Running: ./testmodel.py --libraries=/home/hudson/saved_omc/libraries/.openmodelica/libraries --ompython_omhome=/usr ClaRa_dev_ClaRa.Components.HeatExchangers.Check.Test_HEXvle2gas_L3_1ph_BU.conf.json
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo", uses=false)
loadFile("/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo", uses=false)
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/ClaRa 1.8.2-main/package.mo", uses=false)
Using package ClaRa with version 1.8.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/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)
Using package TILMedia with version 1.8.1 ClaRa (/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo)
Using package SMArtIInt with version 0.2.2 (/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo)
Running command: translateModel(ClaRa.Components.HeatExchangers.Check.Test_HEXvle2gas_L3_1ph_BU,tolerance=1e-05,outputFormat="mat",numberOfIntervals=5000,variableFilter="CPUtime|EventCounter|NonlinearSystems.initialization.1..Calls|NonlinearSystems.initialization.1..Iterations|NonlinearSystems.initialization.1..Jacobians|NonlinearSystems.initialization.1..Residues|NonlinearSystems.initialization.2..Calls|NonlinearSystems.initialization.2..Iterations|NonlinearSystems.initialization.2..Jacobians|NonlinearSystems.initialization.2..Residues|NonlinearSystems.initialization.3..Calls|NonlinearSystems.initialization.3..Iterations|NonlinearSystems.initialization.3..Jacobians|NonlinearSystems.initialization.3..Residues|NonlinearSystems.initialization.4..Calls|NonlinearSystems.initialization.4..Iterations|NonlinearSystems.initialization.4..Jacobians|NonlinearSystems.initialization.4..Residues|NonlinearSystems.simulation.1..Calls|NonlinearSystems.simulation.1..Iterations|NonlinearSystems.simulation.1..Jacobians|NonlinearSystems.simulation.1..Residues|NonlinearSystems.simulation.2..Calls|NonlinearSystems.simulation.2..Iterations|NonlinearSystems.simulation.2..Jacobians|NonlinearSystems.simulation.2..Residues|NonlinearSystems.simulation.3..Calls|NonlinearSystems.simulation.3..Iterations|NonlinearSystems.simulation.3..Jacobians|NonlinearSystems.simulation.3..Residues|NonlinearSystems.simulation.4..Calls|NonlinearSystems.simulation.4..Iterations|NonlinearSystems.simulation.4..Jacobians|NonlinearSystems.simulation.4..Residues|NonlinearSystems.simulation.5..Calls|NonlinearSystems.simulation.5..Iterations|NonlinearSystems.simulation.5..Jacobians|NonlinearSystems.simulation.5..Residues|Time|flueGasFlowSource.T_const|flueGasFlowSource.contributeToCycleSummary|flueGasFlowSource.energyType|flueGasFlowSource.eyeOut.T|flueGasFlowSource.eyeOut.h|flueGasFlowSource.eyeOut.m_flow|flueGasFlowSource.eyeOut.p|flueGasFlowSource.eyeOut.s|flueGasFlowSource.eyeOut.xi.1.|flueGasFlowSource.eyeOut.xi.2.|flueGasFlowSource.eyeOut.xi.3.|flueGasFlowSource.eyeOut.xi.4.|flueGasFlowSource.eyeOut.xi.5.|flueGasFlowSource.eyeOut.xi.6.|flueGasFlowSource.eyeOut.xi.7.|flueGasFlowSource.eyeOut.xi.8.|flueGasFlowSource.eyeOut.xi.9.|flueGasFlowSource.eye_int.1..T|flueGasFlowSource.eye_int.1..h|flueGasFlowSource.eye_int.1..m_flow|flueGasFlowSource.eye_int.1..p|flueGasFlowSource.eye_int.1..s|flueGasFlowSource.eye_int.1..xi.1.|flueGasFlowSource.eye_int.1..xi.2.|flueGasFlowSource.eye_int.1..xi.3.|flueGasFlowSource.eye_int.1..xi.4.|flueGasFlowSource.eye_int.1..xi.5.|flueGasFlowSource.eye_int.1..xi.6.|flueGasFlowSource.eye_int.1..xi.7.|flueGasFlowSource.eye_int.1..xi.8.|flueGasFlowSource.eye_int.1..xi.9.|flueGasFlowSource.gas_a.T_outflow|flueGasFlowSource.gas_a.m_flow|flueGasFlowSource.gas_a.p|flueGasFlowSource.gas_a.xi_outflow.1.|flueGasFlowSource.gas_a.xi_outflow.2.|flueGasFlowSource.gas_a.xi_outflow.3.|flueGasFlowSource.gas_a.xi_outflow.4.|flueGasFlowSource.gas_a.xi_outflow.5.|flueGasFlowSource.gas_a.xi_outflow.6.|flueGasFlowSource.gas_a.xi_outflow.7.|flueGasFlowSource.gas_a.xi_outflow.8.|flueGasFlowSource.gas_a.xi_outflow.9.|flueGasFlowSource.m_flow_const|flueGasFlowSource.variable_T|flueGasFlowSource.variable_m_flow|flueGasFlowSource.variable_xi|flueGasFlowSource.xi.1.|flueGasFlowSource.xi.2.|flueGasFlowSource.xi.3.|flueGasFlowSource.xi.4.|flueGasFlowSource.xi.5.|flueGasFlowSource.xi.6.|flueGasFlowSource.xi.7.|flueGasFlowSource.xi.8.|flueGasFlowSource.xi.9.|flueGasFlowSource.xi_const.1.|flueGasFlowSource.xi_const.2.|flueGasFlowSource.xi_const.3.|flueGasFlowSource.xi_const.4.|flueGasFlowSource.xi_const.5.|flueGasFlowSource.xi_const.6.|flueGasFlowSource.xi_const.7.|flueGasFlowSource.xi_const.8.