Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0008139/0.0008139, allocations: 80.25 kB / 20.04 MB, free: 4.488 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo): time 0.000779/0.000779, allocations: 173.9 kB / 23.34 MB, free: 1.184 MB / 18.57 MB
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo): time 0.8876/0.8876, allocations: 177.1 MB / 203.7 MB, free: 5.711 MB / 186.7 MB
"
[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 0.6285/0.6285, allocations: 116 MB / 376.1 MB, free: 4.16 MB / 346.7 MB
"
[Timeout remaining time 179]
Using package ThermofluidStream with version 1.3.0 (/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: translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|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|efficiency.displayVariablefinal|efficiency.showNumber|efficiency.significantDigits|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dp_ref_color|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.d|flowResistance.inlet.state.h|flowResistance.inlet.state.p|flowResistance.inlet.state.phase|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.d|flowResistance.outlet.state.h|flowResistance.outlet.state.p|flowResistance.outlet.state.phase|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.phi|flowResistance.pressureDropSignificantDigits|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|steamGenerator.L|steamGenerator.P|steamGenerator.Q_flow|steamGenerator.T_out_fixed|steamGenerator.assertionLevel|steamGenerator.clip_p_out|steamGenerator.dT|steamGenerator.dT_fixed|steamGenerator.dh|steamGenerator.dh_fixed|steamGenerator.dp|steamGenerator.dr_corr|steamGenerator.du|steamGenerator.h_in|steamGenerator.h_out|steamGenerator.h_out_fixed|steamGenerator.initM_flow|der.steamGenerator.inlet.m_flow.|steamGenerator.inlet.m_flow|steamGenerator.inlet.r|steamGenerator.inlet.state.T|steamGenerator.inlet.state.d|steamGenerator.inlet.state.h|steamGenerator.inlet.state.p|steamGenerator.inlet.state.phase|steamGenerator.m_acceleration_0|steamGenerator.m_flow|steamGenerator.m_flowStateSelect|steamGenerator.m_flow_0|steamGenerator.outlet.m_flow|steamGenerator.outlet.r|steamGenerator.outlet.state.T|steamGenerator.outlet.state.d|steamGenerator.outlet.state.h|steamGenerator.outlet.state.p|steamGenerator.outlet.state.phase|steamGenerator.outletSpec|steamGenerator.outletSpec_actual|steamGenerator.outletValueSpec|steamGenerator.p|steamGenerator.p_in|steamGenerator.p_inf|steamGenerator.p_min|steamGenerator.p_out|steamGenerator.q|steamGenerator.rho_in|steamGenerator.rho_out|steamGenerator.singularityRegime|steamGenerator.systemSpec|steamGenerator.u_in|steamGenerator.u_out|steamGenerator.v_in|steamGenerator.v_out|steamGenerator.w_amb|steamGenerator.w_exp|steamGenerator.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|waterSink.L|der.waterSink.inlet.m_flow.|waterSink.inlet.m_flow|waterSink.inlet.r|waterSink.inlet.state.T|waterSink.inlet.state.d|waterSink.inlet.state.h|waterSink.inlet.state.p|waterSink.inlet.state.phase|waterSink.p|waterSink.p0|waterSink.p0_par|waterSink.r|waterSource.L|waterSource.T0|waterSource.T0_par|waterSource.h0|waterSource.h0_par|der.waterSource.outlet.m_flow.|waterSource.outlet.m_flow|waterSource.outlet.r|waterSource.outlet.state.T|waterSource.outlet.state.d|waterSource.outlet.state.h|waterSource.outlet.state.p|waterSource.outlet.state.phase|waterSource.p0|waterSource.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop")
translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop,tolerance=1e-06,outputFormat="mat",numberOfIntervals=100,variableFilter="CPUtime|EventCounter|Time|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|efficiency.displayVariablefinal|efficiency.showNumber|efficiency.significantDigits|flowResistance.D_h|flowResistance.L|flowResistance.L_value|flowResistance.a|flowResistance.areaCross|flowResistance.areaCrossInput|flowResistance.areaHydraulic|flowResistance.b|flowResistance.clip_p_out|flowResistance.dp|flowResistance.dp_ref_color|flowResistance.dr_corr|flowResistance.h_in|flowResistance.h_out|flowResistance.initM_flow|der.flowResistance.inlet.m_flow.|flowResistance.inlet.m_flow|flowResistance.inlet.r|flowResistance.inlet.state.T|flowResistance.inlet.state.d|flowResistance.inlet.state.h|flowResistance.inlet.state.p|flowResistance.inlet.state.phase|flowResistance.l|flowResistance.m_acceleration_0|flowResistance.m_flow|flowResistance.m_flowStateSelect|flowResistance.m_flow_0|flowResistance.mu_in|flowResistance.outlet.m_flow|flowResistance.outlet.r|flowResistance.outlet.state.T|flowResistance.outlet.state.d|flowResistance.outlet.state.h|flowResistance.outlet.state.p|flowResistance.outlet.state.phase|flowResistance.p_in|flowResistance.p_min|flowResistance.p_out|flowResistance.perimeter|flowResistance.perimeterInput|flowResistance.phi|flowResistance.pressureDropSignificantDigits|flowResistance.r|flowResistance.rho_in|flowResistance.rho_min|flowResistance.shape|pump.L|pump.P|pump.P_nom|pump.TC|pump.adiabaticModel.eta_is|pump.adiabaticModel.h_in|pump.adiabaticModel.h_out|pump.adiabaticModel.h_out_is|pump.adiabaticModel.p_out|pump.adiabaticModel.s_in|pump.adiabaticModel.state_in.T|pump.adiabaticModel.state_in.d|pump.adiabaticModel.state_in.h|pump.adiabaticModel.state_in.p|pump.adiabaticModel.state_in.phase|pump.adiabaticModel.w_t|pump.adiabaticModel.w_t_is|pump.assertionLevel|pump.clip_p_out|pump.dh|pump.dp|pump.dp_fixed|pump.dp_nom|pump.dp_start|pump.dr_corr|pump.etaSpec|pump.eta_actual|pump.eta_fixed|pump.eta_is|pump.h_in|pump.h_out|pump.initM_flow|der.pump.inlet.m_flow.|pump.inlet.m_flow|pump.inlet.r|pump.inlet.state.T|pump.inlet.state.d|pump.inlet.state.h|pump.inlet.state.p|pump.inlet.state.phase|pump.m_acceleration_0|pump.m_flow|pump.m_flowStateSelect|pump.m_flow_0|pump.outlet.m_flow|pump.outlet.r|pump.outlet.state.T|pump.outlet.state.d|pump.outlet.state.h|pump.outlet.state.p|pump.outlet.state.phase|pump.outletSpec|pump.outletSpec_actual|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|steamGenerator.L|steamGenerator.P|steamGenerator.Q_flow|steamGenerator.T_out_fixed|steamGenerator.assertionLevel|steamGenerator.clip_p_out|steamGenerator.dT|steamGenerator.dT_fixed|steamGenerator.dh|steamGenerator.dh_fixed|steamGenerator.dp|steamGenerator.dr_corr|steamGenerator.du|steamGenerator.h_in|steamGenerator.h_out|steamGenerator.h_out_fixed|steamGenerator.initM_flow|der.steamGenerator.inlet.m_flow.|steamGenerator.inlet.m_flow|steamGenerator.inlet.r|steamGenerator.inlet.state.T|steamGenerator.inlet.state.d|steamGenerator.inlet.state.h|steamGenerator.inlet.state.p|steamGenerator.inlet.state.phase|steamGenerator.m_acceleration_0|steamGenerator.m_flow|steamGenerator.m_flowStateSelect|steamGenerator.m_flow_0|steamGenerator.outlet.m_flow|steamGenerator.outlet.r|steamGenerator.outlet.state.T|steamGenerator.outlet.state.d|steamGenerator.outlet.state.h|steamGenerator.outlet.state.p|steamGenerator.outlet.state.phase|steamGenerator.outletSpec|steamGenerator.outletSpec_actual|steamGenerator.outletValueSpec|steamGenerator.p|steamGenerator.p_in|steamGenerator.p_inf|steamGenerator.p_min|steamGenerator.p_out|steamGenerator.q|steamGenerator.rho_in|steamGenerator.rho_out|steamGenerator.singularityRegime|steamGenerator.systemSpec|steamGenerator.u_in|steamGenerator.u_out|steamGenerator.v_in|steamGenerator.v_out|steamGenerator.w_amb|steamGenerator.w_exp|steamGenerator.w_exp_net|turbine.L|turbine.P|turbine.P_nom|turbine.TC|turbine.adiabaticModel.eta_is|turbine.adiabaticModel.h_in|turbine.adiabaticModel.h_out|turbine.adiabaticModel.h_out_is|turbine.adiabaticModel.p_out|turbine.adiabaticModel.s_in|turbine.adiabaticModel.state_in.T|turbine.adiabaticModel.state_in.d|turbine.adiabaticModel.state_in.h|turbine.adiabaticModel.state_in.p|turbine.adiabaticModel.state_in.phase|turbine.adiabaticModel.w_t|turbine.adiabaticModel.w_t_is|turbine.assertionLevel|turbine.clip_p_out|turbine.dh|turbine.dp|turbine.dp_fixed|turbine.dp_nom|turbine.dp_start|turbine.dr_corr|turbine.etaSpec|turbine.eta_actual|turbine.eta_fixed|turbine.eta_is|turbine.h_in|turbine.h_out|turbine.initM_flow|der.turbine.inlet.m_flow.|turbine.inlet.m_flow|turbine.inlet.r|turbine.inlet.state.T|turbine.inlet.state.d|turbine.inlet.state.h|turbine.inlet.state.p|turbine.inlet.state.phase|turbine.m_acceleration_0|turbine.m_flow|turbine.m_flowStateSelect|turbine.m_flow_0|turbine.outlet.m_flow|turbine.outlet.r|turbine.outlet.state.T|turbine.outlet.state.d|turbine.outlet.state.h|turbine.outlet.state.p|turbine.outlet.state.phase|turbine.outletSpec|turbine.outletSpec_actual|turbine.outletValueSpec|turbine.pRatio|turbine.pRatio_fixed|turbine.p_in|turbine.p_min|turbine.p_out|turbine.p_out_fixed|turbine.singularityRegime|waterSink.L|der.waterSink.inlet.m_flow.|waterSink.inlet.m_flow|waterSink.inlet.r|waterSink.inlet.state.T|waterSink.inlet.state.d|waterSink.inlet.state.h|waterSink.inlet.state.p|waterSink.inlet.state.phase|waterSink.p|waterSink.p0|waterSink.p0_par|waterSink.r|waterSource.L|waterSource.T0|waterSource.T0_par|waterSource.h0|waterSource.h0_par|der.waterSource.outlet.m_flow.|waterSource.outlet.m_flow|waterSource.outlet.r|waterSource.outlet.state.T|waterSource.outlet.state.d|waterSource.outlet.state.h|waterSource.outlet.state.p|waterSource.outlet.state.phase|waterSource.p0|waterSource.p0_par",fileNamePrefix="ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.232e-06/1.232e-06, allocations: 0 / 0.5547 GB, free: 12.71 MB / 490.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 3.059e-05/3.182e-05, allocations: 2.312 kB / 0.5547 GB, free: 12.71 MB / 490.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop): time 0.03196/0.03199, allocations: 50.93 MB / 0.6045 GB, free: 9.598 MB / 0.5261 GB
Notification: Performance of NFInst.instExpressions: time 0.01557/0.04756, allocations: 19.25 MB / 0.6233 GB, free: 6.285 MB / 0.5417 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0006183/0.04818, allocations: 43.56 kB / 0.6233 GB, free: 6.242 MB / 0.5417 GB
Notification: Performance of NFTyping.typeComponents: time 0.0009804/0.04916, allocations: 492.4 kB / 0.6238 GB, free: 5.758 MB / 0.5417 GB
Notification: Performance of NFTyping.typeBindings: time 0.0138/0.06296, allocations: 7.271 MB / 0.6309 GB, free: 14.46 MB / 0.5573 GB
Notification: Performance of NFTyping.typeClassSections: time 0.002167/0.06512, allocations: 1.205 MB / 0.6321 GB, free: 13.25 MB / 0.5573 GB
