Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr Buildings_10_Buildings.Experimental.DHC.Examples.Combined.SeriesVariableFlow.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/Buildings 10.1.1-maint.10.0.x/package.mo", uses=false)
Using package Buildings with version 10.1.1 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Buildings 10.1.1-maint.10.0.x/package.mo)
Using package Modelica with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo)
Using package Complex with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo)
Using package ModelicaServices with version 4.0.0 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo)
Running command: translateModel(Buildings.Experimental.DHC.Examples.Combined.SeriesVariableFlow,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,variableFilter="time|borFie.TBorAve|bui.1..ets.volMix_a.T|bui.1..ets.volMix_b.T|bui.2..ets.volMix_a.T|bui.2..ets.volMix_b.T|bui.3..ets.volMix_a.T|bui.3..ets.volMix_b.T|ETot.y|EHeaPum.y|EPum.y|EPumETS.y|EPumPla.y|EPumDis.y|EPumSto.y|datDes.mPumDis_flow_nominal|bui.1..ets.hexChi.m1_flow_nominal|bui.2..ets.hexChi.m1_flow_nominal|bui.3..ets.hexChi.m1_flow_nominal|bui.1..ets.proHeaWat.heaPum.m2_flow_nominal|bui.2..ets.proHeaWat.heaPum.m2_flow_nominal|bui.3..ets.proHeaWat.heaPum.m2_flow_nominal|bui.1..ets.proHotWat.heaPum.m2_flow_nominal|bui.2..ets.proHotWat.heaPum.m2_flow_nominal|bui.3..ets.proHotWat.heaPum.m2_flow_nominal|bui.1..ets.proHeaWat.heaPum.COP|bui.1..ets.proHotWat.heaPum.COP|bui.2..ets.proHeaWat.heaPum.COP|bui.2..ets.proHotWat.heaPum.COP|bui.3..ets.proHeaWat.heaPum.COP|bui.3..ets.proHotWat.heaPum.COP|TDisWatSup.T|TDisWatRet.T|TDisWatBorLvg.T|pla.dH_flow|borFie.Q_flow|bui.1..ets.PHea|bui.2..ets.PHea|bui.3..ets.PHea|bui.1..ets.PPum|bui.2..ets.PPum|bui.3..ets.PPum|dis.mCon_flow.1.|dis.mCon_flow.2.|dis.mCon_flow.3.|bui.1..ets.THeaWatSupSet|bui.1..ets.senTHeaWatSup.T|bui.2..ets.THeaWatSupSet|bui.2..ets.senTHeaWatSup.T|bui.3..ets.THeaWatSupSet|bui.3..ets.senTHeaWatSup.T|bui.1..ets.senMasFloHeaWat.m_flow|bui.2..ets.senMasFloHeaWat.m_flow|bui.3..ets.senMasFloHeaWat.m_flow|bui.1..ets.TChiWatSupSet|bui.1..ets.senTChiWatSup.T|bui.2..ets.TChiWatSupSet|bui.2..ets.senTChiWatSup.T|bui.3..ets.TChiWatSupSet|bui.3..ets.senTChiWatSup.T|bui.1..ets.senMasFloChiWat.m_flow|bui.2..ets.senMasFloChiWat.m_flow|bui.3..ets.senMasFloChiWat.m_flow",fileNamePrefix="Buildings_10_Buildings.Experimental.DHC.Examples.Combined.SeriesVariableFlow")
