEX.thermalElementB[1].outlet.state.phase)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (817):
 * Single equations (assignments): 719
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 73
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 2
 * Torn equation systems: 23
 * Mixed (continuous/discrete) equation systems: 0
Notification: Equation system details (not torn):
 * Constant Jacobian (size): 0 systems
 * Linear Jacobian (size,density): 0 systems
 * Non-linear Jacobian (size): 2 systems
   {1, 1}
 * Without analytic Jacobian (size): 0 systems
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 20 systems
   {(1,4,100.0%), (1,1,100.0%), (4,25,75.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,5,100.0%), (1,5,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,9,100.0%), (2,2,100.0%), (1,8,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 3 systems
   {(1,1), (2,2), (1,1)}
Notification: Performance of prepare postOptimizeDAE: time 0.02024/7.231, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01155/7.242, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1743/7.416, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inlineArrayEqn (simulation): time 0.1102/7.527, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt constantLinearSystem (simulation): time 0.000182/7.527, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.0002188/7.527, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.2081/7.735, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.1083/7.843, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.01804/7.862, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (simulation): time 0.02223/7.884, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 0.004099/7.888, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.1176/8.005, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 2.252e-05/8.005, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.1586/8.164, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeConstants (simulation): time 0.0596/8.224, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.006117/8.23, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.01166/8.241, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.01294/8.254, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 0.003633/8.258, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sorting global known variables: time 0.02094/8.279, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sort global known variables: time 0.0006639/8.28, allocations: 0 / 0, free: 0 / 0
Notification: Performance of remove unused functions: time 0.1901/8.47, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 20
 * Number of states: 42 (discretizedHEX.thermalElementB[1].h,discretizedHEX.thermalElementB[2].h,discretizedHEX.thermalElementB[3].h,discretizedHEX.thermalElementA[1].h,discretizedHEX.thermalElementA[2].h,discretizedHEX.thermalElementA[3].h,discretizedHEX1.thermalElementB[1].h,discretizedHEX1.thermalElementB[2].h,discretizedHEX1.thermalElementB[3].h,discretizedHEX1.thermalElementA[1].h,discretizedHEX1.thermalElementA[2].h,discretizedHEX1.thermalElementA[3].h,discretizedHEX2.thermalElementB[1].h,discretizedHEX2.thermalElementB[2].h,discretizedHEX2.thermalElementB[3].h,discretizedHEX2.thermalElementA[1].h,discretizedHEX2.thermalElementA[2].h,discretizedHEX2.thermalElementA[3].h,counterFlowNTU.h_out_A,counterFlowNTU.h_out_B,volume.M,volume.U_med,discretizedHEX4.thermalElementB[1].h,discretizedHEX4.thermalElementB[2].h,discretizedHEX4.thermalElementB[3].h,discretizedHEX4.thermalElementA[1].h,discretizedHEX4.thermalElementA[2].h,discretizedHEX4.thermalElementA[3].h,volumeFlex.M,volumeFlex.U_med,receiver.M,receiver.U_med,flowResistance1.inlet.m_flow,flowResistance2.inlet.m_flow,flowResistance3.inlet.m_flow,conductionElement.inlet.m_flow,conductionElement.h,flowResistance6.inlet.m_flow,conductionElement1.inlet.m_flow,conductionElement1.h,pump.m_flow,flowResistance8.inlet.m_flow)
 * Number of discrete variables: 212 (conductionElement1.outlet.state.phase,basicControlValve.outlet.state.phase,sink.inlet.state.phase,counterFlowNTU.outletA.state.phase,counterFlowNTU.inletA.state.phase,discretizedHEX4.outletA.state.phase,discretizedHEX4.thermalElementA[2].outlet.state.phase,discretizedHEX4.thermalElementA[1].outlet.state.phase,discretizedHEX4.inletA.state.phase,junctionT2_1.outlet.state.phase,flowResistance5.outlet.state.phase,flowResistance5.inlet.state.phase,receiver.outlet.state.phase,counterFlowNTU.inletB.state.phase,receiver.inlet.state.phase,discretizedHEX2.thermalElementB[2].outlet.state.phase,discretizedHEX2.thermalElementB[1].outlet.state.phase,counterFlowNTU.outletB.state.phase,discretizedHEX4.inletB.state.phase,discretizedHEX4.thermalElementB[2].outlet.state.phase,discretizedHEX4.outletB.state.phase,discretizedHEX4.thermalElementB[1].outlet.state.phase,flowResistance4.outlet.state.phase,sink2.inlet.state.phase,volumeFlex.inlet.state.phase,discretizedHEX2.thermalElementA[2].outlet.state.phase,discretizedHEX2.thermalElementA[1].outlet.state.phase,discretizedHEX2.inletA.state.phase,discretizedHEX.outletB.state.phase,discretizedHEX.thermalElementB[2].outlet.state.phase,discretizedHEX.thermalElementB[1].outlet.state.phase,discretizedHEX1.outletA.state.phase,discretizedHEX1.thermalElementA[2].outlet.state.phase,discretizedHEX1.thermalElementA[1].outlet.state.phase,discretizedHEX1.inletA.state.phase,discretizedHEX1.outletB.state.phase,discretizedHEX1.thermalElementB[2].outlet.state.phase,discretizedHEX1.thermalElementB[1].outlet.state.phase,discretizedHEX.thermalElementA[1].outlet.state.phase,discretizedHEX.thermalElementA[2].outlet.state.phase,splitterT2_1.splitterN.outlets[2].state.phase,$cse1.phase,$cse2,$cse4.phase,$cse5,$cse6.phase,$cse7,$cse8.phase,$cse9,$cse10.phase,$cse11,$cse12.phase,$cse13,$cse14.phase,$cse15,$cse18.phase,$cse19,$cse20.phase,$cse21,$cse22.phase,$cse23,$cse24.phase,$cse25,$cse26.phase,$cse27,$cse30.phase,$cse31,$cse36.phase,$cse37,$cse38.phase,$cse39,$cse40.phase,$cse41,$cse43.phase,$cse44,$cse46.phase,$cse47,$cse49.phase,$cse50,$cse51.phase,$cse52,$cse53.phase,$cse54,$cse55.phase,$cse56,$cse58.phase,$cse59,$cse61.phase,$cse62,$cse64.phase,$cse65,$cse66.phase,$cse67,$cse68.phase,$cse69,$cse70.phase,$cse71,$cse74.phase,$cse75,$cse78.phase,$cse79,$cse82.phase,$cse83,$cse84.phase,$cse85,$cse86.phase,$cse87,$cse88.phase,$cse89,$cse92.phase,$cse93,$cse96.phase,$cse97,$cse100.phase,$cse101,$cse102.phase,$cse104.phase,$cse106.phase,$cse107,$cse109.phase,$cse112.phase,$cse113.phase,$cse114.phase,$cse115.phase,$cse116.phase,$cse117,$cse118.phase,$cse119,$cse121.phase,$cse123.phase,$cse125.phase,$cse127.phase,$cse129.phase,$cse131.phase,$cse134.phase,$cse135,$cse136.phase,$cse137,$cse138.phase,$cse139,$cse140.phase,$cse141,$cse142.phase,$cse143,$cse144.phase,$cse145,$cse150.phase,$cse151,$cse153.phase,$cse154,$cse155.phase,$cse156,$cse157.phase,$cse158.phase,$cse161.phase,$cse162,$cse163.phase,$cse164,$cse165.phase,$cse166,$cse167.phase,$cse168,$cse169.phase,$cse170,$cse171.phase,$cse172,$cse177.phase,$cse178,$cse179.phase,$cse180,$cse181.phase,$cse182,$cse183.phase,$cse184,$cse187.phase,$cse188,$cse189.phase,$cse190,$cse191.phase,$cse192,$cse193.phase,$cse194,discretizedHEX.thermalElementB[1].state.phase,discretizedHEX.thermalElementB[2].state.phase,discretizedHEX.thermalElementB[3].state.phase,discretizedHEX.thermalElementA[1].state.phase,discretizedHEX.thermalElementA[2].state.phase,discretizedHEX.thermalElementA[3].state.phase,discretizedHEX1.thermalElementB[1].state.phase,discretizedHEX1.thermalElementB[2].state.phase,discretizedHEX1.thermalElementB[3].state.phase,discretizedHEX1.thermalElementA[1].state.phase,discretizedHEX1.thermalElementA[2].state.phase,discretizedHEX1.thermalElementA[3].state.phase,discretizedHEX2.thermalElementB[1].state.phase,discretizedHEX2.thermalElementB[2].state.phase,discretizedHEX2.thermalElementB[3].state.phase,discretizedHEX2.thermalElementA[1].state.phase,discretizedHEX2.thermalElementA[2].state.phase,discretizedHEX2.thermalElementA[3].state.phase,discretizedHEX4.thermalElementB[1].state.phase,discretizedHEX4.thermalElementB[2].state.phase,discretizedHEX4.thermalElementB[3].state.phase,discretizedHEX4.thermalElementA[1].state.phase,discretizedHEX4.thermalElementA[2].state.phase,discretizedHEX4.thermalElementA[3].state.phase,conductionElement.state.phase,dynamicPressureOutflow.outlet.state.phase,flowResistance7.outlet.state.phase,conductionElement1.state.phase,discretizedHEX.inletA.state.phase,source3.outlet.state.phase)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (965):
 * Single equations (assignments): 823
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 116
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 26
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 20 systems
   {(1,5,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (1,3,100.0%), (4,25,75.0%), (1,5,100.0%), (1,8,100.0%), (2,2,100.0%), (1,1,100.0%), (1,9,100.0%), (1,4,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 6 systems
   {(2,2), (1,1), (1,3), (2,4), (1,1), (1,3)}
Notification: Performance of Backend phase and start with SimCode phase: time 1.593/10.06, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created initialization part: time 0.1148/10.18, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created event and clocks part: time 4.898e-05/10.18, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created simulation system equations: time 0.0665/10.24, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.06283/10.31, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.1859/10.49, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0376/10.53, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: alias equations: time 0.04168/10.57, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.02721/10.6, allocations: 0 / 0, free: 0 / 0
Notification: Performance of SimCode: time 0.01581/10.62, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Templates: time 0.3874/11, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 1808]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Media.Tests.TestXRGMedia_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.initialization[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.initialization[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Calls in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Calls from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Iterations in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Iterations from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[1].Residues in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[1].Residues from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Calls in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Calls from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Iterations in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Iterations from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[2].Residues in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[2].Residues from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[3].Calls in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[3].Calls from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[3].Iterations in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[3].Iterations from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[3].Jacobians in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[3].Jacobians from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable NonlinearSystems.simulation[3].Residues in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable NonlinearSystems.simulation[3].Residues from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable flowResistance1.inlet.state.der(d) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable flowResistance1.inlet.state.der(d) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable junctionT2_1.junctionN.inlets[2].der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable junctionT2_1.junctionN.inlets[2].der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable pump.