|flueGasFlowSource.xi_const.9.|flueGasFlowSource1.T_const|flueGasFlowSource1.contributeToCycleSummary|flueGasFlowSource1.energyType|flueGasFlowSource1.eyeOut.T|flueGasFlowSource1.eyeOut.h|flueGasFlowSource1.eyeOut.m_flow|flueGasFlowSource1.eyeOut.p|flueGasFlowSource1.eyeOut.s|flueGasFlowSource1.eyeOut.xi.1.|flueGasFlowSource1.eyeOut.xi.2.|flueGasFlowSource1.eyeOut.xi.3.|flueGasFlowSource1.eyeOut.xi.4.|flueGasFlowSource1.eyeOut.xi.5.|flueGasFlowSource1.eyeOut.xi.6.|flueGasFlowSource1.eyeOut.xi.7.|flueGasFlowSource1.eyeOut.xi.8.|flueGasFlowSource1.eyeOut.xi.9.|flueGasFlowSource1.eye_int.1..T|flueGasFlowSource1.eye_int.1..h|flueGasFlowSource1.eye_int.1..m_flow|flueGasFlowSource1.eye_int.1..p|flueGasFlowSource1.eye_int.1..s|flueGasFlowSource1.eye_int.1..xi.1.|flueGasFlowSource1.eye_int.1..xi.2.|flueGasFlowSource1.eye_int.1..xi.3.|flueGasFlowSource1.eye_int.1..xi.4.|flueGasFlowSource1.eye_int.1..xi.5.|flueGasFlowSource1.eye_int.1..xi.6.|flueGasFlowSource1.eye_int.1..xi.7.|flueGasFlowSource1.eye_int.1..xi.8.|flueGasFlowSource1.eye_int.1..xi.9.|flueGasFlowSource1.gas_a.T_outflow|flueGasFlowSource1.gas_a.m_flow|flueGasFlowSource1.gas_a.p|flueGasFlowSource1.gas_a.xi_outflow.1.|flueGasFlowSource1.gas_a.xi_outflow.2.|flueGasFlowSource1.gas_a.xi_outflow.3.|flueGasFlowSource1.gas_a.xi_outflow.4.|flueGasFlowSource1.gas_a.xi_outflow.5.|flueGasFlowSource1.gas_a.xi_outflow.6.|flueGasFlowSource1.gas_a.xi_outflow.7.|flueGasFlowSource1.gas_a.xi_outflow.8.|flueGasFlowSource1.gas_a.xi_outflow.9.|flueGasFlowSource1.m_flow_const|flueGasFlowSource1.variable_T|flueGasFlowSource1.variable_m_flow|flueGasFlowSource1.variable_xi|flueGasFlowSource1.xi.1.|flueGasFlowSource1.xi.2.|flueGasFlowSource1.xi.3.|flueGasFlowSource1.xi.4.|flueGasFlowSource1.xi.5.|flueGasFlowSource1.xi.6.|flueGasFlowSource1.xi.7.|flueGasFlowSource1.xi.8.|flueGasFlowSource1.xi.9.|flueGasFlowSource1.xi_const.1.|flueGasFlowSource1.xi_const.2.|flueGasFlowSource1.xi_const.3.|flueGasFlowSource1.xi_const.4.|flueGasFlowSource1.xi_const.5.|flueGasFlowSource1.xi_const.6.|flueGasFlowSource1.xi_const.7.|flueGasFlowSource1.xi_const.8.|flueGasFlowSource1.xi_const.9.|flueGasFlowSource2.T_const|flueGasFlowSource2.contributeToCycleSummary|flueGasFlowSource2.energyType|flueGasFlowSource2.eyeOut.T|flueGasFlowSource2.eyeOut.h|flueGasFlowSource2.eyeOut.m_flow|flueGasFlowSource2.eyeOut.p|flueGasFlowSource2.eyeOut.s|flueGasFlowSource2.eyeOut.xi.1.|flueGasFlowSource2.eyeOut.xi.2.|flueGasFlowSource2.eyeOut.xi.3.|flueGasFlowSource2.eyeOut.xi.4.|flueGasFlowSource2.eyeOut.xi.5.|flueGasFlowSource2.eyeOut.xi.6.|flueGasFlowSource2.eyeOut.xi.7.|flueGasFlowSource2.eyeOut.xi.8.|flueGasFlowSource2.eyeOut.xi.9.|flueGasFlowSource2.eye_int.1..T|flueGasFlowSource2.eye_int.1..h|flueGasFlowSource2.eye_int.1..m_flow|flueGasFlowSource2.eye_int.1..p|flueGasFlowSource2.eye_int.1..s|flueGasFlowSource2.eye_int.1..xi.1.|flueGasFlowSource2.eye_int.1..xi.2.|flueGasFlowSource2.eye_int.1..xi.3.|flueGasFlowSource2.eye_int.1..xi.4.|flueGasFlowSource2.eye_int.1..xi.5.|flueGasFlowSource2.eye_int.1..xi.6.|flueGasFlowSource2.eye_int.1..xi.7.|flueGasFlowSource2.eye_int.1..xi.8.|flueGasFlowSource2.eye_int.1..xi.9.|flueGasFlowSource2.gas_a.T_outflow|flueGasFlowSource2.gas_a.m_flow|flueGasFlowSource2.gas_a.p|flueGasFlowSource2.gas_a.xi_outflow.1.|flueGasFlowSource2.gas_a.xi_outflow.2.|flueGasFlowSource2.gas_a.xi_outflow.3.|flueGasFlowSource2.gas_a.xi_outflow.4.|flueGasFlowSource2.gas_a.xi_outflow.5.|flueGasFlowSource2.gas_a.xi_outflow.6.|flueGasFlowSource2.gas_a.xi_outflow.7.|flueGasFlowSource2.gas_a.xi_outflow.8.|flueGasFlowSource2.gas_a.xi_outflow.9.|flueGasFlowSource2.m_flow_const|flueGasFlowSource2.variable_T|flueGasFlowSource2.variable_m_flow|flueGasFlowSource2.variable_xi|flueGasFlowSource2.xi.1.|flueGasFlowSource2.xi.2.|flueGasFlowSource2.xi.3.|flueGasFlowSource2.xi.4.|flueGasFlowSource2.xi.5.|flueGasFlowSource2.xi.6.|flueGasFlowSource2.xi.7.|flueGasFlowSource2.xi.8.|flueGasFlowSource2.xi.9.|flueGasFlowSource2.xi_const.1.|flueGasFlowSource2.xi_const.2.|flueGasFlowSource2.xi_const.3.|flueGasFlowSource2.xi_const.4.|flueGasFlowSource2.xi_const.5.|flueGasFlowSource2.xi_const.6.|flueGasFlowSource2.xi_const.7.|flueGasFlowSource2.xi_const.8.|flueGasFlowSource2.xi_const.9.|flueGasPressureSink.T_const|flueGasPressureSink.contributeToCycleSummary|flueGasPressureSink.energyType|flueGasPressureSink.eyeOut.T|flueGasPressureSink.eyeOut.h|flueGasPressureSink.eyeOut.m_flow|flueGasPressureSink.eyeOut.p|flueGasPressureSink.eyeOut.s|flueGasPressureSink.eyeOut.xi.1.