Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.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 0.001338/0.001338, allocations: 81.3 kB / 20.05 MB, free: 1.48 MB / 14.72 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 0.001439/0.001439, allocations: 165.5 kB / 23.34 MB, free: 4.469 MB / 14.72 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 1.502/1.502, allocations: 177.1 MB / 203.7 MB, free: 9.141 MB / 190.1 MB
"
[Timeout remaining time 178]
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 1.023/1.023, allocations: 116 MB / 376.1 MB, free: 7.492 MB / 350.1 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.Step2SaturatedVapor,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|h_dew.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheaterAndBoiler.L|preheaterAndBoiler.P|preheaterAndBoiler.Q_flow|preheaterAndBoiler.T_out_fixed|preheaterAndBoiler.assertionLevel|preheaterAndBoiler.clip_p_out|preheaterAndBoiler.dT|preheaterAndBoiler.dT_fixed|preheaterAndBoiler.dh|preheaterAndBoiler.dh_fixed|preheaterAndBoiler.dp|preheaterAndBoiler.dr_corr|preheaterAndBoiler.du|preheaterAndBoiler.h_in|preheaterAndBoiler.h_out|preheaterAndBoiler.h_out_fixed|preheaterAndBoiler.initM_flow|der.preheaterAndBoiler.inlet.m_flow.|preheaterAndBoiler.inlet.m_flow|preheaterAndBoiler.inlet.r|preheaterAndBoiler.inlet.state.T|preheaterAndBoiler.inlet.state.d|preheaterAndBoiler.inlet.state.h|preheaterAndBoiler.inlet.state.p|preheaterAndBoiler.inlet.state.phase|preheaterAndBoiler.m_acceleration_0|preheaterAndBoiler.m_flow|preheaterAndBoiler.m_flowStateSelect|preheaterAndBoiler.m_flow_0|preheaterAndBoiler.outlet.m_flow|preheaterAndBoiler.outlet.r|preheaterAndBoiler.outlet.state.T|preheaterAndBoiler.outlet.state.d|preheaterAndBoiler.outlet.state.h|preheaterAndBoiler.outlet.state.p|preheaterAndBoiler.outlet.state.phase|preheaterAndBoiler.outletSpec|preheaterAndBoiler.outletSpec_actual|preheaterAndBoiler.outletSpec_prescribed|preheaterAndBoiler.outletValueSpec|preheaterAndBoiler.p|preheaterAndBoiler.p_in|preheaterAndBoiler.p_inf|preheaterAndBoiler.p_min|preheaterAndBoiler.p_out|preheaterAndBoiler.q|preheaterAndBoiler.rho_in|preheaterAndBoiler.rho_out|preheaterAndBoiler.singularityRegime|preheaterAndBoiler.systemSpec|preheaterAndBoiler.u_in|preheaterAndBoiler.u_out|preheaterAndBoiler.v_in|preheaterAndBoiler.v_out|preheaterAndBoiler.w_amb|preheaterAndBoiler.w_exp|preheaterAndBoiler.w_exp_net|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.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|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.Step2SaturatedVapor")
translateModel(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor,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|h_dew.y|outletPressure.duration|outletPressure.height|outletPressure.offset|outletPressure.startTime|outletPressure.y|preheaterAndBoiler.L|preheaterAndBoiler.P|preheaterAndBoiler.Q_flow|preheaterAndBoiler.T_out_fixed|preheaterAndBoiler.assertionLevel|preheaterAndBoiler.clip_p_out|preheaterAndBoiler.dT|preheaterAndBoiler.dT_fixed|preheaterAndBoiler.dh|preheaterAndBoiler.dh_fixed|preheaterAndBoiler.dp|preheaterAndBoiler.dr_corr|preheaterAndBoiler.du|preheaterAndBoiler.h_in|preheaterAndBoiler.h_out|preheaterAndBoiler.h_out_fixed|preheaterAndBoiler.initM_flow|der.preheaterAndBoiler.inlet.m_flow.|preheaterAndBoiler.inlet.m_flow|preheaterAndBoiler.inlet.r|preheaterAndBoiler.inlet.state.T|preheaterAndBoiler.inlet.state.d|preheaterAndBoiler.inlet.state.h|preheaterAndBoiler.inlet.state.p|preheaterAndBoiler.inlet.state.phase|preheaterAndBoiler.m_acceleration_0|preheaterAndBoiler.m_flow|preheaterAndBoiler.m_flowStateSelect|preheaterAndBoiler.m_flow_0|preheaterAndBoiler.outlet.m_flow|preheaterAndBoiler.outlet.r|preheaterAndBoiler.outlet.state.T|preheaterAndBoiler.outlet.state.d|preheaterAndBoiler.outlet.state.h|preheaterAndBoiler.outlet.state.p|preheaterAndBoiler.outlet.state.phase|preheaterAndBoiler.outletSpec|preheaterAndBoiler.outletSpec_actual|preheaterAndBoiler.outletSpec_prescribed|preheaterAndBoiler.outletValueSpec|preheaterAndBoiler.p|preheaterAndBoiler.p_in|preheaterAndBoiler.p_inf|preheaterAndBoiler.p_min|preheaterAndBoiler.p_out|preheaterAndBoiler.q|preheaterAndBoiler.rho_in|preheaterAndBoiler.rho_out|preheaterAndBoiler.singularityRegime|preheaterAndBoiler.systemSpec|preheaterAndBoiler.u_in|preheaterAndBoiler.u_out|preheaterAndBoiler.v_in|preheaterAndBoiler.v_out|preheaterAndBoiler.w_amb|preheaterAndBoiler.w_exp|preheaterAndBoiler.w_exp_net|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.outletSpec_prescribed|pump.outletValueSpec|pump.pRatio|pump.pRatio_fixed|pump.p_in|pump.p_min|pump.p_out|pump.p_out_fixed|pump.singularityRegime|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.Step2SaturatedVapor") [Timeout 660]