translateModel(Buildings.Experimental.DHC.Examples.Combined.SeriesVariableFlow,tolerance=1e-06,outputFormat="mat",numberOfIntervals=5000,variableFilter="time|borFie.TBorAve|bui.1..ets.volMix_a.T|bui.1..ets.volMix_b.T|bui.2..ets.volMix_a.T|bui.2..ets.volMix_b.T|bui.3..ets.volMix_a.T|bui.3..ets.volMix_b.T|ETot.y|EHeaPum.y|EPum.y|EPumETS.y|EPumPla.y|EPumDis.y|EPumSto.y|datDes.mPumDis_flow_nominal|bui.1..ets.hexChi.m1_flow_nominal|bui.2..ets.hexChi.m1_flow_nominal|bui.3..ets.hexChi.m1_flow_nominal|bui.1..ets.proHeaWat.heaPum.m2_flow_nominal|bui.2..ets.proHeaWat.heaPum.m2_flow_nominal|bui.3..ets.proHeaWat.heaPum.m2_flow_nominal|bui.1..ets.proHotWat.heaPum.m2_flow_nominal|bui.2..ets.proHotWat.heaPum.m2_flow_nominal|bui.3..ets.proHotWat.heaPum.m2_flow_nominal|bui.1..ets.proHeaWat.heaPum.COP|bui.1..ets.proHotWat.heaPum.COP|bui.2..ets.proHeaWat.heaPum.COP|bui.2..ets.proHotWat.heaPum.COP|bui.3..ets.proHeaWat.heaPum.COP|bui.3..ets.proHotWat.heaPum.COP|TDisWatSup.T|TDisWatRet.T|TDisWatBorLvg.T|pla.dH_flow|borFie.Q_flow|bui.1..ets.PHea|bui.2..ets.PHea|bui.3..ets.PHea|bui.1..ets.PPum|bui.2..ets.PPum|bui.3..ets.PPum|dis.mCon_flow.1.|dis.mCon_flow.2.|dis.mCon_flow.3.|bui.1..ets.THeaWatSupSet|bui.1..ets.senTHeaWatSup.T|bui.2..ets.THeaWatSupSet|bui.2..ets.senTHeaWatSup.T|bui.3..ets.THeaWatSupSet|bui.3..ets.senTHeaWatSup.T|bui.1..ets.senMasFloHeaWat.m_flow|bui.2..ets.senMasFloHeaWat.m_flow|bui.3..ets.senMasFloHeaWat.m_flow|bui.1..ets.TChiWatSupSet|bui.1..ets.senTChiWatSup.T|bui.2..ets.TChiWatSupSet|bui.2..ets.senTChiWatSup.T|bui.3..ets.TChiWatSupSet|bui.3..ets.senTChiWatSup.T|bui.1..ets.senMasFloChiWat.m_flow|bui.2..ets.senMasFloChiWat.m_flow|bui.3..ets.senMasFloChiWat.m_flow",fileNamePrefix="Buildings_10_Buildings.Experimental.DHC.Examples.Combined.SeriesVariableFlow")
Thread is still alive.
OMC died, but the thread is still running? This will end badly. The log-file of omc:
Created ZeroMQ Server.
Dumped server port in file: /tmp/openmodelica.hudson.port.c752f059750a4625aef59545ba67618c
Linear iteration variables with predefined start attributes that are unrelevant in NLSJac6. (3)
========================================
1: bui[3].bui.terUniCoo.hexWetNtu.port_a2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[3].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
2: bui[3].bui.terUniCoo.hexWetNtu.port_b2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[3].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
3: bui[3].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T:VARIABLE(min = 1.0 max = 1e4 start = 293.15 unit = "K" nominal = 300.0 protected = true final = true )  "Temperature of the fluid" type: Real [3]