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable pump.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable receiver.der(m_flow_in) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable receiver.der(m_flow_in) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable receiver.medium.state.der(d) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable receiver.medium.state.der(d) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable sink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable sink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable sink2.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable sink2.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable sink3.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable sink3.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable sink4.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable sink4.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable source.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable source.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable source1.outlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable source1.outlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable volume.der(m_flow_in) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable volume.der(m_flow_in) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable volume.der(m_flow_out) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable volume.der(m_flow_out) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
Error: Could not read variable volumeFlex.medium.state.der(d) in file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat.
Warning: Get data of variable volumeFlex.medium.state.der(d) from file ThermofluidStream_dev_ThermofluidStream.Media.Tests.TestXRGMedia_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,NonlinearSystems.initialization[1].Calls,NonlinearSystems.initialization[1].Iterations,NonlinearSystems.initialization[1].Jacobians,NonlinearSystems.initialization[1].Residues,NonlinearSystems.initialization[2].Calls,NonlinearSystems.initialization[2].Iterations,NonlinearSystems.initialization[2].Jacobians,NonlinearSystems.initialization[2].Residues,NonlinearSystems.simulation[1].Calls,NonlinearSystems.simulation[1].Iterations,NonlinearSystems.simulation[1].Jacobians,NonlinearSystems.simulation[1].Residues,NonlinearSystems.simulation[2].Calls,NonlinearSystems.simulation[2].Iterations,NonlinearSystems.simulation[2].Jacobians,NonlinearSystems.simulation[2].Residues,NonlinearSystems.simulation[3].Calls,NonlinearSystems.simulation[3].Iterations,NonlinearSystems.simulation[3].Jacobians,NonlinearSystems.simulation[3].Residues,Time,basicControlValve.Cvs_UK,basicControlValve.Cvs_US,basicControlValve.Kvs,basicControlValve.L,basicControlValve.V_flow_ref,basicControlValve.clip_p_out,basicControlValve.dp,basicControlValve.dp_ref,basicControlValve.dr_corr,basicControlValve.flowCoefficient,basicControlValve.h_in,basicControlValve.h_out,basicControlValve.initM_flow,der(basicControlValve.inlet.m_flow),basicControlValve.inlet.m_flow,basicControlValve.inlet.r,basicControlValve.inlet.state.T,basicControlValve.inlet.state.d,basicControlValve.inlet.state.h,basicControlValve.inlet.state.p,basicControlValve.inlet.state.phase,basicControlValve.k_min,basicControlValve.k_u,basicControlValve.m_acceleration_0,basicControlValve.m_flow,basicControlValve.m_flowStateSelect,basicControlValve.m_flow_0,basicControlValve.m_flow_ref,basicControlValve.m_flow_ref_set,basicControlValve.outlet.m_flow,basicControlValve.outlet.r,basicControlValve.outlet.state.T,basicControlValve.outlet.state.d,basicControlValve.outlet.state.h,basicControlValve.outlet.state.p,basicControlValve.outlet.state.phase,basicControlValve.p_in,basicControlValve.p_min,basicControlValve.p_out,basicControlValve.rho,basicControlValve.rho_ref,basicControlValve.secondsPerHour,basicControlValve.u,basicControlValve.u_in,conductionElement.A,conductionElement.L,conductionElement.M,conductionElement.Q_flow,conductionElement.T,conductionElement.T_0,conductionElement.T_e,conductionElement.T_heatPort,conductionElement.U,conductionElement.U_internal,conductionElement.V,conductionElement.clip_p_out,conductionElement.deltaE_system,der(conductionElement.h),conductionElement.dp,conductionElement.dr_corr,conductionElement.h,conductionElement.h_0,conductionElement.h_in,conductionElement.h_in_norm,conductionElement.h_out,conductionElement.heatPort.Q_flow,conductionElement.heatPort.T,conductionElement.init,conductionElement.initM_flow,der(conductionElement.inlet.m_flow),conductionElement.inlet.m_flow,conductionElement.inlet.r,conductionElement.inlet.state.T,conductionElement.inlet.state.d,conductionElement.inlet.state.h,conductionElement.inlet.state.p,conductionElement.inlet.state.phase,conductionElement.k,conductionElement.k_internal,conductionElement.k_par,conductionElement.m_acceleration_0,conductionElement.m_flow,conductionElement.m_flowStateSelect,conductionElement.m_flow_0,conductionElement.m_flow_assert,conductionElement.outlet.m_flow,conductionElement.outlet.r,conductionElement.outlet.state.T,conductionElement.outlet.state.d,conductionElement.outlet.state.h,conductionElement.outlet.state.p,conductionElement.outlet.state.phase,conductionElement.p_in,conductionElement.p_min,conductionElement.p_out,conductionElement.rho,conductionElement.rho_min,conductionElement.state.T,conductionElement.state.d,conductionElement.state.h,conductionElement.state.p,conductionElement.state.phase,conductionElement1.A,conductionElement1.L,conductionElement1.M,conductionElement1.Q_flow,conductionElement1.T,conductionElement1.T_0,conductionElement1.T_e,conductionElement1.T_heatPort,conductionElement1.U,conductionElement1.U_internal,conductionElement1.V,conductionElement1.clip_p_out,conductionElement1.deltaE_system,der(conductionElement1.h),conductionElement1.dp,conductionElement1.dr_corr,conductionElement1.h,conductionElement1.h_0,conductionElement1.h_in,conductionElement1.h_in_norm,conductionElement1.h_out,conductionElement1.heatPort.Q_flow,conductionElement1.heatPort.T,conductionElement1.init,conductionElement1.initM_flow,der(conductionElement1.inlet.m_flow),conductionElement1.inlet.m_flow,conductionElement1.inlet.r,conductionElement1.inlet.state.T,conductionElement1.inlet.state.d,conductionElement1.inlet.state.h,conductionElement1.inlet.state.p,conductionElement1.inlet.state.phase,conductionElement1.k,conductionElement1.k_internal,conductionElement1.k_par,conductionElement1.m_acceleration_0,conductionElement1.m_flow,conductionElement1.m_flowStateSelect,conductionElement1.m_flow_0,conductionElement1.m_flow_assert,conductionElement1.outlet.m_flow,conductionElement1.outlet.r,conductionElement1.outlet.state.T,conductionElement1.outlet.state.d,conductionElement1.outlet.state.h,conductionElement1.outlet.state.p,conductionElement1.outlet.state.phase,conductionElement1.p_in,conductionElement1.p_min,conductionElement1.p_out,conductionElement1.rho,conductionElement1.rho_min,conductionElement1.state.T,conductionElement1.state.d,conductionElement1.state.h,conductionElement1.state.p,conductionElement1.state.phase,const.k,const.y,counterFlowNTU.A,counterFlowNTU.C_A,counterFlowNTU.C_B,counterFlowNTU.C_max,counterFlowNTU.C_min,counterFlowNTU.C_r,counterFlowNTU.Delta_T_max,counterFlowNTU.L,counterFlowNTU.NTU,counterFlowNTU.TC,counterFlowNTU.T_in_MediumA,counterFlowNTU.T_in_MediumB,counterFlowNTU.cpA_in,counterFlowNTU.cpA_out,counterFlowNTU.cpB_in,counterFlowNTU.cpB_out,counterFlowNTU.cp_A,counterFlowNTU.cp_B,der(counterFlowNTU.h_out_A),der(counterFlowNTU.h_out_B),der(counterFlowNTU.inletA_m_flow),der(counterFlowNTU.inletB_m_flow),counterFlowNTU.dh_A,counterFlowNTU.dh_B,counterFlowNTU.effectiveness,counterFlowNTU.eps,counterFlowNTU.h_in_A,counterFlowNTU.h_in_B,counterFlowNTU.h_out_A,counterFlowNTU.h_out_B,counterFlowNTU.inletA.m_flow,counterFlowNTU.inletA.r,counterFlowNTU.inletA.state.T,counterFlowNTU.inletA.state.d,counterFlowNTU.inletA.state.h,counterFlowNTU.inletA.state.p,counterFlowNTU.inletA.state.phase,counterFlowNTU.inletA_m_flow,counterFlowNTU.inletA_r,counterFlowNTU.inletA_state.T,counterFlowNTU.inletA_state.d,counterFlowNTU.inletA_state.h,counterFlowNTU.inletA_state.p,counterFlowNTU.inletA_state.phase,counterFlowNTU.inletB.m_flow,counterFlowNTU.inletB.r,counterFlowNTU.inletB.state.T,counterFlowNTU.inletB.state.d,counterFlowNTU.inletB.state.h,counterFlowNTU.inletB.state.p,counterFlowNTU.inletB.state.phase,counterFlowNTU.inletB_m_flow,counterFlowNTU.inletB_r,counterFlowNTU.inletB_state.T,counterFlowNTU.inletB_state.d,counterFlowNTU.inletB_state.h,counterFlowNTU.inletB_state.p,counterFlowNTU.inletB_state.phase,counterFlowNTU.k_NTU,counterFlowNTU.m_flow_A,counterFlowNTU.m_flow_B,counterFlowNTU.m_flow_reg,counterFlowNTU.outletA.m_flow,counterFlowNTU.outletA.r,counterFlowNTU.outletA.state.T,counterFlowNTU.outletA.state.d,counterFlowNTU.outletA.state.h,counterFlowNTU.outletA.state.p,counterFlowNTU.outletA.state.phase,counterFlowNTU.outletA_m_flow,counterFlowNTU.outletA_r,counterFlowNTU.outletA_state.T,counterFlowNTU.outletA_state.d,counterFlowNTU.outletA_state.h,counterFlowNTU.outletA_state.p,counterFlowNTU.outletA_state.phase,counterFlowNTU.outletB.m_flow,counterFlowNTU.outletB.r,counterFlowNTU.outletB.state.T,counterFlowNTU.outletB.state.d,counterFlowNTU.outletB.state.h,counterFlowNTU.outletB.state.p,counterFlowNTU.outletB.state.phase,counterFlowNTU.outletB_m_flow,counterFlowNTU.outletB_r,counterFlowNTU.outletB_state.T,counterFlowNTU.outletB_state.d,counterFlowNTU.outletB_state.h,counterFlowNTU.outletB_state.p,counterFlowNTU.outletB_state.phase,counterFlowNTU.p_A,counterFlowNTU.p_B,counterFlowNTU.q_flow,counterFlowNTU.q_flowA,counterFlowNTU.q_flowB,counterFlowNTU.q_max,counterFlowNTU.summary.Q_flow_A,counterFlowNTU.summary.Q_flow_B,counterFlowNTU.summary.Tin_A,counterFlowNTU.summary.Tin_B,counterFlowNTU.summary.Tout_A,counterFlowNTU.summary.Tout_B,counterFlowNTU.summary.dT_A,counterFlowNTU.summary.dT_B,counterFlowNTU.summary.dh_A,counterFlowNTU.summary.dh_B,counterFlowNTU.summary.efficiency,counterFlowNTU.summary.hin_A,counterFlowNTU.summary.hin_B,counterFlowNTU.summary.hout_A,counterFlowNTU.summary.hout_B,discretizedHEX.A,discretizedHEX.G,discretizedHEX.M_A,discretizedHEX.M_B,discretizedHEX.Q_flow_A,discretizedHEX.Q_flow_B,discretizedHEX.V_Hex,discretizedHEX.deltaE_system,discretizedHEX.inletA.m_flow,discretizedHEX.inletA.r,discretizedHEX.inletA.state.T,discretizedHEX.inletA.state.d,discretizedHEX.inletA.state.h,discretizedHEX.inletA.state.p,discretizedHEX.inletA.state.phase,discretizedHEX.inletA_m_flow,discretizedHEX.inletA_r,discretizedHEX.inletA_state.T,discretizedHEX.inletA_state.d,discretizedHEX.inletA_state.h,discretizedHEX.inletA_state.p,discretizedHEX.inletA_state.phase,discretizedHEX.inletB.m_flow,discretizedHEX.inletB.r,discretizedHEX.inletB.state.T,discretizedHEX.inletB.state.d,discretizedHEX.inletB.state.h,discretizedHEX.inletB.state.p,discretizedHEX.inletB.state.phase,discretizedHEX.inletB_m_flow,discretizedHEX.inletB_r,discretizedHEX.inletB_state.T,discretizedHEX.inletB_state.d,discretizedHEX.inletB_state.h,discretizedHEX.inletB_state.p,discretizedHEX.inletB_state.phase,discretizedHEX.k_wall,discretizedHEX.m_flow_0_A,discretizedHEX.m_flow_0_B,discretizedHEX.m_flow_assert,discretizedHEX.nCells,discretizedHEX.nCellsParallel,discretizedHEX.outletA.m_flow,discretizedHEX.outletA.r,discretizedHEX.outletA.state.T,discretizedHEX.outletA.state.d,discretizedHEX.outletA.state.h,discretizedHEX.outletA.state.p,discretizedHEX.outletA.state.phase,discretizedHEX.outletA_m_flow,discretizedHEX.outletA_r,discretizedHEX.outletA_state.T,discretizedHEX.outletA_state.d,discretizedHEX.outletA_state.h,discretizedHEX.outletA_state.p,discretizedHEX.outletA_state.phase,discretizedHEX.outletB.m_flow,discretized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_color,flowResistance6.dr_corr,flowResistance6.h_in,flowResistance6.h_out,flowResistance6.initM_flow,der(flowResistance6.inlet.m_flow),flowResistance6.inlet.m_flow,flowResistance6.inlet.r,flowResistance6.inlet.state.T,flowResistance6.inlet.state.d,flowResistance6.inlet.state.h,flowResistance6.inlet.state.p,flowResistance6.inlet.state.phase,flowResistance6.l,flowResistance6.m_acceleration_0,flowResistance6.m_flow,flowResistance6.m_flowStateSelect,flowResistance6.m_flow_0,flowResistance6.mu_in,flowResistance6.outlet.m_flow,flowResistance6.outlet.r,flowResistance6.outlet.state.T,flowResistance6.outlet.state.d,flowResistance6.outlet.state.h,flowResistance6.outlet.state.p,flowResistance6.outlet.state.phase,flowResistance6.p_in,flowResistance6.p_min,flowResistance6.p_out,flowResistance6.perimeter,flowResistance6.perimeterInput,flowResistance6.phi,flowResistance6.pressureDropSignificantDigits,flowResistance6.r,flowResistance6.rho_in,flowResistance6.rho_min,flowResistance6.shape,flowResistance7.D_h,flowResistance7.L,flowResistance7.L_value,flowResistance7.a,flowResistance7.areaCross,flowResistance7.areaCrossInput,flowResistance7.areaHydraulic,flowResistance7.b,flowResistance7.clip_p_out,flowResistance7.dp,flowResistance7.dp_ref_color,flowResistance7.dr_corr,flowResistance7.h_in,flowResistance7.h_out,flowResistance7.initM_flow,der(flowResistance7.inlet.m_flow),flowResistance7.inlet.m_flow,flowResistance7.inlet.r,flowResistance7.inlet.state.T,flowResistance7.inlet.state.d,flowResistance7.inlet.state.h,flowResistance7.inlet.state.p,flowResistance7.inlet.state.phase,flowResistance7.l,flowResistance7.m_acceleration_0,flowResistance7.m_flow,flowResistance7.m_flowStateSelect,flowResistance7.m_flow_0,flowResistance7.mu_in,flowResistance7.outlet.m_flow,flowResistance7.outlet.r,flowResistance7.outlet.state.T,flowResistance7.outlet.state.d,flowResistance7.outlet.state.h,flowResistance7.outlet.state.p,flowResistance7.outlet.state.phase,flowResistance7.p_in,flowResistance7.p_min,flowResistance7.p_out,flowResistance7.perimeter,flowResistance7.perimeterInput,flowResistance7.phi,flowResistance7.pressureDropSignificantDigits,flowResistance7.r,flowResistance7.rho_in,flowResistance7.rho_min,flowResistance7.shape,flowResistance8.D_h,flowResistance8.L,flowResistance8.L_value,flowResistance8.a,flowResistance8.areaCross,flowResistance8.areaCrossInput,flowResistance8.areaHydraulic,flowResistance8.b,flowResistance8.clip_p_out,flowResistance8.dp,flowResistance8.dp_ref_color,flowResistance8.dr_corr,flowResistance8.h_in,flowResistance8.h_out,flowResistance8.initM_flow,der(flowResistance8.inlet.m_flow),flowResistance8.inlet.m_flow,flowResistance8.inlet.r,flowResistance8.inlet.state.T,flowResistance8.inlet.state.d,flowResistance8.inlet.state.h,flowResistance8.inlet.state.p,flowResistance8.inlet.state.phase,flowResistance8.l,flowResistance8.m_acceleration_0,flowResistance8.m_flow,flowResistance8.m_flowStateSelect,flowResistance8.m_flow_0,flowResistance8.mu_in,flowResistance8.outlet.m_flow,flowResistance8.outlet.r,flowResistance8.outlet.state.T,flowResistance8.outlet.state.d,flowResistance8.outlet.state.h,flowResistance8.outlet.state.p,flowResistance8.outlet.state.phase,flowResistance8.p_in,flowResistance8.p_min,flowResistance8.p_out,flowResistance8.perimeter,flowResistance8.perimeterInput,flowResistance8.phi,flowResistance8.pressureDropSignificantDigits,flowResistance8.r,flowResistance8.rho_in,flowResistance8.rho_min,flowResistance8.shape,junctionT2_1.L,junctionT2_1.inletA.m_flow,junctionT2_1.inletA.r,junctionT2_1.inletA.state.T,junctionT2_1.inletA.state.d,junctionT2_1.inletA.state.h,junctionT2_1.inletA.state.p,junctionT2_1.inletA.state.phase,junctionT2_1.inletB.m_flow,junctionT2_1.inletB.r,junctionT2_1.inletB.state.T,junctionT2_1.inletB.state.d,junctionT2_1.inletB.state.h,junctionT2_1.inletB.state.p,junctionT2_1.inletB.state.phase,junctionT2_1.junctionN.L,junctionT2_1.junctionN.N,junctionT2_1.junctionN.h[1],junctionT2_1.junctionN.h[2],junctionT2_1.junctionN.h_mix,der(junctionT2_1.junctionN.inlets[1].m_flow),junctionT2_1.junctionN.inlets[1].m_flow,junctionT2_1.junctionN.inlets[1].r,junctionT2_1.junctionN.inlets[1].state.T,junctionT2_1.junctionN.inlets[1].state.d,junctionT2_1.junctionN.inlets[1].state.h,junctionT2_1.junctionN.inlets[1].state.p,junctionT2_1.junctionN.inlets[1].state.phase,der(junctionT2_1.junctionN.inlets[2].m_flow),junctionT2_1.junctionN.inlets[2].m_flow,junctionT2_1.junctionN.inlets[2].r,junctionT2_1.junctionN.inlets[2].state.T,junctionT2_1.junctionN.inlets[2].state.d,junctionT2_1.junctionN.inlets[2].state.h,junctionT2_1.junctionN.inlets[2].state.p,junctionT2_1.junctionN.inlets[2].state.phase,junctionT2_1.junctionN.m_flow_eps,der(junctionT2_1.junctionN.outlet.m_flow),junctionT2_1.junctionN.outlet.m_flow,junctionT2_1.junctionN.outlet.r,junctionT2_1.junctionN.outlet.state.T,junctionT2_1.junctionN.outlet.state.d,junctionT2_1.junctionN.outlet.state.h,junctionT2_1.junctionN.outlet.state.p,junctionT2_1.junctionN.outlet.state.phase,jun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.p,sink4.p0,sink4.p0_par,sink4.r,source.L,source.T0,source.T0_par,source.h0,source.h0_par,der(source.outlet.m_flow),source.outlet.m_flow,source.outlet.r,source.outlet.state.T,source.outlet.state.d,source.outlet.state.h,source.outlet.state.p,source.outlet.state.phase,source.p0,source.p0_par,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,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,splitterT2_1.L,splitterT2_1.inlet.m_flow,splitterT2_1.inlet.r,splitterT2_1.inlet.state.T,splitterT2_1.inlet.state.d,splitterT2_1.inlet.state.h,splitterT2_1.inlet.state.p,splitterT2_1.inlet.state.phase,splitterT2_1.outletA.m_flow,splitterT2_1.outletA.r,splitterT2_1.outletA.state.T,splitterT2_1.outletA.state.d,splitterT2_1.outletA.state.h,splitterT2_1.outletA.state.p,splitterT2_1.outletA.state.phase,splitterT2_1.outletB.m_flow,splitterT2_1.outletB.r,splitterT2_1.outletB.state.T,splitterT2_1.outletB.state.d,splitterT2_1.outletB.state.h,splitterT2_1.outletB.state.p,splitterT2_1.outletB.state.phase,splitterT2_1.splitterN.L,splitterT2_1.splitterN.N,der(splitterT2_1.splitterN.inlet.m_flow),splitterT2_1.splitterN.inlet.m_flow,splitterT2_1.splitterN.inlet.r,splitterT2_1.splitterN.inlet.state.T,splitterT2_1.splitterN.inlet.state.d,splitterT2_1.splitterN.inlet.state.h,splitterT2_1.splitterN.inlet.state.p,splitterT2_1.splitterN.inlet.state.phase,der(splitterT2_1.splitterN.outlets[1].m_flow),splitterT2_1.splitterN.outlets[1].m_flow,splitterT2_1.splitterN.outlets[1].r,splitterT2_1.splitterN.outlets[1].state.T,splitterT2_1.splitterN.outlets[1].state.d,splitterT2_1.splitterN.outlets[1].state.h,splitterT2_1.splitterN.outlets[1].state.p,splitterT2_1.splitterN.outlets[1].state.phase,der(splitterT2_1.splitterN.outlets[2].m_flow),splitterT2_1.splitterN.outlets[2].m_flow,splitterT2_1.splitterN.outlets[2].r,splitterT2_1.splitterN.outlets[2].state.T,splitterT2_1.splitterN.outlets[2].state.d,splitterT2_1.splitterN.outlets[2].state.h,splitterT2_1.splitterN.outlets[2].state.p,splitterT2_1.splitterN.outlets[2].state.phase,splitterT2_1.splitterN.r_mix,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.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[1],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,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,volumeFlex.A,volumeFlex.K,volumeFlex.L,volumeFlex.M,volumeFlex.Q_flow,volumeFlex.T_heatPort,volumeFlex.T_start,volumeFlex.U,volumeFlex.U_med,volumeFlex.V,volumeFlex.V_ref,volumeFlex.W_v,volumeFlex.d,volumeFlex.density_derp_h,der(volumeFlex.M),der(volumeFlex.U_med),der(volumeFlex.V),der(volumeFlex.m_flow_in),der(volumeFlex.m_flow_out),volumeFlex.h_in,volumeFlex.h_out,volumeFlex.h_start,volumeFlex.inlet.m_flow,volumeFlex.inlet.r,volumeFlex.inlet.state.T,volumeFlex.inlet.state.d,volumeFlex.inlet.state.h,volumeFlex.inlet.state.p,volumeFlex.inlet.state.phase,volumeFlex.k_volume_damping,volumeFlex.m_flow_assert,volumeFlex.m_flow_in,volumeFlex.m_flow_out,volumeFlex.medium.MM,volumeFlex.medium.R_s,volumeFlex.medium.T,volumeFlex.medium.T_degC,volumeFlex.medium.X[1],volumeFlex.medium.d,der(volumeFlex.medium.h),der(volumeFlex.medium.p),der(volumeFlex.medium.u),volumeFlex.medium.h,volumeFlex.medium.p,volumeFlex.medium.p_bar,volumeFlex.medium.phase,volumeFlex.medium.preferredMediumStates,volumeFlex.medium.quality,volumeFlex.medium.sat.Tsat,volumeFlex.medium.sat.psat,volumeFlex.medium.standardOrderComponents,volumeFlex.medium.state.T,volumeFlex.medium.state.d,der(volumeFlex.medium.state.d),volumeFlex.medium.state.h,volumeFlex.medium.state.p,volumeFlex.medium.state.phase,volumeFlex.medium.u,volumeFlex.outlet.m_flow,volumeFlex.outlet.r,volumeFlex.outlet.state.T,volumeFlex.outlet.state.d,volumeFlex.outlet.state.h,volumeFlex.outlet.state.p,volumeFlex.outlet.state.phase,volumeFlex.p_in,volumeFlex.p_ref,volumeFlex.p_start,volumeFlex.r,volumeFlex.r_damping,volumeFlex.r_in,volumeFlex.r_out,volumeFlex.state_in.T,volumeFlex.state_in.d,volumeFlex.state_in.h,volumeFlex.state_in.p,volumeFlex.state_in.phase,volumeFlex.state_out.T,volumeFlex.state_out.d,volumeFlex.state_out.h,volumeFlex.state_out.p,volumeFlex.state_out.phase

Variables in the result:basicControlValve.Cvs_UK,basicControlValve.Cvs_US,basicControlValve.Kvs,basicControlValve.L,basicControlValve.V_flow_ref,basicControlValve.clip_p_out,basicControlValve.dp,basicControlValve.dp_ref,basicControlValve.dr_corr,basicControlValve.flowCoefficient,basicControlValve.h_in,basicControlValve.h_out,basicControlValve.initM_flow,basicControlValve.inlet.m_flow,basicControlValve.inlet.r,basicControlValve.inlet.state.T,basicControlValve.inlet.state.d,basicControlValve.inlet.state.h,basicControlValve.inlet.state.p,basicControlValve.inlet.state.phase,basicControlValve.k_min,basicControlValve.k_u,basicControlValve.m_acceleration_0,basicControlValve.m_flow,basicControlValve.m_flowStateSelect,basicControlValve.m_flow_0,basicControlValve.m_flow_ref,basicControlValve.m_flow_ref_set,basicControlValve.outlet.m_flow,basicControlValve.outlet.r,basicControlValve.outlet.state.T,basicControlValve.outlet.state.d,basicControlValve.outlet.state.h,basicControlValve.outlet.state.p,basicControlValve.outlet.state.phase,basicControlValve.p_in,basicControlValve.p_min,basicControlValve.p_out,basicControlValve.rho,basicControlValve.rho_ref,basicControlValve.secondsPerHour,basicControlValve.u,basicControlValve.u_in,conductionElement.A,conductionElement.L,conductionElement.M,conductionElement.Q_flow,conductionElement.T,conductionElement.T_0,conductionElement.T_e,conductionElement.T_heatPort,conductionElement.U,conductionElement.U_internal,conductionElement.V,conductionElement.clip_p_out,conductionElement.deltaE_system,conductionElement.dp,conductionElement.dr_corr,conductionElement.h,conductionElement.h_0,conductionElement.h_in,conductionElement.h_in_norm,conductionElement.h_out,conductionElement.heatPort.Q_flow,conductionElement.heatPort.T,conductionElement.init,conductionElement.initM_flow,conductionElement.inlet.m_flow,conductionElement.inlet.r,conductionElement.inlet.state.T,conductionElement.inlet.state.d,conductionElement.inlet.state.h,conductionElement.inlet.state.p,conductionElement.inlet.state.phase,conductionElement.k,conductionElement.k_internal,conductionElement.k_par,conductionElement.m_acceleration_0,conductionElement.m_flow,conductionElement.m_flowStateSelect,conductionElement.m_flow_0,conductionElement.m_flow_assert,conductionElement.outlet.m_flow,conductionElement.outlet.r,conductionElement.outlet.state.T,conductionElement.outlet.state.d,conductionElement.outlet.state.h,conductionElement.outlet.state.p,conductionElement.outlet.state.phase,conductionElement.p_in,conductionElement.p_min,conductionElement.p_out,conductionElement.rho,conductionElement.rho_min,conductionElement.state.T,conductionElement.state.d,conductionElement.state.h,conductionElement.state.p,conductionElement.state.phase,conductionElement1.A,conductionElement1.L,conductionElement1.M,conductionElement1.Q_flow,conductionElement1.T,conductionElement1.T_0,conductionElement1.T_e,conductionElement1.T_heatPort,conductionElement1.U,conductionElement1.U_internal,conductionElement1.V,conductionElement1.clip_p_out,conductionElement1.deltaE_system,conductionElement1.dp,conductionElement1.dr_corr,conductionElement1.h,conductionElement1.h_0,conductionElement1.h_in,conductionElement1.h_in_norm,conductionElement1.h_out,conductionElement1.heatPort.Q_flow,conductionElement1.heatPort.T,conductionElement1.init,conductionElement1.initM_flow,conductionElement1.inlet.m_flow,conductionElement1.inlet.r,conductionElement1.inlet.state.T,conductionElement1.inlet.state.d,conductionElement1.inlet.state.h,conductionElement1.inlet.state.p,conductionElement1.inlet.state.phase,conductionElement1.k,conductionElement1.k_internal,conductionElement1.k_par,conductionElement1.m_acceleration_0,conductionElement1.m_flow,conductionElement1.m_flowStateSelect,conductionElement1.m_flow_0,conductionElement1.m_flow_assert,conductionElement1.outlet.m_flow,conductionElement1.outlet.r,conductionElement1.outlet.state.T,conductionElement1.outlet.state.d,conductionElement1.outlet.state.h,conductionElement1.outlet.state.p,conductionElement1.outlet.state.phase,conductionElement1.p_in,conductionElement1.p_min,conductionElement1.p_out,conductionElement1.rho,conductionElement1.rho_min,conductionElement1.state.T,conductionElement1.state.d,conductionElement1.state.h,conductionElement1.state.p,conductionElement1.state.phase,const.k,const.y,counterFlowNTU.A,counterFlowNTU.C_A,counterFlowNTU.C_B,counterFlowNTU.C_max,counterFlowNTU.C_min,counterFlowNTU.C_r,counterFlowNTU.Delta_T_max,counterFlowNTU.L,counterFlowNTU.NTU,counterFlowNTU.TC,counterFlowNTU.T_in_MediumA,counterFlowNTU.T_in_MediumB,counterFlowNTU.cpA_in,counterFlowNTU.cpA_out,counterFlowNTU.cpB_in,counterFlowNTU.cpB_out,counterFlowNTU.cp_A,counterFlowNTU.cp_B,counterFlowNTU.dh_A,counterFlowNTU.dh_B,counterFlowNTU.effectiveness,counterFlowNTU.eps,counterFlowNTU.h_in_A,counterFlowNTU.h_in_B,counterFlowNTU.h_out_A,counterFlowNTU.h_out_B,counterFlowNTU.inletA.m_flow,counterFlowNTU.inletA.r,counterFlowNTU.inletA.state.T,counterFlowNTU.inletA.state.d,counterFlowNTU.inletA.state.h,counterFlowNTU.inletA.state.p,counterFlowNTU.inletA.state.phase,counterFlowNTU.inletA_m_flow,counterFlowNTU.inletA_r,counterFlowNTU.inletA_state.T,counterFlowNTU.inletA_state.d,counterFlowNTU.inletA_state.h,counterFlowNTU.inletA_state.p,counterFlowNTU.inletA_state.phase,counterFlowNTU.inletB.m_flow,counterFlowNTU.inletB.r,counterFlowNTU.inletB.state.T,counterFlowNTU.inletB.state.d,counterFlowNTU.inletB.state.h,counterFlowNTU.inletB.state.p,counterFlowNTU.inletB.state.phase,counterFlowNTU.inletB_m_flow,counterFlowNTU.inletB_r,counterFlowNTU.inletB_state.T,counterFlowNTU.inletB_state.d,counterFlowNTU.inletB_state.h,counterFlowNTU.inletB_state.p,counterFlowNTU.inletB_state.phase,counterFlowNTU.k_NTU,counterFlowNTU.m_flow_A,counterFlowNTU.m_flow_B,counterFlowNTU.m_flow_reg,counterFlowNTU.outletA.m_flow,counterFlowNTU.outletA.r,counterFlowNTU.outletA.state.T,counterFlowNTU.outletA.state.d,counterFlowNTU.outletA.state.h,counterFlowNTU.outletA.state.p,counterFlowNTU.outletA.state.phase,counterFlowNTU.outletA_m_flow,counterFlowNTU.outletA_r,counterFlowNTU.outletA_state.T,counterFlowNTU.outletA_state.d,counterFlowNTU.outletA_state.h,counterFlowNTU.outletA_state.p,counterFlowNTU.outletA_state.phase,counterFlowNTU.outletB.m_flow,counterFlowNTU.outletB.r,counterFlowNTU.outletB.state.T,counterFlowNTU.outletB.state.d,counterFlowNTU.outletB.state.h,counterFlowNTU.outletB.state.p,counterFlowNTU.outletB.state.phase,counterFlowNTU.outletB_m_flow,counterFlowNTU.outletB_r,counterFlowNTU.outletB_state.T,counterFlowNTU.outletB_state.d,counterFlowNTU.outletB_state.h,counterFlowNTU.outletB_state.p,counterFlowNTU.outletB_state.phase,counterFlowNTU.p_A,counterFlowNTU.p_B,counterFlowNTU.q_flow,counterFlowNTU.q_flowA,counterFlowNTU.q_flowB,counterFlowNTU.q_max,counterFlowNTU.summary.Q_flow_A,counterFlowNTU.summary.Q_flow_B,counterFlowNTU.summary.Tin_A,counterFlowNTU.summary.Tin_B,counterFlowNTU.summary.Tout_A,counterFlowNTU.summary.Tout_B,counterFlowNTU.summary.dT_A,counterFlowNTU.summary.dT_B,counterFlowNTU.summary.dh_A,counterFlowNTU.summary.dh_B,counterFlowNTU.summary.efficiency,counterFlowNTU.summary.hin_A,counterFlowNTU.summary.hin_B,counterFlowNTU.summary.hout_A,counterFlowNTU.summary.hout_B,der(conductionElement.h),der(conductionElement.inlet.m_flow),der(conductionElement1.h),der(conductionElement1.inlet.m_flow),der(counterFlowNTU.h_out_A),der(counterFlowNTU.h_out_B),der(discretizedHEX.thermalElementA[1].h),der(discretizedHEX.thermalElementA[2].h),der(discretizedHEX.thermalElementA[3].h),der(discretizedHEX.thermalElementA[3].inlet.m_flow),der(discretizedHEX.thermalElementB[1].h),der(discretizedHEX.thermalElementB[2].h),der(discretizedHEX.thermalElementB[3].h),der(discretizedHEX1.thermalElementA[1].h),der(discretizedHEX1.thermalElementA[2].h),der(discretizedHEX1.thermalElementA[3].h),der(discretizedHEX1.thermalElementB[1].h),der(discretizedHEX1.thermalElementB[2].h),der(discretizedHEX1.thermalElementB[3].h),der(discretizedHEX2.thermalElementA[1].h),der(discretizedHEX2.thermalElementA[2].h),der(discretizedHEX2.thermalElementA[3].h),der(discretizedHEX2.thermalElementB[1].h),der(discretizedHEX2.thermalElementB[2].h),der(discretizedHEX2.thermalElementB[3].h),der(discretizedHEX4.thermalElementA[1].h),der(discretizedHEX4.thermalElementA[2].h),der(discretizedHEX4.thermalElementA[3].h),der(discretizedHEX4.thermalElementB[1].h),der(discretizedHEX4.thermalElementB[2].h),der(discretizedHEX4.thermalElementB[3].h),der(flowResistance1.inlet.m_flow),der(flowResistance2.inlet.m_flow),der(flowResistance3.inlet.m_flow),der(flowResistance6.inlet.m_flow),der(flowResistance8.inlet.m_flow),der(junctionT2_1.junctionN.outlet.m_flow),der(pump.m_flow),der(receiver.M),der(receiver.U_med),der(receiver.medium.h),der(receiver.medium.p),der(receiver.medium.u),der(volume.M),der(volume.U_med),der(volume.medium.h),der(volume.medium.p),der(volume.medium.u),der(volumeFlex.M),der(volumeFlex.U_med),der(volumeFlex.V),der(volumeFlex.medium.h),der(volumeFlex.medium.p),der(volumeFlex.medium.u),discretizedHEX.A,discretizedHEX.G,discretizedHEX.M_A,discretizedHEX.M_B,discretizedHEX.Q_flow_A,discretizedHEX.Q_flow_B,discretizedHEX.V_Hex,discretizedHEX.deltaE_system,discretizedHEX.inletA.m_flow,discretizedHEX.inletA.r,discretizedHEX.inletA.state.T,discretizedHEX.inletA.state.d,discretizedHEX.inletA.state.h,discretizedHEX.inletA.state.p,discretizedHEX.inletA.state.phase,discretizedHEX.inletA_m_flow,discretizedHEX.inletA_r,discretizedHEX.inletA_state.T,discretizedHEX.inletA_state.d,discretizedHEX.inletA_state.h,discretizedHEX.inletA_state.p,discretizedHEX.inletA_state.phase,discretizedHEX.inletB.m_flow,discretizedHEX.inletB.r,discretizedHEX.inletB.state.T,discretizedHEX.inletB.state.d,discretizedHEX.inletB.state.h,discretizedHEX.inletB.state.p,discretizedHEX.inletB.state.phase,discretizedHEX.inletB_m_flow,discretizedHEX.inletB_r,discretizedHEX.inletB_state.T,discretizedHEX.inletB_state.d,discretizedHEX.inletB_state.h,discretizedHEX.inletB_state.p,discretizedHEX.inletB_state.phase,discretizedHEX.k_wall,discretizedHEX.m_flow_0_A,discretizedHEX.m_flow_0_B,discretizedHEX.m_flow_assert,discretizedHEX.nCells,discretizedHEX.nCellsParallel,discretizedHEX.outletA.m_flow,discretizedHEX.outletA.r,discretizedHEX.outletA.state.T,discretizedHEX.outletA.state.d,discretizedHEX.outletA.state.h,discretizedHEX.outletA.state.p,discretizedHEX.outletA.state.phase,discretizedHEX.outletA_m_flow,discretizedHEX.outletA_r,discretizedHEX.outletA_state.T,discretizedHEX.outletA_state.d,discretizedHEX.outletA_state.h,discretizedHEX.outletA_state.p,discretizedHEX.outletA_state.phase,discretizedHEX.outletB.m_flow,discretizedHEX.outletB.r,discretizedHEX.outletB.state.T,discretizedHEX.outletB.state.d,discretizedHEX.outletB.state.h,discretizedHEX.outletB.state.p,discretizedHEX.outletB.state.phase,discretizedHEX.outletB_m_flow,discretizedHEX.outletB_r,discretizedHEX.outletB_state.T,discretizedHEX.outletB_state.d,discretizedHEX.outletB_state.h,discretizedHEX.outletB_state.p,discretizedHEX.outletB_state.phase,discretizedHEX.summary.Q_flow_A,discretizedHEX.summary.Q_flow_B,discretizedHEX.summary.Tin_A,discretizedHEX.summary.Tin_B,discretizedHEX.summary.Tout_A,discretizedHEX.summary.Tout_B,discretizedHEX.summary.dT_A,discretizedHEX.summary.dT_B,discretizedHEX.summary.dh_A,discretizedHEX.summary.dh_B,discretizedHEX.summary.efficiency,discretizedHEX.summary.hin_A,discretizedHEX.summary.hin_B,discretizedHEX.summary.hout_A,discretizedHEX.summary.hout_B,discretizedHEX.thermalConductor[1].G,discretizedHEX.thermalConductor[1].Q_flow,discretizedHEX.thermalConductor[1].dT,discretizedHEX.thermalConductor[1].port_a.Q_flow,discretizedHEX.thermalConductor[1].port_a.T,discretizedHEX.thermalConductor[1].port_b.Q_flow,discretizedHEX.thermalConductor[1].port_b.T,discretizedHEX.thermalConductor[2].G,discretizedHEX.thermalConductor[2].Q_flow,discretizedHEX.thermalConductor[2].dT,discretizedHEX.thermalConductor[2].port_a.Q_flow,discretizedHEX.thermalConductor[2].port_a.T,discretizedHEX.thermalConductor[2].port_b.Q_flow,discretizedHEX.thermalConductor[2].port_b.T,discretizedHEX.thermalConductor[3].G,discretizedHEX.thermalConductor[3].Q_flow,discretizedHEX.thermalConductor[3].dT,discretizedHEX.thermalConductor[3].port_a.Q_flow,discretizedHEX.thermalConductor[3].port_a.T,discretizedHEX.thermalConductor[3].port_b.Q_flow,discretizedHEX.thermalConductor[3].port_b.T,discretizedHEX.thermalElementA[1].A,discretizedHEX.thermalElementA[1].L,discretizedHEX.thermalElementA[1].M,discretizedHEX.thermalElementA[1].Q_flow,discretizedHEX.thermalElementA[1].Re_exp,discretizedHEX.thermalElementA[1].T,discretizedHEX.thermalElementA[1].T_0,discretizedHEX.thermalElementA[1].T_e,discretizedHEX.thermalElementA[1].T_heatPort,discretizedHEX.thermalElementA[1].U,discretizedHEX.thermalElementA[1].U_min,discretizedHEX.thermalElementA[1].U_nom,discretizedHEX.thermalElementA[1].V,discretizedHEX.thermalElementA[1].clip_p_out,discretizedHEX.thermalElementA[1].deltaE_system,discretizedHEX.thermalElementA[1].dp,discretizedHEX.thermalElementA[1].dr_corr,discretizedHEX.thermalElementA[1].h,discretizedHEX.thermalElementA[1].h_0,discretizedHEX.thermalElementA[1].h_in,discretizedHEX.thermalElementA[1].h_in_norm,discretizedHEX.thermalElementA[1].h_out,discretizedHEX.thermalElementA[1].heatPort.Q_flow,discretizedHEX.thermalElementA[1].heatPort.T,discretizedHEX.thermalElementA[1].init,discretizedHEX.thermalElementA[1].initM_flow,discretizedHEX.thermalElementA[1].inlet.m_flow,discretizedHEX.thermalElementA[1].inlet.r,discretizedHEX.thermalElementA[1].inlet.state.T,discretizedHEX.thermalElementA[1].inlet.state.d,discretizedHEX.thermalElementA[1].inlet.state.h,discretizedHEX.thermalElementA[1].inlet.state.p,discretizedHEX.thermalElementA[1].inlet.state.phase,discretizedHEX.thermalElementA[1].k,discretizedHEX.thermalElementA[1].m_acceleration_0,discretizedHEX.thermalElementA[1].m_flow,discretizedHEX.thermalElementA[1].m_flowStateSelect,discretizedHEX.thermalElementA[1].m_flow_0,discretizedHEX.thermalElementA[1].m_flow_assert,discretizedHEX.thermalElementA[1].m_flow_nom,discretizedHEX.thermalElementA[1].nCellsParallel,discretizedHEX.thermalElementA[1].outlet.m_flow,discretizedHEX.thermalElementA[1].outlet.r,discretizedHEX.thermalElementA[1].outlet.state.T,discretizedHEX.thermalElementA[1].outlet.state.d,discretizedHEX.thermalElementA[1].outlet.state.h,discretizedHEX.thermalElementA[1].outlet.state.p,discretizedHEX.thermalElementA[1].outlet.state.phase,discretizedHEX.thermalElementA[1].p_in,discretizedHEX.thermalElementA[1].p_min,discretizedHEX.thermalElementA[1].p_out,discretizedHEX.thermalElementA[1].rho,discretizedHEX.thermalElementA[1].rho_min,discretizedHEX.thermalElementA[1].state.T,discretizedHEX.thermalElementA[1].state.d,discretizedHEX.thermalElementA[1].state.h,discretizedHEX.thermalElementA[1].state.p,discretizedHEX.thermalElementA[1].state.phase,discretizedHEX.thermalElementA[2].A,discretizedHEX.thermalElementA[2].L,discretizedHEX.thermalElementA[2].M,d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[Calling sys.exit(0), Time elapsed: 54.14022957000088]