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]
"Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.1.0+maint.om/package.mo): time 0.001153/0.001153, allocations: 90.56 kB / 20.21 MB, free: 4.055 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 0.0008371/0.0008371, allocations: 169.3 kB / 23.54 MB, free: 0.7344 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 0.8551/0.8551, allocations: 177.1 MB / 203.9 MB, free: 5.59 MB / 186.7 MB
"
[Timeout remaining time 179]
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 0.6539/0.6539, allocations: 118.6 MB / 379 MB, free: 1.461 MB / 346.7 MB
"
[Timeout remaining time 179]
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: 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_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_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop") [Timeout 660]
"Notification: Performance of FrontEnd - loaded program: time 1.232e-06/1.232e-06, allocations: 0 / 483.7 MB, free: 8.219 MB / 410.7 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 1.321e-05/1.444e-05, allocations: 2.312 kB / 483.7 MB, free: 8.215 MB / 410.7 MB
Notification: Performance of NFInst.instantiate(ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop): time 0.03157/0.03158, allocations: 50.99 MB / 0.5222 GB, free: 13.89 MB / 458.7 MB
Notification: Performance of NFInst.instExpressions: time 0.01537/0.04695, allocations: 19.24 MB / 0.5409 GB, free: 10.59 MB / 474.7 MB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0004359/0.04739, allocations: 51.5 kB / 0.541 GB, free: 10.54 MB / 474.7 MB
Notification: Performance of NFTyping.typeComponents: time 0.0008902/0.04828, allocations: 488.4 kB / 0.5415 GB, free: 10.06 MB / 474.7 MB
Notification: Performance of NFTyping.typeBindings: time 0.01116/0.05944, allocations: 7.286 MB / 0.5486 GB, free: 2.742 MB / 474.7 MB
Notification: Performance of NFTyping.typeClassSections: time 0.002167/0.06161, allocations: 1.209 MB / 0.5498 GB, free: 1.527 MB / 474.7 MB
Notification: Performance of NFFlatten.flatten: time 0.0009626/0.06257, allocations: 1.439 MB / 0.5512 GB, free: 80 kB / 474.7 MB
Notification: Performance of NFFlatten.resolveConnections: time 0.0002011/0.06277, allocations: 127.4 kB / 0.5513 GB, free: 15.94 MB / 490.7 MB
Notification: Performance of NFEvalConstants.evaluate: time 0.00466/0.06743, allocations: 3.982 MB / 0.5552 GB, free: 11.9 MB / 490.7 MB
Notification: Performance of NFSimplifyModel.simplify: time 0.0003371/0.06777, allocations: 362.8 kB / 0.5555 GB, free: 11.55 MB / 490.7 MB
Notification: Performance of NFPackage.collectConstants: time 5.999e-05/0.06783, allocations: 63.98 kB / 0.5556 GB, free: 11.48 MB / 490.7 MB
Notification: Performance of NFFlatten.collectFunctions: time 0.01197/0.07979, allocations: 10.3 MB / 0.5656 GB, free: 1.168 MB / 490.7 MB
Notification: Performance of NFScalarize.scalarize: time 0.0001112/0.0799, allocations: 167.1 kB / 0.5658 GB, free: 1.004 MB / 490.7 MB
Notification: Performance of NFVerifyModel.verify: time 0.0002113/0.08012, allocations: 311.2 kB / 0.5661 GB, free: 0.6992 MB / 490.7 MB
Notification: Performance of NFConvertDAE.convert: time 0.007895/0.08801, allocations: 8.808 MB / 0.5747 GB, free: 7.867 MB / 0.4948 GB
Notification: Performance of FrontEnd - DAE generated: time 3.626e-06/0.08801, allocations: 0 / 0.5747 GB, free: 7.867 MB / 0.4948 GB
Notification: Performance of FrontEnd: time 1.212e-06/0.08802, allocations: 0 / 0.5747 GB, free: 7.867 MB / 0.4948 GB
Notification: Performance of Transformations before backend: time 9.578e-06/0.08803, allocations: 0 / 0.5747 GB, free: 7.867 MB / 0.4948 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 0.002673/0.0907, allocations: 2.112 MB / 0.5768 GB, free: 5.715 MB / 0.4948 GB
Notification: Performance of prepare preOptimizeDAE: time 3.719e-05/0.09074, allocations: 8.031 kB / 0.5768 GB, free: 5.707 MB / 0.4948 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.0008198/0.09156, allocations: 379.6 kB / 0.5771 GB, free: 5.336 MB / 0.4948 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.001006/0.09256, allocations: 0.6733 MB / 0.5778 GB, free: 4.633 MB / 0.4948 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.0001037/0.09267, allocations: 161.3 kB / 0.5779 GB, free: 4.453 MB / 0.4948 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 6.471e-05/0.09273, allocations: 68.38 kB / 0.578 GB, free: 4.387 MB / 0.4948 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.0009692/0.0937, allocations: 0.8009 MB / 0.5788 GB, free: 3.539 MB / 0.4948 GB