"Notification: Performance of FrontEnd - Absyn->SCode: time 2.643e-05/2.643e-05, allocations: 2.281 kB / 0.5547 GB, free: 13.67 MB / 478.1 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor): time 0.06475/0.06478, allocations: 51.03 MB / 0.6046 GB, free: 10.46 MB / 0.5137 GB
Notification: Performance of NFInst.instExpressions: time 0.03081/0.09559, allocations: 21.61 MB / 0.6257 GB, free: 4.793 MB / 0.5294 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.001008/0.0966, allocations: 43.56 kB / 0.6257 GB, free: 4.75 MB / 0.5294 GB
Notification: Performance of NFTyping.typeComponents: time 0.001476/0.09807, allocations: 492.4 kB / 0.6262 GB, free: 4.266 MB / 0.5294 GB
Notification: Performance of NFTyping.typeBindings: time 0.02237/0.1204, allocations: 7.325 MB / 0.6333 GB, free: 12.91 MB / 0.545 GB
Notification: Performance of NFTyping.typeClassSections: time 0.003853/0.1243, allocations: 1.209 MB / 0.6345 GB, free: 11.7 MB / 0.545 GB
Notification: Performance of NFFlatten.flatten: time 0.002731/0.127, allocations: 1.825 MB / 0.6363 GB, free: 9.859 MB / 0.545 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.0004247/0.1274, allocations: 140.1 kB / 0.6364 GB, free: 9.703 MB / 0.545 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.0104/0.1378, allocations: 4.162 MB / 0.6405 GB, free: 5.484 MB / 0.545 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.0008847/0.1387, allocations: 370.8 kB / 0.6409 GB, free: 5.121 MB / 0.545 GB
Notification: Performance of NFPackage.collectConstants: time 0.0001434/0.1389, allocations: 60 kB / 0.6409 GB, free: 5.062 MB / 0.545 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.0184/0.1573, allocations: 9.456 MB / 0.6501 GB, free: 11.6 MB / 0.5606 GB
Notification: Performance of combineBinaries: time 0.001983/0.1593, allocations: 1.675 MB / 0.6518 GB, free: 9.906 MB / 0.5606 GB
Notification: Performance of replaceArrayConstructors: time 0.0009975/0.1603, allocations: 1.13 MB / 0.6529 GB, free: 8.762 MB / 0.5606 GB
Notification: Performance of NFVerifyModel.verify: time 0.0002622/0.1605, allocations: 100 kB / 0.653 GB, free: 8.664 MB / 0.5606 GB
Notification: Performance of FrontEnd: time 0.0006768/0.1612, allocations: 235.4 kB / 0.6532 GB, free: 8.434 MB / 0.5606 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 177 (149)
 * Number of variables: 177 (177)
Notification: Performance of [SIM] Bindings: time 0.005501/0.1667, allocations: 4.607 MB / 0.6577 GB, free: 3.633 MB / 0.5606 GB
Notification: Performance of [SIM] FunctionAlias: time 0.001067/0.1678, allocations: 0.7109 MB / 0.6584 GB, free: 2.988 MB / 0.5606 GB
Notification: Performance of [SIM] Early Inline: time 0.004392/0.1722, allocations: 3.357 MB / 0.6617 GB, free: 15.7 MB / 0.5762 GB
Notification: Performance of [SIM] Simplify 1: time 0.0004369/0.1726, allocations: 248.1 kB / 0.6619 GB, free: 15.42 MB / 0.5762 GB
Notification: Performance of [SIM] Alias: time 0.005535/0.1781, allocations: 3.564 MB / 0.6654 GB, free: 11.37 MB / 0.5762 GB
Notification: Performance of [SIM] Simplify 2: time 0.0002999/0.1784, allocations: 172.1 kB / 0.6656 GB, free: 11.17 MB / 0.5762 GB
Notification: Performance of [SIM] Remove Stream: time 0.000262/0.1787, allocations: 192.1 kB / 0.6657 GB, free: 10.96 MB / 0.5762 GB
Notification: Performance of [SIM] Detect States: time 0.000928/0.1796, allocations: 0.6615 MB / 0.6664 GB, free: 10.21 MB / 0.5762 GB
Notification: Performance of [SIM] Events: time 0.0001945/0.1798, allocations: 103.2 kB / 0.6665 GB, free: 10.11 MB / 0.5762 GB
Notification: Performance of [SIM] Partitioning: time 0.001339/0.1812, allocations: 0.9527 MB / 0.6674 GB, free: 9.102 MB / 0.5762 GB