|flueGasPressureSink.eyeOut.xi.2.|flueGasPressureSink.eyeOut.xi.3.|flueGasPressureSink.eyeOut.xi.4.|flueGasPressureSink.eyeOut.xi.5.|flueGasPressureSink.eyeOut.xi.6.|flueGasPressureSink.eyeOut.xi.7.|flueGasPressureSink.eyeOut.xi.8.|flueGasPressureSink.eyeOut.xi.9.|flueGasPressureSink.eye_int.1..T|flueGasPressureSink.eye_int.1..h|flueGasPressureSink.eye_int.1..m_flow|flueGasPressureSink.eye_int.1..p|flueGasPressureSink.eye_int.1..s|flueGasPressureSink.eye_int.1..xi.1.|flueGasPressureSink.eye_int.1..xi.2.|flueGasPressureSink.eye_int.1..xi.3.|flueGasPressureSink.eye_int.1..xi.4.|flueGasPressureSink.eye_int.1..xi.5.|flueGasPressureSink.eye_int.1..xi.6.|flueGasPressureSink.eye_int.1..xi.7.|flueGasPressureSink.eye_int.1..xi.8.|flueGasPressureSink.eye_int.1..xi.9.|flueGasPressureSink.gas_a.T_outflow|flueGasPressureSink.gas_a.m_flow|flueGasPressureSink.gas_a.p|flueGasPressureSink.gas_a.xi_outflow.1.|flueGasPressureSink.gas_a.xi_outflow.2.|flueGasPressureSink.gas_a.xi_outflow.3.|flueGasPressureSink.gas_a.xi_outflow.4.|flueGasPressureSink.gas_a.xi_outflow.5.|flueGasPressureSink.gas_a.xi_outflow.6.|flueGasPressureSink.gas_a.xi_outflow.7.|flueGasPressureSink.gas_a.xi_outflow.8.|flueGasPressureSink.gas_a.xi_outflow.9.|flueGasPressureSink.p_const|flueGasPressureSink.variable_T|flueGasPressureSink.variable_p|flueGasPressureSink.variable_xi|flueGasPressureSink.xi_const.1.|flueGasPressureSink.xi_const.2.|flueGasPressureSink.xi_const.3.|flueGasPressureSink.xi_const.4.|flueGasPressureSink.xi_const.5.|flueGasPressureSink.xi_const.6.|flueGasPressureSink.xi_const.7.|flueGasPressureSink.xi_const.8.|flueGasPressureSink.xi_const.9.|flueGasPressureSink1.T_const|flueGasPressureSink1.contributeToCycleSummary|flueGasPressureSink1.energyType|flueGasPressureSink1.eyeOut.T|flueGasPressureSink1.eyeOut.h|flueGasPressureSink1.eyeOut.m_flow|flueGasPressureSink1.eyeOut.p|flueGasPressureSink1.eyeOut.s|flueGasPressureSink1.eyeOut.xi.1.|flueGasPressureSink1.eyeOut.xi.2.|flueGasPressureSink1.eyeOut.xi.3.|flueGasPressureSink1.eyeOut.xi.4.|flueGasPressureSink1.eyeOut.xi.5.|flueGasPressureSink1.eyeOut.xi.6.|flueGasPressureSink1.eyeOut.xi.7.|flueGasPressureSink1.eyeOut.xi.8.|flueGasPressureSink1.eyeOut.xi.9.|flueGasPressureSink1.eye_int.1..T|flueGasPressureSink1.eye_int.1..h|flueGasPressureSink1.eye_int.1..m_flow|flueGasPressureSink1.eye_int.1..p|flueGasPressureSink1.eye_int.1..s|flueGasPressureSink1.eye_int.1..xi.1.|flueGasPressureSink1.eye_int.1..xi.2.|flueGasPressureSink1.eye_int.1..xi.3.|flueGasPressureSink1.eye_int.1..xi.4.|flueGasPressureSink1.eye_int.1..xi.5.|flueGasPressureSink1.eye_int.1..xi.6.|flueGasPressureSink1.eye_int.1..xi.7.|flueGasPressureSink1.eye_int.1..xi.8.|flueGasPressureSink1.eye_int.1..xi.9.|flueGasPressureSink1.gas_a.T_outflow|flueGasPressureSink1.gas_a.m_flow|flueGasPressureSink1.gas_a.p|flueGasPressureSink1.gas_a.xi_outflow.1.|flueGasPressureSink1.gas_a.xi_outflow.2.|flueGasPressureSink1.gas_a.xi_outflow.3.|flueGasPressureSink1.gas_a.xi_outflow.4.|flueGasPressureSink1.gas_a.xi_outflow.5.|flueGasPressureSink1.gas_a.xi_outflow.6.|flueGasPressureSink1.gas_a.xi_outflow.7.|flueGasPressureSink1.gas_a.xi_outflow.8.|flueGasPressureSink1.gas_a.xi_outflow.9.|flueGasPressureSink1.p_const|flueGasPressureSink1.variable_T|flueGasPressureSink1.variable_p|flueGasPressureSink1.variable_xi|flueGasPressureSink1.xi_const.1.|flueGasPressureSink1.xi_const.2.|flueGasPressureSink1.xi_const.3.|flueGasPressureSink1.xi_const.4.|flueGasPressureSink1.xi_const.5.|flueGasPressureSink1.xi_const.6.|flueGasPressureSink1.xi_const.7.|flueGasPressureSink1.xi_const.8.|flueGasPressureSink1.xi_const.9.|flueGasPressureSink2.T_const|flueGasPressureSink2.contributeToCycleSummary|flueGasPressureSink2.energyType|flueGasPressureSink2.eyeOut.T|flueGasPressureSink2.eyeOut.h|flueGasPressureSink2.eyeOut.m_flow|flueGasPressureSink2.eyeOut.p|flueGasPressureSink2.eyeOut.s|flueGasPressureSink2.eyeOut.xi.1.|flueGasPressureSink2.eyeOut.xi.2.|flueGasPressureSink2.eyeOut.xi.3.|flueGasPressureSink2.eyeOut.xi.4.|flueGasPressureSink2.eyeOut.xi.5.|flueGasPressureSink2.eyeOut.xi.6.|flueGasPressureSink2.eyeOut.xi.7.|flueGasPressureSink2.eyeOut.xi.8.|flueGasPressureSink2.eyeOut.xi.9.|flueGasPressureSink2.eye_int.1..T|flueGasPressureSink2.eye_int.1..h|flueGasPressureSink2.eye_int.1..m_flow|flueGasPressureSink2.eye_int.1..p|flueGasPressureSink2.eye_int.1..s|flueGasPressureSink2.eye_int.1..xi.1.|flueGasPressureSink2.eye_int.1..xi.2.|flueGasPressureSink2.eye_int.1..xi.3.|flueGasPressureSink2.eye_int.1..xi.4.|flueGasPressureSink2.eye_int.1..xi.5.