Info: Only non-linear iteration variables in non-linear eqation systems require start values. All other start values have no influence on convergence and are ignored. Use "-d=dumpLoops" to show all loops. In OMEdit Tools->Options->Simulation->Additional Translation Flags, in OMNotebook call setCommandLineOptions("-d=dumpLoops")


Linear iteration variables with predefined start attributes that are unrelevant in NLSJac13. (3)
========================================
1: bui[2].bui.terUniCoo.hexWetNtu.port_a2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[2].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
2: bui[2].bui.terUniCoo.hexWetNtu.port_b2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[2].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
3: bui[2].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T:VARIABLE(min = 1.0 max = 1e4 start = 293.15 unit = "K" nominal = 300.0 protected = true final = true )  "Temperature of the fluid" type: Real [3]

Info: Only non-linear iteration variables in non-linear eqation systems require start values. All other start values have no influence on convergence and are ignored. Use "-d=dumpLoops" to show all loops. In OMEdit Tools->Options->Simulation->Additional Translation Flags, in OMNotebook call setCommandLineOptions("-d=dumpLoops")


Linear iteration variables with predefined start attributes that are unrelevant in NLSJac20. (3)
========================================
1: bui[1].bui.terUniCoo.hexWetNtu.port_a2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
2: bui[1].bui.terUniCoo.hexWetNtu.port_b2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
3: bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T:VARIABLE(min = 1.0 max = 1e4 start = bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T_start unit = "K" nominal = 300.0 protected = true final = true )  "Temperature of the fluid" type: Real [3]

Info: Only non-linear iteration variables in non-linear eqation systems require start values. All other start values have no influence on convergence and are ignored. Use "-d=dumpLoops" to show all loops. In OMEdit Tools->Options->Simulation->Additional Translation Flags, in OMNotebook call setCommandLineOptions("-d=dumpLoops")


Linear iteration variables with predefined start attributes that are unrelevant in NLSJac64. (3)
========================================
1: bui[3].bui.terUniCoo.hexWetNtu.port_a2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[3].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
2: bui[3].bui.terUniCoo.hexWetNtu.port_b2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[3].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
3: bui[3].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T:VARIABLE(min = 1.0 max = 1e4 start = 293.15 unit = "K" nominal = 300.0 protected = true final = true )  "Temperature of the fluid" type: Real [3]

Info: Only non-linear iteration variables in non-linear eqation systems require start values. All other start values have no influence on convergence and are ignored. Use "-d=dumpLoops" to show all loops. In OMEdit Tools->Options->Simulation->Additional Translation Flags, in OMNotebook call setCommandLineOptions("-d=dumpLoops")


Linear iteration variables with predefined start attributes that are unrelevant in NLSJac69. (3)
========================================
1: bui[2].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.hOut_internal:VARIABLE(flow=false start = 45300.945 unit = "J/kg" protected = true )  "Internal connector for leaving temperature of the component" type: Real [3]
2: bui[2].bui.terUniCoo.hexWetNtu.port_a2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[2].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
3: bui[2].bui.terUniCoo.hexWetNtu.port_b2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[2].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]

Info: Only non-linear iteration variables in non-linear eqation systems require start values. All other start values have no influence on convergence and are ignored. Use "-d=dumpLoops" to show all loops. In OMEdit Tools->Options->Simulation->Additional Translation Flags, in OMNotebook call setCommandLineOptions("-d=dumpLoops")


Linear iteration variables with predefined start attributes that are unrelevant in NLSJac74. (3)
========================================
1: bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.hOut_internal:VARIABLE(flow=false start = 1006.0 * (-273.15 + bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T_start) * (1.0 - bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.X_start[1]) + (2.5010145e6 + 1860.0 * (-273.15 + bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.T_start)) * bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.vol.X_start[1] unit = "J/kg" protected = true )  "Internal connector for leaving temperature of the component" type: Real [3]
2: bui[1].bui.terUniCoo.hexWetNtu.port_a2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]
3: bui[1].bui.terUniCoo.hexWetNtu.port_b2.h_outflow:VARIABLE(min = -1e10 max = 1e10 start = bui[1].bui.terUniCoo.hexWetNtu.heaCooHum_u.h_outflow_start unit = "J/kg" nominal = 45300.945 )  "Specific thermodynamic enthalpy close to the connection point if m_flow < 0" type: Real [3]

Info: Only non-linear iteration variables in non-linear eqation systems require start values. All other start values have no influence on convergence and are ignored. Use "-d=dumpLoops" to show all loops. In OMEdit Tools->Options->Simulation->Additional Translation Flags, in OMNotebook call setCommandLineOptions("-d=dumpLoops")

Segmentation fault (core dumped)
Aborted the command.
Failed to read output from testmodel.py, exit status != 0:
OMC died, but the thread is still running? This will end badly.