Notification: Performance of [SIM] Causalize: time 0.003483/0.1846, allocations: 2.427 MB / 0.6698 GB, free: 6.652 MB / 0.5762 GB
Notification: Performance of [SIM] After Index Reduction Inline: time 0.002055/0.1867, allocations: 1.788 MB / 0.6715 GB, free: 4.891 MB / 0.5762 GB
Notification: Performance of [INI] Simplify: time 0.001596/0.1883, allocations: 0.783 MB / 0.6723 GB, free: 4.023 MB / 0.5762 GB
Notification: Performance of [INI] Inline: time 0.002946/0.1912, allocations: 2.494 MB / 0.6747 GB, free: 1.516 MB / 0.5762 GB
Notification: Performance of [INI] Partitioning: time 0.0001318/0.1914, allocations: 64.05 kB / 0.6748 GB, free: 1.438 MB / 0.5762 GB
Notification: Performance of [INI] Cleanup: time 0.0004319/0.1918, allocations: 439.6 kB / 0.6752 GB, free: 1.008 MB / 0.5762 GB
Notification: Performance of [INI] Causalize: time 0.004677/0.1965, allocations: 3.067 MB / 0.6782 GB, free: 13.89 MB / 0.5919 GB
Notification: Performance of [INI] Tearing: time 0.0001402/0.1966, allocations: 115.9 kB / 0.6783 GB, free: 13.77 MB / 0.5919 GB
Notification: Performance of [SIM] Initialization: time 5.14e-06/0.1966, allocations: 4 kB / 0.6783 GB, free: 13.77 MB / 0.5919 GB
Notification: Performance of [SIM] Remove Dummies: time 1.898e-05/0.1966, allocations: 1 kB / 0.6783 GB, free: 13.77 MB / 0.5919 GB
Notification: Performance of [SIM] Tearing: time 9.785e-05/0.1967, allocations: 91.95 kB / 0.6784 GB, free: 13.68 MB / 0.5919 GB
Notification: Performance of [SIM] Categorize: time 1.618e-05/0.1967, allocations: 8 kB / 0.6784 GB, free: 13.67 MB / 0.5919 GB
Notification: Performance of [SIM] Solve: time 0.001573/0.1983, allocations: 0.8356 MB / 0.6792 GB, free: 12.82 MB / 0.5919 GB
Notification: Performance of [SIM] Jacobian: time 0.001644/0.2, allocations: 1.15 MB / 0.6804 GB, free: 11.59 MB / 0.5919 GB
Notification: Performance of [SIM] Minimize Homotopy System: time 7.61e-07/0.2, allocations: 0 / 0.6804 GB, free: 11.59 MB / 0.5919 GB
Notification: Partition statistics after passing the back-end:
 * Number of ODE partitions: ..................... 0
 * Number of algebraic partitions: ............... 0
 * Number of ODE event partitions: ............... 1
 * Number of algebraic event partitions: ......... 0
 * Number of clocked partitions: ................. 0
 * Number of initial partitions: ................. 1
 * Number of initial(lambda=0) partitions: ....... 0
Notification: Variable statistics after passing the back-end:
 * Number of states: ............................. 1 (1) {pump.m_flow}
 * Number of discrete states: .................... 0 (0) {}
 * Number of clocked states: ..................... 0 (0) {}
 * Number of discrete variables: ................. 21 (21) {pump.inlet.state.phase, pump.outlet.state.phase, pump.adiabaticModel.state_in.phase, turbine.inlet.state.phase, turbine.outlet.state.phase, turbine.adiabaticModel.state_in.phase, preheaterAndBoiler.inlet.state.phase, preheaterAndBoiler.outlet.state.phase, waterSource.outlet.state.phase, waterSink.inlet.state.phase, flowResistance.inlet.state.phase, flowResistance.outlet.state.phase, $FUN_1.phase, $FUN_2.phase, $FUN_5.phase, $FUN_6.phase, $FUN_8.phase, $SEV_1, $SEV_0, $TEV_1, $TEV_0}
 * Number of clocks: ............................. 0 (0) {}
 * Number of top-level inputs: ................... 0 (0) {}
Notification: [Simulation] Strong Component statistics after passing the back-end:
 * Number of single strong components: ........... 110 (scalar:110, array:0, record:0)
 * Number of multi strong components: ............ 0 (algorithm:0, when:0, if:0, tuple:7)
 * Number of for-loop strong components: ......... 0 (resizable: 0, generic: 0, entwined:0)
 * Number of algebraic-loop strong components: ... 1 (linear: 1, nonlinear:0)
Notification: [Initialization] Strong Component statistics after passing the back-end:
 * Number of single strong components: ........... 140 (scalar:140, array:0, record:0)
 * Number of multi strong components: ............ 0 (algorithm:0, when:0, if:0, tuple:7)
 * Number of for-loop strong components: ......... 0 (resizable: 0, generic: 0, entwined:0)
 * Number of algebraic-loop strong components: ... 1 (linear: 1, nonlinear:0)
Notification: Performance of backend: time 0.0001048/0.2001, allocations: 69.14 kB / 0.6804 GB, free: 11.53 MB / 0.5919 GB