Notification: Performance of NFFlatten.flatten: time 0.001254/0.06638, allocations: 1.431 MB / 0.6335 GB, free: 11.8 MB / 0.5573 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0002221/0.0666, allocations: 127.3 kB / 0.6336 GB, free: 11.67 MB / 0.5573 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.004262/0.07086, allocations: 3.975 MB / 0.6375 GB, free: 7.641 MB / 0.5573 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0003869/0.07125, allocations: 366.8 kB / 0.6378 GB, free: 7.281 MB / 0.5573 GB
Notification: Performance of NFPackage.collectConstants: time 5.694e-05/0.0713, allocations: 60 kB / 0.6379 GB, free: 7.223 MB / 0.5573 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.2613/0.3326, allocations: 10.29 MB / 0.6479 GB, free: 24.59 MB / 0.5573 GB
Notification: Performance of NFScalarize.scalarize: time 0.0002069/0.3328, allocations: 157.8 kB / 0.6481 GB, free: 24.59 MB / 0.5573 GB
Notification: Performance of NFVerifyModel.verify: time 0.0004478/0.3333, allocations: 310.3 kB / 0.6484 GB, free: 24.59 MB / 0.5573 GB
Notification: Performance of NFConvertDAE.convert: time 0.01614/0.3494, allocations: 8.793 MB / 0.657 GB, free: 24.46 MB / 0.5573 GB
Notification: Performance of FrontEnd - DAE generated: time 6.563e-06/0.3494, allocations: 3.938 kB / 0.657 GB, free: 24.46 MB / 0.5573 GB
Notification: Performance of FrontEnd: time 1.773e-06/0.3494, allocations: 0 / 0.657 GB, free: 24.46 MB / 0.5573 GB
Notification: Performance of Transformations before backend: time 1.902e-05/0.3494, allocations: 0 / 0.657 GB, free: 24.46 MB / 0.5573 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 173
 * Number of variables: 173
Notification: Performance of Generate backend data structure: time 0.005386/0.3548, allocations: 2.079 MB / 0.659 GB, free: 23.41 MB / 0.5573 GB
Notification: Performance of prepare preOptimizeDAE: time 4.98e-05/0.3549, allocations: 7.781 kB / 0.659 GB, free: 23.41 MB / 0.5573 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.000661/0.3555, allocations: 226.2 kB / 0.6592 GB, free: 23.36 MB / 0.5573 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0007745/0.3563, allocations: 0.6462 MB / 0.6599 GB, free: 23.12 MB / 0.5573 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 9.71e-05/0.3564, allocations: 158.7 kB / 0.66 GB, free: 22.99 MB / 0.5573 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 6.178e-05/0.3565, allocations: 78.2 kB / 0.6601 GB, free: 22.98 MB / 0.5573 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.001031/0.3575, allocations: 0.8011 MB / 0.6609 GB, free: 22.85 MB / 0.5573 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.775e-05/0.3575, allocations: 1.969 kB / 0.6609 GB, free: 22.85 MB / 0.5573 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 3.689e-05/0.3576, allocations: 28.47 kB / 0.6609 GB, free: 22.85 MB / 0.5573 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.773e-05/0.3576, allocations: 17.44 kB / 0.6609 GB, free: 22.85 MB / 0.5573 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0009051/0.3585, allocations: 0.5847 MB / 0.6615 GB, free: 22.84 MB / 0.5573 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.002399/0.3609, allocations: 2.435 MB / 0.6639 GB, free: 21.61 MB / 0.5573 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.000927/0.3618, allocations: 499.3 kB / 0.6643 GB, free: 21.58 MB / 0.5573 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0002622/0.3621, allocations: 180.1 kB / 0.6645 GB, free: 21.57 MB / 0.5573 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.05996/0.422, allocations: 35.03 MB / 0.6987 GB, free: 13.84 MB / 0.5573 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 4.088e-05/0.4221, allocations: 38.75 kB / 0.6988 GB, free: 13.8 MB / 0.5573 GB
