Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_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]
"[<interactive>:1:22-1:33:writable] Warning: Modelica only supports 32-bit signed integers! Transforming: 13743895347 into a real
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.0003368/0.0003368, 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 0.0002723/0.0002723, 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 0.09164/0.09164, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 180]
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo", uses=false) [Timeout 180]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo): time 0.04759/0.04759, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 180]
Using package ThermofluidStream with version 1.4.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ThermofluidStream 1.4.0/package.mo)
Using package Modelica with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.1.0+maint.om/package.mo)
Using package Complex with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.1.0+maint.om/package.mo)
Using package ModelicaServices with version 4.1.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo)
Running command: simulate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",variableFilter="CPUtime|EventCounter|Time|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|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_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop",simflags="-abortSlowSimulation -alarm=240  -emit_protected -lv LOG_STATS")
simulate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop,startTime=0,stopTime=1,tolerance=1e-06,numberOfIntervals=100,outputFormat="mat",variableFilter="CPUtime|EventCounter|Time|dropOfCommons.L|dropOfCommons.assertionLevel|dropOfCommons.g|dropOfCommons.instanceNameColor.[0-9,]+.|dropOfCommons.k_volume_damping|dropOfCommons.m_flow_reg|dropOfCommons.omega_reg|dropOfCommons.p_min|dropOfCommons.rho_min|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_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop",simflags="-abortSlowSimulation -alarm=240  -emit_protected -lv LOG_STATS") [Timeout 900]
"Notification: Performance of FrontEnd - loaded program: time 7.61e-07/7.61e-07, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - Absyn->SCode: time 1.356e-05/1.433e-05, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop): time 0.0202/0.02021, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.instExpressions: time 0.0228/0.04302, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFInst.updateImplicitVariability: time 0.0003935/0.04341, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeComponents: time 0.0005507/0.04396, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeBindings: time 0.01777/0.06173, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFTyping.typeClassSections: time 0.002165/0.0639, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.flatten: time 0.001024/0.06492, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.resolveConnections: time 0.00023/0.06515, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFEvalConstants.evaluate: time 0.004866/0.07002, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFSimplifyModel.simplify: time 0.0004118/0.07043, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFPackage.collectConstants: time 6.232e-05/0.07049, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFFlatten.collectFunctions: time 0.01873/0.08922, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFScalarize.scalarize: time 0.0001668/0.08939, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFVerifyModel.verify: time 0.0003388/0.08972, allocations: 0 / 0, free: 0 / 0
Notification: Performance of NFConvertDAE.convert: time 0.01076/0.1005, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd - DAE generated: time 0.0001141/0.1006, allocations: 0 / 0, free: 0 / 0
Notification: Performance of FrontEnd: time 2.254e-06/0.1006, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Transformations before backend: time 8.306e-06/0.1006, 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: 173
 * Number of variables: 173
Notification: Performance of Generate backend data structure: time 0.003427/0.104, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare preOptimizeDAE: time 9.435e-05/0.1041, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0005731/0.1047, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evaluateParameters (simulation): time 0.0008965/0.1056, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001058/0.1057, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt expandDerOperator (simulation): time 7.71e-05/0.1058, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt clockPartitioning (simulation): time 0.0007815/0.1066, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt findStateOrder (simulation): time 1.978e-05/0.1066, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt replaceEdgeChange (simulation): time 5.627e-05/0.1066, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.875e-05/0.1067, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0004585/0.1071, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.002015/0.1091, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt comSubExp (simulation): time 0.000603/0.1097, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt resolveLoops (simulation): time 0.0001247/0.1099, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt evalFunc (simulation): time 0.232/0.3419, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 2.603e-05/0.3419, allocations: 0 / 0, free: 0 / 0
Notification: Performance of pre-optimization done (n=47): time 6.282e-06/0.3419, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=47): time 0.001055/0.343, allocations: 0 / 0, free: 0 / 0
Notification: Performance of inlineWhenForInitialization (initialization): time 2.073e-05/0.343, allocations: 0 / 0, free: 0 / 0
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0004095/0.3434, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectPreVariables (initialization): time 3.918e-05/0.3434, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialEqns (initialization): time 0.0001767/0.3436, allocations: 0 / 0, free: 0 / 0
Notification: Performance of collectInitialBindings (initialization): time 0.0001169/0.3437, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001176/0.3438, allocations: 0 / 0, free: 0 / 0
Notification: Performance of setup shared object (initialization): time 4.894e-05/0.3439, allocations: 0 / 0, free: 0 / 0
Notification: Performance of preBalanceInitialSystem (initialization): time 7.313e-05/0.344, allocations: 0 / 0, free: 0 / 0
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0001129/0.3441, allocations: 0 / 0, free: 0 / 0
Notification: Performance of analyzeInitialSystem (initialization): time 0.0002389/0.3443, allocations: 0 / 0, free: 0 / 0
Notification: Performance of solveInitialSystemEqSystem (initialization): time 6.522e-06/0.3443, allocations: 0 / 0, free: 0 / 0
Notification: Performance of matching and sorting (n=69) (initialization): time 0.0004517/0.3448, allocations: 0 / 0, free: 0 / 0
Notification: Performance of prepare postOptimizeDAE: time 1.84e-05/0.3448, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 9.118e-06/0.3448, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (initialization): time 0.0002111/0.345, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002569/0.3453, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.0007889/0.3461, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0002192/0.3463, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.93e-05/0.3463, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 23