Notification: Performance of SimCode: time 0.3557/0.5558, allocations: 14.44 MB / 0.6945 GB, free: 51.46 MB / 0.5919 GB
Notification: Performance of Templates: time 0.06564/0.6214, allocations: 50.21 MB / 0.7436 GB, free: 34.98 MB / 0.5919 GB
"
[Timeout remaining time 659]
make -j1 -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.makefile [Timeout 660]
(rm -f ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.pipe ; mkfifo ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.pipe ; head -c 1048576 < ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.pipe >> ../files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.sim & ./ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat","/mnt/ReferenceFiles/ThermofluidStream-main-regression/ReferenceData/ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_ref.mat","/var/lib/jenkins/ws/OpenModelicaLibraryTestingWork/OpenModelicaLibraryTesting/files/ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor.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.Step2SaturatedVapor_res.mat.
Warning: Get data of variable CPUtime from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable EventCounter in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable EventCounter from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.P in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.P from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.T_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.T_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.dT_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.dT_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.dh_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.dh_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.du in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.du from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.h_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.h_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.p_inf in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.p_inf from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.u_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.u_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.u_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.u_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.v_in in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.v_in from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.v_out in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.v_out from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.w_amb in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.w_amb from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.w_exp in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.w_exp from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable preheaterAndBoiler.w_exp_net in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable preheaterAndBoiler.w_exp_net from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable pump.p_out_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable pump.p_out_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.P_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.P_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.TC in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.TC from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.assertionLevel in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.assertionLevel from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.dp_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.dp_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.dp_nom in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.dp_nom from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.dp_start in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.dp_start from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable turbine.pRatio_fixed in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable turbine.pRatio_fixed from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat failed!
Error: Could not read variable waterSink.inlet.der(m_flow) in file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_res.mat.