Notification: Performance of pre-optimization done (n=47): time 3.366e-06/0.4221, allocations: 1.969 kB / 0.6988 GB, free: 13.8 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=47): time 0.001625/0.4237, allocations: 0.8222 MB / 0.6996 GB, free: 13.15 MB / 0.5573 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 1.326e-05/0.4237, allocations: 59.89 kB / 0.6996 GB, free: 13.08 MB / 0.5573 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0004613/0.4242, allocations: 0.5979 MB / 0.7002 GB, free: 12.61 MB / 0.5573 GB
Notification: Performance of collectPreVariables (initialization): time 2.226e-05/0.4242, allocations: 32.52 kB / 0.7002 GB, free: 12.58 MB / 0.5573 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0001468/0.4244, allocations: 427.2 kB / 0.7006 GB, free: 12.29 MB / 0.5573 GB
Notification: Performance of collectInitialBindings (initialization): time 5.878e-05/0.4244, allocations: 172.5 kB / 0.7008 GB, free: 12.15 MB / 0.5573 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 8.979e-05/0.4245, allocations: 106.5 kB / 0.7009 GB, free: 12.08 MB / 0.5573 GB
Notification: Performance of setup shared object (initialization): time 6.035e-05/0.4246, allocations: 378.4 kB / 0.7013 GB, free: 11.73 MB / 0.5573 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0001584/0.4247, allocations: 130.9 kB / 0.7014 GB, free: 11.64 MB / 0.5573 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0001906/0.4249, allocations: 298.5 kB / 0.7017 GB, free: 11.34 MB / 0.5573 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0003728/0.4253, allocations: 468.7 kB / 0.7021 GB, free: 10.96 MB / 0.5573 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.857e-06/0.4253, allocations: 4 kB / 0.7021 GB, free: 10.96 MB / 0.5573 GB
Notification: Performance of matching and sorting (n=69) (initialization): time 0.0005672/0.4259, allocations: 0.5948 MB / 0.7027 GB, free: 10.52 MB / 0.5573 GB
Notification: Performance of prepare postOptimizeDAE: time 1.82e-05/0.4259, allocations: 8 kB / 0.7027 GB, free: 10.52 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 7.184e-06/0.4259, allocations: 4 kB / 0.7027 GB, free: 10.51 MB / 0.5573 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0001829/0.4261, allocations: 61.27 kB / 0.7028 GB, free: 10.46 MB / 0.5573 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002049/0.4263, allocations: 116.1 kB / 0.7029 GB, free: 10.36 MB / 0.5573 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0007874/0.4271, allocations: 1.554 MB / 0.7044 GB, free: 8.91 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0002373/0.4273, allocations: 50.3 kB / 0.7044 GB, free: 8.871 MB / 0.5573 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 2.77e-05/0.4273, allocations: 26.86 kB / 0.7045 GB, free: 8.848 MB / 0.5573 GB
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 23
 * Number of states: 0 ()
 * Number of discrete variables: 5 (steamGenerator.outlet.state.phase,waterSource.outlet.state.phase,turbine.outlet.state.phase,flowResistance.outlet.state.phase,pump.outlet.state.phase)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (64):
 * Single equations (assignments): 63
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 0
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 0
 * Torn equation systems: 1
 * Mixed (continuous/discrete) equation systems: 0
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 1 system
   {(1,5,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 0 systems
