startTime=0
stopTime=10
tolerance=1e-06
numberOfIntervals=1000
stepSize=0.01
wasm-jit simulation: 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|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.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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_ThermofluidStream.Media.Tests.TestXRGMedia",simflags="-alarm=1200  -emit_protected -lv LOG_STATS")
LOG_SUCCESS       | info    | The initialization finished successfully without homotopy method.
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/FlowControl/Internal/PartialValve.mo:33:3-33:137:writable]
|                 | |       | The following assertion has been violated at time 5.500000
|                 | |       | ((ramp.y <= 1.0 and ramp.y >= 0.0)) --> "In "TestXRGMedia.basicControlValve": Actuator signal out of valid range [0,1]"
LOG_STATS         | info    | ### STATISTICS ###
LOG_STATS         | info    | events
LOG_STATS         | info    | |       2 state events
LOG_STATS         | info    | |       0 time events
LOG_STATS         | info    | solver: dassl-events
LOG_STATS         | info    | |     797 steps taken
LOG_STATS         | info    | |    1064 calls of functionODE
LOG_STATS         | info    | |      83 evaluations of jacobian
LOG_STATS         | info    | |      36 error test failures
LOG_STATS         | info    | |       0 convergence test failures
LOG_STATS         | info    | |   68120 linear system solves
LOG_SUCCESS       | info    | The simulation finished successfully.