|flueGasPressureSink2.eye_int.1..xi.6.|flueGasPressureSink2.eye_int.1..xi.7.|flueGasPressureSink2.eye_int.1..xi.8.|flueGasPressureSink2.eye_int.1..xi.9.|flueGasPressureSink2.gas_a.T_outflow|flueGasPressureSink2.gas_a.m_flow|flueGasPressureSink2.gas_a.p|flueGasPressureSink2.gas_a.xi_outflow.1.|flueGasPressureSink2.gas_a.xi_outflow.2.|flueGasPressureSink2.gas_a.xi_outflow.3.|flueGasPressureSink2.gas_a.xi_outflow.4.|flueGasPressureSink2.gas_a.xi_outflow.5.|flueGasPressureSink2.gas_a.xi_outflow.6.|flueGasPressureSink2.gas_a.xi_outflow.7.|flueGasPressureSink2.gas_a.xi_outflow.8.|flueGasPressureSink2.gas_a.xi_outflow.9.|flueGasPressureSink2.p_const|flueGasPressureSink2.variable_T|flueGasPressureSink2.variable_p|flueGasPressureSink2.variable_xi|flueGasPressureSink2.xi_const.1.|flueGasPressureSink2.xi_const.2.|flueGasPressureSink2.xi_const.3.|flueGasPressureSink2.xi_const.4.|flueGasPressureSink2.xi_const.5.|flueGasPressureSink2.xi_const.6.|flueGasPressureSink2.xi_const.7.|flueGasPressureSink2.xi_const.8.|flueGasPressureSink2.xi_const.9.|gasCompositionByMassFractions.X.1.|gasCompositionByMassFractions.X.2.|gasCompositionByMassFractions.X.3.|gasCompositionByMassFractions.X.4.|gasCompositionByMassFractions.X.5.|gasCompositionByMassFractions.X.6.|gasCompositionByMassFractions.X.7.|gasCompositionByMassFractions.X.8.|gasCompositionByMassFractions.X.9.|gasCompositionByMassFractions.sumXi|gasCompositionByMassFractions.xi_ASH|gasCompositionByMassFractions.xi_CO|gasCompositionByMassFractions.xi_CO2|gasCompositionByMassFractions.xi_H2O|gasCompositionByMassFractions.xi_N2|gasCompositionByMassFractions.xi_NH3|gasCompositionByMassFractions.xi_NO|gasCompositionByMassFractions.xi_O2|gasCompositionByMassFractions.xi_SO2|gasCompositionByMassFractions.xi_in.1.|gasCompositionByMassFractions.xi_in.2.|gasCompositionByMassFractions.xi_in.3.|gasCompositionByMassFractions.xi_in.4.|gasCompositionByMassFractions.xi_in.5.|gasCompositionByMassFractions.xi_in.6.|gasCompositionByMassFractions.xi_in.7.|gasCompositionByMassFractions.xi_in.8.|gasCompositionByMassFractions.xi_in.9.|gasTemperatureSensor_hex_2ph.T_ref.1.|gasTemperatureSensor_hex_2ph.T_ref.2.|gasTemperatureSensor_hex_2ph.inlet.T_outflow|gasTemperatureSensor_hex_2ph.inlet.m_flow|gasTemperatur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Outlet.xi_dryGas.7.|hex_2ph.shell.flueGasOutlet.xi_dryGas.8.|hex_2ph.shell.flueGasOutlet.xi_gas|hex_2ph.shell.flueGasOutlet.xi_s|hex_2ph.shell.geo.A_cross|hex_2ph.shell.geo.A_front|hex_2ph.shell.geo.A_heat.1.|hex_2ph.shell.geo.A_heat.2.|hex_2ph.shell.geo.A_heat_CF.1.|hex_2ph.shell.geo.A_heat_CF.2.|hex_2ph.shell.geo.A_hor|hex_2ph.shell.geo.A_narrowed_ort|hex_2ph.shell.geo.A_narrowed_par|hex_2ph.shell.geo.CF_geo.1.|hex_2ph.shell.geo.CF_geo.2.|hex_2ph.shell.geo.Delta_l_ort|hex_2ph.shell.geo.Delta_l_par|hex_2ph.shell.geo.Delta_z_ort|hex_2ph.shell.geo.Delta_z_par|hex_2ph.shell.geo.MIN|hex_2ph.shell.geo.N_heat|hex_2ph.shell.geo.N_inlet|hex_2ph.shell.geo.N_outlet|hex_2ph.shell.geo.N_passes|hex_2ph.shell.geo.N_rows|hex_2ph.shell.geo.N_tubes|hex_2ph.shell.geo.N_tubes_parallel|hex_2ph.shell.geo.a|hex_2ph.shell.geo.b|hex_2ph.shell.geo.diameter_t|hex_2ph.shell.geo.fa|hex_2ph.shell.geo.flowOrientation|hex_2ph.shell.geo.height|hex_2ph.shell.geo.height_fill|hex_2ph.shell.geo.interior|hex_2ph.shell.geo.length|hex_2ph.shell.geo.length_bundle_ort|hex_2ph.shell.geo.length_bundle_par|hex_2ph.shell.geo.length_tubes|hex_2ph.shell.geo.psi|hex_2ph.shell.geo.shape.1,1.|hex_2ph.shell.geo.shape.1,2.|hex_2ph.shell.geo.shape.2,1.|hex_2ph.shell.geo.shape.2,2.|hex_2ph.shell.geo.staggeredAlignment|hex_2ph.shell.geo.tubeOrientation|hex_2ph.shell.geo.volume|hex_2ph.shell.geo.width|hex_2ph.shell.geo.z_in.1.|hex_2ph.shell.geo.z_out.1.|hex_2ph.shell.h_nom|hex_2ph.shell.h_start|hex_2ph.shell.heat.Q_flow|hex_2ph.shell.heat.T|hex_2ph.shell.heatSurfaceAlloc|hex_2ph.shell.heattransfer.A_finned|hex_2ph.shell.heattransfer.A_tubes|hex_2ph.shell.heattransfer.CF_fouling|hex_2ph.shell.heattransfer.Delta_T_L|hex_2ph.shell.heattransfer.Delta_T_U|hex_2ph.shell.heattransfer.Delta_T_mean|hex_2ph.shell.heattransfer.Delta_T_wi|hex_2ph.shell.heattransfer.Delta_T_wo|hex_2ph.shell.heattransfer.HR|hex_2ph.shell.heattransfer.HR_nom|hex_2ph.shell.heattransfer.HT_type|hex_2ph.shell.heattransfer.N_f|hex_2ph.shell.heattransfer.N_tubes_p|hex_2ph.shell.heattransfer.Nu|hex_2ph.shell.heattransfer.Re|hex_2ph.shell.heattransfer.T_f|hex_2ph.shell.heattransfer.alpha|hex_2ph.shell.heattransfer.h_f|hex_2ph.shell.heattransfer.heat.Q_flow|hex_2ph.shell.heattransfer.heat.T|hex_2ph.shell.heattransfer.heatSurfaceAlloc|hex_2ph.shell.heattransfer.s_f|hex_2ph.shell.heattransfer.t_f|hex_2ph.shell.heattransfer.w|hex_2ph.shell.heattransfer.w_0|hex_2ph.shell.initOption|hex_2ph.shell.inlet.T_outflow|hex_2ph.shell.inlet.m_flow|hex_2ph.shell.inlet.p|hex_2ph.shell.inlet.xi_outflow.1.