Notification: Performance of prepare postOptimizeDAE: time 0.0001931/0.4275, allocations: 209.1 kB / 0.7047 GB, free: 8.695 MB / 0.5573 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 5.739e-05/0.4276, allocations: 86.8 kB / 0.7048 GB, free: 8.613 MB / 0.5573 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001024/0.4286, allocations: 1.673 MB / 0.7064 GB, free: 7.504 MB / 0.5573 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 6.733e-06/0.4286, allocations: 7.922 kB / 0.7064 GB, free: 7.496 MB / 0.5573 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.017e-06/0.4286, allocations: 3.188 kB / 0.7064 GB, free: 7.496 MB / 0.5573 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001419/0.4287, allocations: 142.4 kB / 0.7065 GB, free: 7.375 MB / 0.5573 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 4.733e-05/0.4288, allocations: 21.89 kB / 0.7066 GB, free: 7.359 MB / 0.5573 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001253/0.4289, allocations: 15.55 kB / 0.7066 GB, free: 7.352 MB / 0.5573 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 3.987e-05/0.429, allocations: 36.3 kB / 0.7066 GB, free: 7.32 MB / 0.5573 GB
Notification: Performance of postOpt createDAEmodeBDAE (simulation): time 0.0007066/0.4297, allocations: 0.8939 MB / 0.7075 GB, free: 6.664 MB / 0.5573 GB
Notification: Performance of postOpt symbolicJacobianDAE (simulation): time 0.0008198/0.4305, allocations: 1.346 MB / 0.7088 GB, free: 5.703 MB / 0.5573 GB
Notification: Performance of postOpt setEvaluationStage (simulation): time 0.0002114/0.4307, allocations: 289.6 kB / 0.7091 GB, free: 5.531 MB / 0.5573 GB
Notification: Performance of sorting global known variables: time 0.0003487/0.431, allocations: 0.4916 MB / 0.7096 GB, free: 5.168 MB / 0.5573 GB
Notification: Performance of Backend: time 6.21e-07/0.431, allocations: 0 / 0.7096 GB, free: 5.168 MB / 0.5573 GB
Notification: Performance of simCode: created initialization part: time 0.011/0.442, allocations: 2.964 MB / 0.7124 GB, free: 2.574 MB / 0.5573 GB
Notification: Performance of SimCode: time 0.002038/0.4441, allocations: 2.207 MB / 0.7146 GB, free: 496 kB / 0.5573 GB
Notification: Performance of Templates: time 0.06519/0.5093, allocations: 69.97 MB / 0.7829 GB, free: 10.94 MB / 0.6355 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.diff",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[1] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.dT_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.dT_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable waterSink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable waterSink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
"
[Timeout remaining time 660]
""

Variables in the reference:CPUtime,EventCounter,Time,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,efficiency.displayVariablefinal,efficiency.showNumber,efficiency.significantDigits,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,der(flowResistance.inlet.m_flow),flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,pump.L,pump.P,pump.P_nom,pump.TC,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.assertionLevel,pump.clip_p_out,pump.dh,pump.dp,pump.dp_fixed,pump.dp_nom,pump.dp_start,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,der(pump.inlet.m_flow),pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,steamGenerator.L,steamGenerator.P,steamGenerator.Q_flow,steamGenerator.T_out_fixed,steamGenerator.assertionLevel,steamGenerator.clip_p_out,steamGenerator.dT,steamGenerator.dT_fixed,steamGenerator.dh,steamGenerator.dh_fixed,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.du,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.h_out_fixed,steamGenerator.initM_flow,der(steamGenerator.inlet.m_flow),steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletSpec_actual,steamGenerator.outletValueSpec,steamGenerator.p,steamGenerator.p_in,steamGenerator.p_inf,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.systemSpec,steamGenerator.u_in,steamGenerator.u_out,steamGenerator.v_in,steamGenerator.v_out,steamGenerator.w_amb,steamGenerator.w_exp,steamGenerator.w_exp_net,turbine.L,turbine.P,turbine.P_nom,turbine.TC,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.assertionLevel,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dp_fixed,turbine.dp_nom,turbine.dp_start,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,der(turbine.inlet.m_flow),turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.pRatio_fixed,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,waterSink.L,der(waterSink.inlet.m_flow),waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p,waterSink.p0,waterSink.p0_par,waterSink.r,waterSource.L,waterSource.T0,waterSource.T0_par,waterSource.h0,waterSource.h0_par,der(waterSource.outlet.m_flow),waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0,waterSource.p0_par

Variables in the result:$cse4.R_s,$cse4.T,$cse4.cp,$cse4.cv,$cse4.dpT,$cse4.h,$cse4.p,$cse4.pd,$cse4.phase,$cse4.pt,$cse4.region,$cse4.rho,$cse4.s,$cse4.vp,$cse4.vt,$cse4.x,$cse5.R_s,$cse5.T,$cse5.cp,$cse5.cv,$cse5.dpT,$cse5.h,$cse5.p,$cse5.pd,$cse5.phase,$cse5.pt,$cse5.region,$cse5.rho,$cse5.s,$cse5.vp,$cse5.vt,$cse5.x,der(flowResistance.inlet.m_flow),dropOfCommons.L,dropOfCommons.assertionLevel,dropOfCommons.g,dropOfCommons.k_volume_damping,dropOfCommons.m_flow_reg,dropOfCommons.omega_reg,dropOfCommons.p_min,dropOfCommons.rho_min,efficiency.displayVariablefinal,efficiency.number,efficiency.showNumber,efficiency.significantDigits,flowResistance.D_h,flowResistance.L,flowResistance.L_value,flowResistance.a,flowResistance.areaCross,flowResistance.areaCrossInput,flowResistance.areaHydraulic,flowResistance.b,flowResistance.clip_p_out,flowResistance.dp,flowResistance.dp_ref_color,flowResistance.dr_corr,flowResistance.h_in,flowResistance.h_out,flowResistance.initM_flow,flowResistance.inlet.m_flow,flowResistance.inlet.r,flowResistance.inlet.state.T,flowResistance.inlet.state.d,flowResistance.inlet.state.h,flowResistance.inlet.state.p,flowResistance.inlet.state.phase,flowResistance.l,flowResistance.m_acceleration_0,flowResistance.m_flow,flowResistance.m_flowStateSelect,flowResistance.m_flow_0,flowResistance.mu_in,flowResistance.outlet.m_flow,flowResistance.outlet.r,flowResistance.outlet.state.T,flowResistance.outlet.state.d,flowResistance.outlet.state.h,flowResistance.outlet.state.p,flowResistance.outlet.state.phase,flowResistance.p_in,flowResistance.p_min,flowResistance.p_out,flowResistance.perimeter,flowResistance.perimeterInput,flowResistance.phi,flowResistance.pressureDropSignificantDigits,flowResistance.r,flowResistance.rho_in,flowResistance.rho_min,flowResistance.shape,pump.L,pump.P,pump.P_in_internal,pump.adiabaticModel.eta_is,pump.adiabaticModel.h_in,pump.adiabaticModel.h_out,pump.adiabaticModel.h_out_is,pump.adiabaticModel.p_out,pump.adiabaticModel.s_in,pump.adiabaticModel.state_in.T,pump.adiabaticModel.state_in.d,pump.adiabaticModel.state_in.h,pump.adiabaticModel.state_in.p,pump.adiabaticModel.state_in.phase,pump.adiabaticModel.w_t,pump.adiabaticModel.w_t_is,pump.clip_p_out,pump.dh,pump.dp,pump.dr_corr,pump.etaSpec,pump.eta_actual,pump.eta_fixed,pump.eta_is,pump.h_in,pump.h_out,pump.initM_flow,pump.inlet.m_flow,pump.inlet.r,pump.inlet.state.T,pump.inlet.state.d,pump.inlet.state.h,pump.inlet.state.p,pump.inlet.state.phase,pump.m_acceleration_0,pump.m_flow,pump.m_flowStateSelect,pump.m_flow_0,pump.outlet.m_flow,pump.outlet.r,pump.outlet.state.T,pump.outlet.state.d,pump.outlet.state.h,pump.outlet.state.p,pump.outlet.state.phase,pump.outletSpec,pump.outletSpec_actual,pump.outletValueSpec,pump.pRatio,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,steamGenerator.L,steamGenerator.Q_flow,steamGenerator.T_in,steamGenerator.T_out_fixed,steamGenerator.clip_p_out,steamGenerator.dT,steamGenerator.dh,steamGenerator.dp,steamGenerator.dr_corr,steamGenerator.h_in,steamGenerator.h_out,steamGenerator.initM_flow,steamGenerator.inlet.m_flow,steamGenerator.inlet.r,steamGenerator.inlet.state.T,steamGenerator.inlet.state.d,steamGenerator.inlet.state.h,steamGenerator.inlet.state.p,steamGenerator.inlet.state.phase,steamGenerator.m_acceleration_0,steamGenerator.m_flow,steamGenerator.m_flowStateSelect,steamGenerator.m_flow_0,steamGenerator.outlet.m_flow,steamGenerator.outlet.r,steamGenerator.outlet.state.T,steamGenerator.outlet.state.d,steamGenerator.outlet.state.h,steamGenerator.outlet.state.p,steamGenerator.outlet.state.phase,steamGenerator.outletSpec,steamGenerator.outletSpec_actual,steamGenerator.outletValueSpec,steamGenerator.p,steamGenerator.p_in,steamGenerator.p_min,steamGenerator.p_out,steamGenerator.q,steamGenerator.rho_in,steamGenerator.rho_out,steamGenerator.singularityRegime,steamGenerator.systemSpec,time,turbine.L,turbine.P,turbine.P_in_internal,turbine.adiabaticModel.eta_is,turbine.adiabaticModel.h_in,turbine.adiabaticModel.h_out,turbine.adiabaticModel.h_out_is,turbine.adiabaticModel.p_out,turbine.adiabaticModel.s_in,turbine.adiabaticModel.state_in.T,turbine.adiabaticModel.state_in.d,turbine.adiabaticModel.state_in.h,turbine.adiabaticModel.state_in.p,turbine.adiabaticModel.state_in.phase,turbine.adiabaticModel.w_t,turbine.adiabaticModel.w_t_is,turbine.clip_p_out,turbine.dh,turbine.dp,turbine.dr_corr,turbine.etaSpec,turbine.eta_actual,turbine.eta_fixed,turbine.eta_is,turbine.h_in,turbine.h_out,turbine.initM_flow,turbine.inlet.m_flow,turbine.inlet.r,turbine.inlet.state.T,turbine.inlet.state.d,turbine.inlet.state.h,turbine.inlet.state.p,turbine.inlet.state.phase,turbine.m_acceleration_0,turbine.m_flow,turbine.m_flowStateSelect,turbine.m_flow_0,turbine.outlet.m_flow,turbine.outlet.r,turbine.outlet.state.T,turbine.outlet.state.d,turbine.outlet.state.h,turbine.outlet.state.p,turbine.outlet.state.phase,turbine.outletSpec,turbine.outletSpec_actual,turbine.outletValueSpec,turbine.pRatio,turbine.p_in,turbine.p_min,turbine.p_out,turbine.p_out_fixed,turbine.singularityRegime,waterSink.L,waterSink.inlet.m_flow,waterSink.inlet.r,waterSink.inlet.state.T,waterSink.inlet.state.d,waterSink.inlet.state.h,waterSink.inlet.state.p,waterSink.inlet.state.phase,waterSink.p,waterSink.p0,waterSink.p0_par,waterSink.r,waterSource.L,waterSource.T0,waterSource.T0_par,waterSource.h0,waterSource.h0_par,waterSource.outlet.m_flow,waterSource.outlet.r,waterSource.outlet.state.T,waterSource.outlet.state.d,waterSource.outlet.state.h,waterSource.outlet.state.p,waterSource.outlet.state.phase,waterSource.p0,waterSource.p0_par
[Calling sys.exit(0), Time elapsed: 6.248835966922343]