Warning: Get data of variable waterSink.inlet.der(m_flow) from file ThermofluidStream_dev_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step2SaturatedVapor_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,h_dew.y,outletPressure.duration,outletPressure.height,outletPressure.offset,outletPressure.startTime,outletPressure.y,preheaterAndBoiler.L,preheaterAndBoiler.P,preheaterAndBoiler.Q_flow,preheaterAndBoiler.T_out_fixed,preheaterAndBoiler.assertionLevel,preheaterAndBoiler.clip_p_out,preheaterAndBoiler.dT,preheaterAndBoiler.dT_fixed,preheaterAndBoiler.dh,preheaterAndBoiler.dh_fixed,preheaterAndBoiler.dp,preheaterAndBoiler.dr_corr,preheaterAndBoiler.du,preheaterAndBoiler.h_in,preheaterAndBoiler.h_out,preheaterAndBoiler.h_out_fixed,preheaterAndBoiler.initM_flow,der(preheaterAndBoiler.inlet.m_flow),preheaterAndBoiler.inlet.m_flow,preheaterAndBoiler.inlet.r,preheaterAndBoiler.inlet.state.T,preheaterAndBoiler.inlet.state.d,preheaterAndBoiler.inlet.state.h,preheaterAndBoiler.inlet.state.p,preheaterAndBoiler.inlet.state.phase,preheaterAndBoiler.m_acceleration_0,preheaterAndBoiler.m_flow,preheaterAndBoiler.m_flowStateSelect,preheaterAndBoiler.m_flow_0,preheaterAndBoiler.outlet.m_flow,preheaterAndBoiler.outlet.r,preheaterAndBoiler.outlet.state.T,preheaterAndBoiler.outlet.state.d,preheaterAndBoiler.outlet.state.h,preheaterAndBoiler.outlet.state.p,preheaterAndBoiler.outlet.state.phase,preheaterAndBoiler.outletSpec,preheaterAndBoiler.outletSpec_actual,preheaterAndBoiler.outletSpec_prescribed,preheaterAndBoiler.outletValueSpec,preheaterAndBoiler.p,preheaterAndBoiler.p_in,preheaterAndBoiler.p_inf,preheaterAndBoiler.p_min,preheaterAndBoiler.p_out,preheaterAndBoiler.q,preheaterAndBoiler.rho_in,preheaterAndBoiler.rho_out,preheaterAndBoiler.singularityRegime,preheaterAndBoiler.systemSpec,preheaterAndBoiler.u_in,preheaterAndBoiler.u_out,preheaterAndBoiler.v_in,preheaterAndBoiler.v_out,preheaterAndBoiler.w_amb,preheaterAndBoiler.w_exp,preheaterAndBoiler.w_exp_net,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.outletSpec_prescribed,pump.outletValueSpec,pump.pRatio,pump.pRatio_fixed,pump.p_in,pump.p_min,pump.p_out,pump.p_out_fixed,pump.singularityRegime,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: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,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,h_dew.y,outletPressure.duration,outletPressure.height,outletPressure.offset,outletPressure.startTime,outletPressure.y,preheaterAndBoiler.L,preheaterAndBoiler.Q_flow,preheaterAndBoiler.clip_p_out,preheaterAndBoiler.dT,preheaterAndBoiler.dh,preheaterAndBoiler.dp,preheaterAndBoiler.dr_corr,preheaterAndBoiler.h_in,preheaterAndBoiler.h_out,preheaterAndBoiler.initM_flow,preheaterAndBoiler.inlet.m_flow,preheaterAndBoiler.inlet.r,preheaterAndBoiler.inlet.state.T,preheaterAndBoiler.inlet.state.d,preheaterAndBoiler.inlet.state.h,preheaterAndBoiler.inlet.state.p,preheaterAndBoiler.inlet.state.phase,preheaterAndBoiler.m_acceleration_0,preheaterAndBoiler.m_flow,preheaterAndBoiler.m_flowStateSelect,preheaterAndBoiler.m_flow_0,preheaterAndBoiler.outlet.m_flow,preheaterAndBoiler.outlet.r,preheaterAndBoiler.outlet.state.T,preheaterAndBoiler.outlet.state.d,preheaterAndBoiler.outlet.state.h,preheaterAndBoiler.outlet.state.p,preheaterAndBoiler.outlet.state.phase,preheaterAndBoiler.outletSpec,preheaterAndBoiler.outletSpec_actual,preheaterAndBoiler.outletSpec_prescribed,preheaterAndBoiler.outletValueSpec,preheaterAndBoiler.p,preheaterAndBoiler.p_in,preheaterAndBoiler.p_min,preheaterAndBoiler.p_out,preheaterAndBoiler.q,preheaterAndBoiler.singularityRegime,preheaterAndBoiler.systemSpec,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.outletSpec_prescribed,pump.outletValueSpec,pump.pRatio,pump.p_in,pump.p_min,pump.p_out,pump.singularityRegime,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: 8.391589745879173]