|hex_2ph.shell.inlet.xi_outflow.2.|hex_2ph.shell.inlet.xi_outflow.3.|hex_2ph.shell.inlet.xi_outflow.4.|hex_2ph.shell.inlet.xi_outflow.5.|hex_2ph.shell.inlet.xi_outflow.6.|hex_2ph.shell.inlet.xi_outflow.7.|hex_2ph.shell.inlet.xi_outflow.8.|hex_2ph.shell.inlet.xi_outflow.9.|hex_2ph.shell.m_flow_nom|hex_2ph.shell.outlet.T_outflow|hex_2ph.shell.outlet.m_flow|hex_2ph.shell.outlet.p|hex_2ph.shell.outlet.xi_outflow.1.|hex_2ph.shell.outlet.xi_outflow.2.|hex_2ph.shell.outlet.xi_outflow.3.|hex_2ph.shell.outlet.xi_outflow.4.|hex_2ph.shell.outlet.xi_outflow.5.|hex_2ph.shell.outlet.xi_outflow.6.|hex_2ph.shell.outlet.xi_outflow.7.|hex_2ph.shell.outlet.xi_outflow.8.|hex_2ph.shell.outlet.xi_outflow.9.|hex_2ph.shell.p_nom|hex_2ph.shell.p_start|hex_2ph.shell.pressureLoss.Delta_p|hex_2ph.shell.pressureLoss.Delta_p_nom|hex_2ph.shell.pressureLoss.Delta_p_smooth|hex_2ph.shell.pressureLoss.zeta|hex_2ph.shell.summary.inlet.H_flow|hex_2ph.shell.summary.inlet.T|hex_2ph.shell.summary.inlet.h|hex_2ph.shell.summary.inlet.m_flow|hex_2ph.shell.summary.inlet.p|hex_2ph.shell.summary.inlet.xi.1.|hex_2ph.shell.summary.inlet.xi.2.|hex_2ph.shell.summary.inlet.xi.3.|hex_2ph.shell.summary.inlet.xi.4.|hex_2ph.shell.summary.inlet.xi.5.|hex_2ph.shell.summary.inlet.xi.6.|hex_2ph.shell.summary.inlet.xi.7.|hex_2ph.shell.summary.inlet.xi.8.|hex_2ph.shell.summary.inlet.xi.9.|hex_2ph.shell.summary.outlet.H_flow|hex_2ph.shell.summary.outlet.T|hex_2ph.shell.summary.outlet.h|hex_2ph.shell.summary.outlet.m_flow|hex_2ph.shell.summary.outlet.p|hex_2ph.shell.summary.outlet.xi.1.|hex_2ph.shell.summary.outlet.xi.2.|hex_2ph.shell.summary.outlet.xi.3.|hex_2ph.shell.summary.outlet.xi.4.|hex_2ph.shell.summary.outlet.xi.5.|hex_2ph.shell.summary.outlet.xi.6.|hex_2ph.shell.summary.outlet.xi.7.|hex_2ph.shell.summary.outlet.xi.8.|hex_2ph.shell.summary.outlet.xi.9.|hex_2ph.shell.summary.outline.A_heat|hex_2ph.shell.summary.outline.Delta_p|hex_2ph.shell.summary.outline.H|hex_2ph.shell.summary.outline.Q_flow_tot|hex_2ph.shell.summary.outline.T|hex_2ph.shell.summary.outline.h|hex_2ph.shell.summary.outline.mass|hex_2ph.shell.summary.outline.p|hex_2ph.shell.summary.outline.rho|hex_2ph.shell.summary.outline.volume_tot|hex_2ph.shell.useHomotopy|hex_2ph.shell.use_dynamicMassbalance|hex_2ph.shell.xi_nom.1.|hex_2ph.shell.xi_nom.2.|hex_2ph.shell.xi_nom.3.|hex_2ph.shell.xi_nom.4.|hex_2ph.shell.xi_nom.5.|hex_2ph.shell.xi_nom.6.|hex_2ph.shell.xi_nom.7.|hex_2ph.shell.xi_nom.8.|hex_2ph.shell.xi_nom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ph.tubes.summary.outline.level_rel|hex_2ph.tubes.summary.outline.showExpertSummary|hex_2ph.tubes.summary.outline.volume.1.|hex_2ph.tubes.summary.outline.volume.2.|hex_2ph.tubes.summary.outline.volume_tot|hex_2ph.tubes.summary.outline.yps.1.|hex_2ph.tubes.summary.outline.yps.2.|hex_2ph.tubes.useHomotopy|hex_2ph.tubes.volume_liq|hex_2ph.tubes.volume_vap|hex_2ph.tubes.yps.1.|hex_2ph.tubes.yps.2.|hex_2ph.useHomotopy|hex_2ph.wall.A_heat.1.|hex_2ph.wall.A_heat.2.|hex_2ph.wall.A_heat.3.|hex_2ph.wall.A_heat.4.|hex_2ph.wall.A_heat.5.|hex_2ph.wall.A_heat.6.|hex_2ph.wall.A_heat_m|hex_2ph.wall.A_heat_m_rad.1.|hex_2ph.wall.A_heat_m_rad.2.|hex_2ph.wall.A_heat_m_rad.3.|hex_2ph.wall.CF_lambda|hex_2ph.wall.Delta_radius.1.|hex_2ph.wall.Delta_radius.2.|hex_2ph.wall.Delta_radius.3.|hex_2ph.wall.HR|hex_2ph.wall.HR_nom|hex_2ph.wall.HR_rad.1.|hex_2ph.wall.HR_rad.2.|hex_2ph.wall.HR_rad.3.|hex_2ph.wall.N_passes|hex_2ph.wall.N_rad|hex_2ph.wall.N_tubes|hex_2ph.wall.Q_flow.1.|hex_2ph.wall.Q_flow.2.|hex_2ph.wall.Q_flow.3.|hex_2ph.wall.Q_flow.4.|hex_2ph.wall.T.1.|hex_2ph.wall.T.2.|hex_2ph.wall.T.3.|hex_2ph.wall.T_mean|hex_2ph.wall.T_start.1.|hex_2ph.wall.T_start.2.|hex_2ph.wall.T_start.3.|hex_2ph.wall.Tdr.1.|hex_2ph.wall.Tdr.2.|hex_2ph.wall.Tdr.3.|hex_2ph.wall.Tdr.4.|hex_2ph.wall.U.1.|hex_2ph.wall.U.2.|hex_2ph.wall.U.3.|der.hex_2ph.wall.U.1..|der.hex_2ph.wall.U.2..|der.hex_2ph.wall.U.3..|hex_2ph.wall.diameter_i|hex_2ph.wall.diameter_o|hex_2ph.wall.initOption|hex_2ph.wall.innerPhase.Q_flow|hex_2ph.wall.innerPhase.T|hex_2ph.wall.length|hex_2ph.wall.mass|hex_2ph.wall.mass_struc|hex_2ph.wall.outerPhase.Q_flow|hex_2ph.wall.outerPhase.T|hex_2ph.wall.radius.1.