 * Number of states: 0 ()
 * Number of discrete variables: 5 (pump.outlet.state.phase,flowResistance.outlet.state.phase,turbine.outlet.state.phase,waterSource.outlet.state.phase,steamGenerator.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 0.0001619/0.3465, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt lateInlineFunction (simulation): time 7.207e-05/0.3466, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.0009553/0.3475, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inlineArrayEqn (simulation): time 1.841e-05/0.3475, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt constantLinearSystem (simulation): time 3.206e-06/0.3475, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifysemiLinear (simulation): time 5.63e-06/0.3475, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeSimpleEquations (simulation): time 0.001537/0.3491, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 4.668e-06/0.3491, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt solveSimpleEquations (simulation): time 0.0001635/0.3492, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt tearingSystem (simulation): time 0.0001626/0.3494, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt inputDerivativesUsed (simulation): time 2.388e-05/0.3494, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStrongComponentJacobians (simulation): time 0.0005631/0.35, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt calculateStateSetsJacobians (simulation): time 1.964e-06/0.35, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt symbolicJacobian (simulation): time 0.0006664/0.3507, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt removeConstants (simulation): time 0.0001877/0.3509, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.0001952/0.351, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001979/0.3512, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt findZeroCrossings (simulation): time 7.174e-05/0.3513, allocations: 0 / 0, free: 0 / 0
Notification: Performance of postOpt collapseArrayExpressions (simulation): time 2.369e-05/0.3513, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sorting global known variables: time 0.0002411/0.3516, allocations: 0 / 0, free: 0 / 0
Notification: Performance of sort global known variables: time 2.354e-05/0.3516, allocations: 0 / 0, free: 0 / 0
Notification: Performance of remove unused functions: time 0.002895/0.3545, allocations: 0 / 0, free: 0 / 0
Notification: Model statistics after passing the back-end for simulation:
 * Number of independent subsystems: 2
 * Number of states: 1 (flowResistance.inlet.m_flow)
 * Number of discrete variables: 10 ($cse1.phase,$cse1.region,$cse2.phase,$cse2.region,$cse3.phase,$cse3.region,$cse6.phase,$cse6.region,$cse7.phase,$cse7.region)
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for simulation (47):
 * Single equations (assignments): 41
 * Array equations: 0
 * Algorithm blocks: 0
 * Record equations: 5
 * 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 Backend phase and start with SimCode phase: time 0.004589/0.3591, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created initialization part: time 0.0004646/0.3596, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created event and clocks part: time 1.924e-06/0.3596, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created simulation system equations: time 0.0002446/0.3598, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created of all other equations (e.g. parameter, nominal, assert, etc): time 0.001158/0.361, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: created linear, non-linear and system jacobian parts: time 0.001989/0.3629, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: some other stuff during SimCode phase: time 0.0001905/0.3631, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: alias equations: time 0.0003175/0.3635, allocations: 0 / 0, free: 0 / 0
Notification: Performance of simCode: all other stuff during SimCode phase: time 0.0004707/0.3639, allocations: 0 / 0, free: 0 / 0
Notification: Performance of SimCode: time 3.675e-05/0.364, allocations: 0 / 0, free: 0 / 0
Notification: Performance of Templates: time 0.009673/0.3736, allocations: 0 / 0, free: 0 / 0
"
[Timeout remaining time 899]
diffSimulationResults("ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_ref.mat","",relTol=0.003,relTolDiffMinMax=0.003,rangeDelta=0.001) [Timeout 660]
"Error: Could not read variable CPUtime in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.P in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.P from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.dT_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.dT_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.dh_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.dh_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.du in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.du from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.h_out_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.h_out_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.p_inf in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.p_inf from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.u_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.u_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.u_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.u_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.v_in in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.v_in from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.v_out in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.v_out from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.w_amb in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.w_amb from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.w_exp in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.w_exp from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable steamGenerator.w_exp_net in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable steamGenerator.w_exp_net from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.P_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.P_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.TC in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.TC from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.assertionLevel in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.assertionLevel from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.dp_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.dp_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.dp_nom in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.dp_nom from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.dp_start in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.dp_start from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable turbine.pRatio_fixed in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable turbine.pRatio_fixed from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable waterSink.inlet.der(m_flow) in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable waterSink.inlet.der(m_flow) from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
"
[Timeout remaining time 660]
Reference file matches
[Calling sys.exit(0), Time elapsed: 1.2655535927042365]