Notification: Performance of preOpt findStateOrder (simulation): time 1.27e-05/0.09371, allocations: 0 / 0.5788 GB, free: 3.539 MB / 0.4948 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 3.566e-05/0.09375, allocations: 31.94 kB / 0.5788 GB, free: 3.508 MB / 0.4948 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 1.117e-05/0.09376, allocations: 16 kB / 0.5788 GB, free: 3.492 MB / 0.4948 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.0008293/0.09459, allocations: 0.5905 MB / 0.5794 GB, free: 2.902 MB / 0.4948 GB
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.001956/0.09654, allocations: 2.445 MB / 0.5818 GB, free: 388 kB / 0.4948 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.0007919/0.09734, allocations: 496.4 kB / 0.5823 GB, free: 15.89 MB / 0.5105 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.0002033/0.09754, allocations: 182.3 kB / 0.5824 GB, free: 15.71 MB / 0.5105 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.05857/0.1561, allocations: 34.98 MB / 0.6166 GB, free: 12.7 MB / 0.5417 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 3.48e-05/0.1561, allocations: 47 kB / 0.6167 GB, free: 12.64 MB / 0.5417 GB
Notification: Performance of pre-optimization done (n=47): time 2.084e-06/0.1561, allocations: 0 / 0.6167 GB, free: 12.64 MB / 0.5417 GB
Notification: Performance of matching and sorting (n=47): time 0.001721/0.1579, allocations: 0.8715 MB / 0.6175 GB, free: 11.76 MB / 0.5417 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 2.211e-05/0.1579, allocations: 59.91 kB / 0.6176 GB, free: 11.69 MB / 0.5417 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.0005185/0.1584, allocations: 0.6254 MB / 0.6182 GB, free: 11.05 MB / 0.5417 GB
Notification: Performance of collectPreVariables (initialization): time 2.344e-05/0.1584, allocations: 33.7 kB / 0.6182 GB, free: 11.02 MB / 0.5417 GB
Notification: Performance of collectInitialEqns (initialization): time 0.0002103/0.1586, allocations: 440.3 kB / 0.6186 GB, free: 10.58 MB / 0.5417 GB
Notification: Performance of collectInitialBindings (initialization): time 8.191e-05/0.1587, allocations: 170.5 kB / 0.6188 GB, free: 10.41 MB / 0.5417 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.0001071/0.1588, allocations: 110.3 kB / 0.6189 GB, free: 10.3 MB / 0.5417 GB
Notification: Performance of setup shared object (initialization): time 0.0001184/0.159, allocations: 382.8 kB / 0.6193 GB, free: 9.918 MB / 0.5417 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0001693/0.1591, allocations: 129.2 kB / 0.6194 GB, free: 9.789 MB / 0.5417 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.0004909/0.1596, allocations: 298.6 kB / 0.6197 GB, free: 9.426 MB / 0.5417 GB
Notification: Performance of analyzeInitialSystem (initialization): time 0.0004412/0.1601, allocations: 471.4 kB / 0.6201 GB, free: 8.898 MB / 0.5417 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 3.607e-06/0.1601, allocations: 0 / 0.6201 GB, free: 8.898 MB / 0.5417 GB
Notification: Performance of matching and sorting (n=69) (initialization): time 0.0006735/0.1607, allocations: 0.6225 MB / 0.6207 GB, free: 8.262 MB / 0.5417 GB
Notification: Performance of prepare postOptimizeDAE: time 2.125e-05/0.1608, allocations: 8 kB / 0.6207 GB, free: 8.254 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 1.019e-05/0.1608, allocations: 4 kB / 0.6207 GB, free: 8.25 MB / 0.5417 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.0002726/0.161, allocations: 81.27 kB / 0.6208 GB, free: 8.168 MB / 0.5417 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0002355/0.1613, allocations: 111.8 kB / 0.6209 GB, free: 8.059 MB / 0.5417 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.001021/0.1623, allocations: 1.546 MB / 0.6224 GB, free: 6.406 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.0002078/0.1625, allocations: 