|hex_2ph.wall.radius.2.|hex_2ph.wall.radius.3.|hex_2ph.wall.radius.4.|hex_2ph.wall.radius_m.1.|hex_2ph.wall.radius_m.2.|hex_2ph.wall.radius_m.3.|hex_2ph.wall.radius_m.4.|hex_2ph.wall.radius_m.5.|hex_2ph.wall.radius_m.6.|hex_2ph.wall.radius_v.1.|hex_2ph.wall.radius_v.2.|hex_2ph.wall.radius_v.3.|hex_2ph.wall.radius_v.4.|hex_2ph.wall.radius_v.5.|hex_2ph.wall.sizefunc|hex_2ph.wall.solid.1..T|hex_2ph.wall.solid.1..cp|hex_2ph.wall.solid.1..cp_nominal|hex_2ph.wall.solid.1..d|hex_2ph.wall.solid.1..lambda|hex_2ph.wall.solid.1..lambda_nominal|hex_2ph.wall.solid.2..T|hex_2ph.wall.solid.2..cp|hex_2ph.wall.solid.2..cp_nominal|hex_2ph.wall.solid.2..d|hex_2ph.wall.solid.2..lambda|hex_2ph.wall.solid.2..lambda_nominal|hex_2ph.wall.solid.3..T|hex_2ph.wall.solid.3..cp|hex_2ph.wall.solid.3..cp_nominal|hex_2ph.wall.solid.3..d|hex_2ph.wall.solid.3..lambda|hex_2ph.wall.solid.3..lambda_nominal|hex_2ph.wall.summary.A_heat.1.|hex_2ph.wall.summary.A_heat.2.|hex_2ph.wall.summary.A_heat.3.|hex_2ph.wall.summary.A_heat.4.|hex_2ph.wall.summary.A_heat.5.|hex_2ph.wall.summary.A_heat.6.|hex_2ph.wall.summary.Delta_radius.1.|hex_2ph.wall.summary.Delta_radius.2.|hex_2ph.wall.summary.Delta_radius.3.|hex_2ph.wall.summary.N_A_heat|hex_2ph.wall.summary.N_rad|hex_2ph.wall.summary.N_tubes|hex_2ph.wall.summary.Q_flow.1.|hex_2ph.wall.summary.Q_flow.2.|hex_2ph.wall.summary.Q_flow.3.|hex_2ph.wall.summary.Q_flow.4.|hex_2ph.wall.summary.T.1.|hex_2ph.wall.summary.T.2.|hex_2ph.wall.summary.T.3.|hex_2ph.wall.summary.U.1.|hex_2ph.wall.summary.U.2.|hex_2ph.wall.summary.U.3.|hex_2ph.wall.summary.cp.1.|hex_2ph.wall.summary.cp.2.|hex_2ph.wall.summary.cp.3.|hex_2ph.wall.summary.d.1.|hex_2ph.wall.summary.d.2.|hex_2ph.wall.summary.d.3.|hex_2ph.wall.summary.diameter_i|hex_2ph.wall.summary.diameter_o|hex_2ph.wall.summary.length|hex_2ph.wall.summary.mass|hex_2ph.wall.summary.radius.1.|hex_2ph.wall.summary.radius.2.|hex_2ph.wall.summary.radius.3.|hex_2ph.wall.summary.radius.4.|hex_2ph.wall.summary.radius_m.1.|hex_2ph.wall.summary.radius_m.2.|hex_2ph.wall.summary.radius_m.3.|hex_2ph.wall.summary.radius_m.4.|hex_2ph.wall.summary.radius_m.5.|hex_2ph.wall.summary.radius_m.6.|hex_2ph.wall.summary.radius_v.1.|hex_2ph.wall.summary.radius_v.2.|hex_2ph.wall.summary.radius_v.3.|hex_2ph.wall.summary.radius_v.4.|hex_2ph.wall.summary.radius_v.5.|hex_2ph.width|hex_2ph.width_hotwell|hex_2ph.xi_shell_start.1.|hex_2ph.xi_shell_start.2.|hex_2ph.xi_shell_start.3.|hex_2ph.xi_shell_start.4.|hex_2ph.xi_shell_start.5.|hex_2ph.xi_shell_start.6.|hex_2ph.xi_shell_start.7.|hex_2ph.xi_shell_start.8.|hex_2ph.xi_shell_start.9.|hex_2ph.yps_liq_nom|hex_2ph.yps_nom.1.|hex_2ph.yps_nom.2.|hex_2ph.z_in_shell|hex_2ph.z_in_tubes|hex_2ph.z_out_shell|hex_2ph.z_out_tubes|hex_ntu.CF_geo|hex_ntu.Delta_z_ort|hex_ntu.Delta_z_par|hex_ntu.In1.T_outflow|hex_ntu.In1.m_flow|hex_ntu.In1.p|hex_ntu.In1.xi_outflow.1.|hex_ntu.In1.xi_outflow.2.|hex_ntu.In1.xi_outflow.3.|hex_ntu.In1.xi_outflow.4.|hex_ntu.In1.xi_outflow.5.|hex_ntu.In1.xi_outflow.6.|hex_ntu.In1.xi_outflow.7.|hex_ntu.In1.xi_outflow.8.|hex_ntu.In1.xi_outflow.9.|hex_ntu.In2.h_outflow|hex_ntu.In2.m_flow|hex_ntu.In2.p|hex_ntu.N_passes|hex_ntu.N_rows|hex_ntu.N_tubes|hex_ntu.Out1.T_outflow|hex_ntu.Out1.m_flow|hex_ntu.Out1.p|hex_ntu.Out1.xi_outflow.1.|hex_ntu.Out1.xi_outflow.2.|hex_ntu.Out1.xi_outflow.3.|hex_ntu.Out1.xi_outflow.4.|hex_ntu.Out1.xi_outf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.2.|hex_simple.shell.bulk.xi_dryGas.3.|hex_simple.shell.bulk.xi_dryGas.4.|hex_simple.shell.bulk.xi_dryGas.5.|hex_simple.shell.bulk.xi_dryGas.6.|hex_simple.shell.bulk.xi_dryGas.7.|hex_simple.shell.bulk.xi_dryGas.8.|hex_simple.shell.bulk.xi_gas|hex_simple.shell.bulk.xi_s|hex_simple.shell.flueGasInlet.M|hex_simple.shell.flueGasInlet.M_i.10.|hex_simple.shell.flueGasInlet.M_i.1.|hex_simple.shell.flueGasInlet.M_i.2.|hex_simple.shell.flueGasInlet.M_i.3.|hex_simple.shell.flueGasInlet.M_i.4.|hex_simple.shell.flueGasInlet.M_i.5.|hex_simple.shell.flueGasInlet.M_i.6.|hex_simple.shell.flueGasInlet.M_i.7.|hex_simple.shell.flueGasInlet.M_i.8.|hex_simple.shell.flueGasInlet.M_i.9.|hex_simple.shell.flueGasInlet.T|hex_simple.shell.flueGasInlet.beta|hex_simple.shell.flueGasInlet.computeTransportProperties|hex_simple.shell.flueGasInlet.cp|hex_simple.shell.flueGasInlet.cv|hex_simple.shell.flueGasInlet.d|hex_simple.shell.flueGasInlet.delta_hd|hex_simple.shell.flueGasInlet.delta_hv|hex_simple.shell.flueGasInlet.drhodh_pxi|hex_simple.shell.flueGasInlet.drhodp_hxi|hex_simple.shell.flueGasInlet.drhodxi_ph.1.|hex_simple.shell.flueGasInlet.drhodxi_ph.2.|hex_simple.shell.flueGasInlet.drhodxi_ph.3.|hex_simple.shell.flueGasInlet.drhodxi_ph.4.|hex_simple.shell.flueGasInlet.drhodxi_ph.5.|hex_simple.shell.flueGasInlet.drhodxi_ph.6.|hex_simple.shell.flueGasInlet.drhodxi_ph.7.|hex_simple.shell.flueGasInlet.drhodxi_ph.8.|hex_simple.shell.flueGasInlet.drhodxi_ph.9.|hex_simple.shell.flueGasInlet.gasPointer.id|hex_simple.shell.flueGasInlet.h|hex_simple.shell.flueGasInlet.h1px|hex_simple.shell.flueGasInlet.h_i.10.|hex_simple.shell.flueGasInlet.h_i.1.|hex_simple.shell.flueGasInlet.h_i.2.|hex_simple.shell.flueGasInlet.h_i.3.|hex_simple.shell.flueGasInlet.h_i.4.|hex_simple.shell.flueGasInlet.h_i.5.|hex_simple.shell.flueGasInlet.h_i.6.|hex_simple.shell.flueGasInlet.h_i.7.|hex_simple.shell.flueGasInlet.h_i.8.|hex_simple.shell.flueGasInlet.h_i.9.|hex_simple.shell.flueGasInlet.humRatio|hex_simple.shell.flueGasInlet.humRatio_s|hex_simple.shell.flueGasInlet.kappa|hex_simple.shell.flueGasInlet.p|hex_simple.shell.flueGasInlet.p_i.10.|hex_simple.shell.flueGasInlet.p_i.1.|hex_simple.shell.flueGasInlet.p_i.2.|hex_simple.shell.flueGasInlet.p_i.3.|hex_simple.shell.flueGasInlet.p_i.4.|hex_simple.shell.flueGasInlet.p_i.5.|hex_simple.shell.flueGasInlet.p_i.6.|hex_simple.shell.flueGasInlet.p_i.7.|hex_simple.shell.flueGasInlet.p_i.8.|hex_simple.shell.flueGasInlet.p_i.9.|hex_simple.shell.flueGasInlet.p_s|hex_simple.shell.flueGasInlet.phi|hex_simple.shell.flueGasInlet.s|hex_simple.shell.flueGasInlet.stateSelectPreferForInputs|hex_simple.shell.flueGasInlet.transp.Pr|hex_simple.shell.flueGasInlet.transp.eta|hex_simple.shell.flueGasInlet.transp.lambda|hex_simple.shell.flueGasInlet.transp.sigma|hex_simple.shell.flueGasInlet.w|hex_simple.shell.flueGasInlet.x.1.|hex_simple.shell.flueGasInlet.x.2.|hex_simple.shell.flueGasInlet.x.3.|hex_simple.shell.flueGasInlet.x.4.|hex_simple.shell.flueGasInlet.x.5.|hex_simple.shell.flueGasInlet.x.6.|hex_simple.shell.flueGasInlet.x.7.|hex_simple.shell.flueGasInlet.x.8.|hex_simple.shell.flueGasInlet.x.9.|hex_simple.shell.flueGasInlet.xi.1.|hex_simple.shell.flueGasInlet.xi.2.|hex_simple.shell.flueGasInlet.xi.3.|hex_simple.shell.flueGasInlet.xi.4.|hex_simple.shell.flueGasInlet.xi.5.|hex_simple.shell.flueGasInlet.xi.6.|hex_simple.shell.flueGasInlet.xi.7.|hex_simple.shell.flueGasInlet.xi.8.|hex_simple.shell.flueGasInlet.xi.9.|hex_simple.shell.flueGasInlet.xi_dryGas.1.|hex_simple.shell.flueGasInlet.xi_dryGas.2.|hex_simple.shell.flueGasInlet.xi_dryGas.3.|hex_simple.shell.flueGasInlet.xi_dryGas.4.|hex_simple.shell.flueGasInlet.xi_dryGas.5.|hex_simple.shell.flueGasInlet.xi_dryGas.6.|hex_simple.shell.flueGasInlet.xi_dryGas.7.|hex_simple.shell.flueGasInlet.xi_dryGas.8.|hex_simple.shell.flueGasInlet.xi_gas|hex_simple.shell.flueGasInlet.xi_s|hex_simple.shell.flueGasOutlet.M|hex_simple.shell.flueGasOutlet.M_i.10.|hex_simple.shell.flueGasOutlet.M_i.1.|hex_simple.shell.flueGasOutlet.M_i.2.|hex_simple.shell.flueGasOutlet.M_i.3.|hex_simple.shell.flueGasOutlet.M_i.4.|hex_simple.shell.flueGasOutlet.M_i.5.|hex_simple.shell.flueGasOutlet.M_i.6.|hex_simple.shell.flueGasOutlet.M_i.7.|hex_simple.shell.flueGasOutlet.M_i.8.|hex_simple.shell.flueGasOutlet.M_i.9.|hex_simple.shell.flueGasOutlet.T|hex_simple.shell.flueGasOutlet.beta|hex_simple.shell.flueGasOutlet.computeTransportProperties|hex_simple.shell.flueGasOutlet.cp|hex_simple.shell.flueGasOutlet.cv|hex_simple.shell.flueGasOutlet.d|hex_simple.shell.flueGasOutlet.delta_hd|hex_simple.shell.flueGasOutlet.delta_hv|hex_simple.shell.flueGasOutlet.drhodh_pxi|hex_simple.shell.flueGasOutlet.drhodp_hxi|hex_simple.shell.flueGasOutlet.drhodxi_ph.1.|hex_simple.shell.flueGasOutlet.drhodxi_ph.2.|hex_simple.shell.flueGasOutlet.drhodxi_ph.3.|hex_simple.shell.flueGasOutlet.drhodxi_ph.4.|hex_simple.shell.flueGasOutlet.drhodxi_ph.5.|hex_simple.shell.flueGasOutlet.drhodxi_ph.6.|hex_simple.shell.flueGasOutlet.drhodxi_ph.7.|hex_simple.shel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ensityDerivatives|hex_simple.tubes.fluidIn.deactivateTwoPhaseRegion|hex_simple.tubes.fluidIn.drhodh_pxi|hex_simple.tubes.fluidIn.drhodp_hxi|hex_simple.tubes.fluidIn.gamma|hex_simple.tubes.fluidIn.h|hex_simple.tubes.fluidIn.interpolateTransportProperties|hex_simple.tubes.fluidIn.kappa|hex_simple.tubes.fluidIn.p|hex_simple.tubes.fluidIn.q|hex_simple.tubes.fluidIn.s|hex_simple.tubes.fluidIn.stateSelectPreferForInputs|hex_simple.tubes.fluidIn.transp.Pr|hex_simple.tubes.fluidIn.transp.eta|hex_simple.tubes.fluidIn.transp.lambda|hex_simple.tubes.fluidIn.transp.sigma|hex_simple.tubes.fluidIn.vleFluidPointer.id|hex_simple.tubes.fluidIn.w|hex_simple.tubes.fluidOut.M|hex_simple.tubes.fluidOut.M_i.1.