59.61 kB / 0.6225 GB, free: 6.348 MB / 0.5417 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 3.057e-05/0.1625, allocations: 24 kB / 0.6225 GB, free: 6.324 MB / 0.5417 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 0.0002159/0.1627, allocations: 211.3 kB / 0.6227 GB, free: 6.109 MB / 0.5417 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 8.598e-05/0.1628, allocations: 95.48 kB / 0.6228 GB, free: 6.016 MB / 0.5417 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.001255/0.1641, allocations: 1.688 MB / 0.6244 GB, free: 4.312 MB / 0.5417 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 7.775e-06/0.1641, allocations: 3.984 kB / 0.6245 GB, free: 4.309 MB / 0.5417 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 2.945e-06/0.1641, allocations: 0 / 0.6245 GB, free: 4.309 MB / 0.5417 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.0001552/0.1643, allocations: 150.9 kB / 0.6246 GB, free: 4.16 MB / 0.5417 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 4.614e-05/0.1643, allocations: 23.89 kB / 0.6246 GB, free: 4.137 MB / 0.5417 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.0001271/0.1644, allocations: 8 kB / 0.6246 GB, free: 4.129 MB / 0.5417 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 4.64e-05/0.1645, allocations: 40.42 kB / 0.6247 GB, free: 4.09 MB / 0.5417 GB
Notification: Performance of postOpt createDAEmodeBDAE (simulation): time 0.0008346/0.1653, allocations: 0.8937 MB / 0.6255 GB, free: 3.191 MB / 0.5417 GB
Notification: Performance of postOpt symbolicJacobianDAE (simulation): time 0.001263/0.1666, allocations: 1.373 MB / 0.6269 GB, free: 1.797 MB / 0.5417 GB
Notification: Performance of postOpt setEvaluationStage (simulation): time 0.0002439/0.1668, allocations: 284.7 kB / 0.6272 GB, free: 1.523 MB / 0.5417 GB
Notification: Performance of sorting global known variables: time 0.0004057/0.1672, allocations: 0.5068 MB / 0.6276 GB, free: 1.023 MB / 0.5417 GB
Notification: Performance of Backend: time 3.81e-07/0.1672, allocations: 0 / 0.6276 GB, free: 1.023 MB / 0.5417 GB
Notification: Performance of simCode: created initialization part: time 0.006156/0.1734, allocations: 2.972 MB / 0.6305 GB, free: 14.02 MB / 0.5573 GB
Notification: Performance of SimCode: time 0.002105/0.1755, allocations: 2.285 MB / 0.6328 GB, free: 11.7 MB / 0.5573 GB
Notification: Performance of Templates: time 0.1985/0.374, allocations: 71.7 MB / 0.7028 GB, free: 126.4 MB / 0.5573 GB
"
[Timeout remaining time 660]
make -j1 -f ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.makefile [Timeout 660]
(rm -f ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe ; mkfifo ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe ; head -c 1048576 < ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe >> ../files/ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.sim & ./ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop  -abortSlowSimulation -alarm=1200  -emit_protected -lv LOG_STATS > ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop.pipe 2>&1) [Timeout 1200]
diffSimulationResults("ThermofluidStream_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_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_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 dropOfCommons.instanceNameColor[1] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[1] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[2] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[2] from file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat failed!
Error: Could not read variable dropOfCommons.instanceNameColor[3] in file ThermofluidStream_ThermofluidStream.Idealized.Examples.ClausiusRankine.Step1OpenLoop_res.mat.
Warning: Get data of variable dropOfCommons.instanceNameColor[3] 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]
""

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.iconIsCompression,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.iconIsHeating,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.isCycle,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.iconIsCompression,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: 5.941201198962517]