|hex_simple.tubes.fluidOut.T|hex_simple.tubes.fluidOut.VLE.T_l|hex_simple.tubes.fluidOut.VLE.T_v|hex_simple.tubes.fluidOut.VLE.d_l|hex_simple.tubes.fluidOut.VLE.d_v|hex_simple.tubes.fluidOut.VLE.h_l|hex_simple.tubes.fluidOut.VLE.h_v|hex_simple.tubes.fluidOut.VLE.nc|hex_simple.tubes.fluidOut.VLE.p_l|hex_simple.tubes.fluidOut.VLE.p_v|hex_simple.tubes.fluidOut.VLE.s_l|hex_simple.tubes.fluidOut.VLE.s_v|hex_simple.tubes.fluidOut.VLEAdditional.beta_l|hex_simple.tubes.fluidOut.VLEAdditional.beta_v|hex_simple.tubes.fluidOut.VLEAdditional.cp_l|hex_simple.tubes.fluidOut.VLEAdditional.cp_v|hex_simple.tubes.fluidOut.VLEAdditional.kappa_l|hex_simple.tubes.fluidOut.VLEAdditional.kappa_v|hex_simple.tubes.fluidOut.VLETransp.Pr_l|hex_simple.tubes.fluidOut.VLETransp.Pr_v|hex_simple.tubes.fluidOut.VLETransp.eta_l|hex_simple.tubes.fluidOut.VLETransp.eta_v|hex_simple.tubes.fluidOut.VLETransp.lambda_l|hex_simple.tubes.fluidOut.VLETransp.lambda_v|hex_simple.tubes.fluidOut.beta|hex_simple.tubes.fluidOut.computeSurfaceTension|hex_simple.tubes.fluidOut.computeTransportProperties|hex_simple.tubes.fluidOut.computeVLEAdditionalProperties|hex_simple.tubes.fluidOut.computeVLETransportProperties|hex_simple.tubes.fluidOut.cp|hex_simple.tubes.fluidOut.crit.T|hex_simple.tubes.fluidOut.crit.d|hex_simple.tubes.fluidOut.crit.h|hex_simple.tubes.fluidOut.crit.p|hex_simple.tubes.fluidOut.crit.s|hex_simple.tubes.fluidOut.cv|hex_simple.tubes.fluidOut.d|hex_simple.tubes.fluidOut.deactivateDensityDerivatives|hex_simple.tubes.fluidOut.deactivateTwoPhaseRegion|hex_simple.tubes.fluidOut.drhodh_pxi|hex_simple.tubes.fluidOut.drhodp_hxi|hex_simple.tubes.fluidOut.gamma|hex_simple.tubes.fluidOut.h|hex_simple.tubes.fluidOut.interpolateTransportProperties|hex_simple.tubes.fluidOut.kappa|hex_simple.tubes.fluidOut.p|hex_simple.tubes.fluidOut.q|hex_simple.tubes.fluidOut.s|hex_simple.tubes.fluidOut.stateSelectPreferForInputs|hex_simple.tubes.fluidOut.transp.Pr|hex_simple.tubes.fluidOut.transp.eta|hex_simple.tubes.fluidOut.transp.lambda|hex_simple.tubes.fluidOut.transp.sigma|hex_simple.tubes.fluidOut.vleFluidPointer.id|hex_simple.tubes.fluidOut.w|hex_simple.tubes.geo.A_cross|hex_simple.tubes.geo.A_front|hex_simple.tubes.geo.A_heat.1.|hex_simple.tubes.geo.A_heat_CF.1.|hex_simple.tubes.geo.A_hor|hex_simple.tubes.geo.CF_geo.1.|hex_simple.tubes.geo.N_heat|hex_simple.tubes.geo.N_inlet|hex_simple.tubes.geo.N_outlet|hex_simple.tubes.geo.N_passes|hex_simple.tubes.geo.N_tubes|hex_simple.tubes.geo.diameter|hex_simple.tubes.geo.diameter_hyd|hex_simple.tubes.geo.height_fill|hex_simple.tubes.geo.length|hex_simple.tubes.geo.orientation|hex_simple.tubes.geo.shape.1,1.|hex_simple.tubes.geo.shape.1,2.|hex_simple.tubes.geo.shape.2,1.|hex_simple.tubes.geo.shape.2,2.|hex_simple.tubes.geo.volume|hex_simple.tubes.geo.z_in.1.|hex_simple.tubes.geo.z_out.1.|hex_simple.tubes.h_nom|hex_simple.tubes.h_start|hex_simple.tubes.heat.Q_flow|hex_simple.tubes.heat.T|hex_simple.tubes.heatSurfaceAlloc|hex_simple.tubes.heattransfer.CF_alpha_tubes|hex_simple.tubes.heattransfer.Delta_T_L|hex_simple.tubes.heattransfer.Delta_T_U|hex_simple.tubes.heattransfer.Delta_T_mean|hex_simple.tubes.heattransfer.Delta_T_wi|hex_simple.tubes.heattransfer.Delta_T_wo|hex_simple.tubes.heattransfer.HR|hex_simple.tubes.heattransfer.HR_nom|hex_simple.tubes.heattransfer.Pr|hex_simple.tubes.heattransfer.Re|hex_simple.tubes.heattransfer.alpha|hex_simple.tubes.heattransfer.alpha_lam|hex_simple.tubes.heattransfer.alpha_nom|hex_simple.tubes.heattransfer.alpha_turb|hex_simple.tubes.heattransfer.boundary|hex_simple.tubes.heattransfer.correlation|hex_simple.tubes.heattransfer.failureStatus|hex_simple.tubes.heattransfer.heat.Q_flow|hex_simple.tubes.heattransfer.heat.T|hex_simple.tubes.heattransfer.heatSurfaceAlloc|hex_simple.tubes.heattransfer.m_flow|hex_simple.tubes.heattransfer.velocity|hex_simple.tubes.initOption|hex_simple.tubes.inlet.h_outflow|hex_simple.tubes.inlet.m_flow|hex_simple.tubes.inlet.p|hex_simple.tubes.m_flow_nom|hex_simple.tubes.mass|hex_simple.tubes.outlet.h_outflow|hex_simple.tubes.outlet.m_flow|hex_simple.tubes.outlet.p|hex_simple.tubes.p|hex_simple.tubes.p_nom|hex_simple.tubes.p_start|hex_simple.tubes.phaseBorder.Delta_p_geo_in|hex_simple.tubes.phaseBorder.Delta_p_geo_out|hex_simple.tubes.phaseBorder.h_inflow|hex_simple.tubes.phase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Outlet.xi_dryGas.7.|hex_2ph.shell.flueGasOutlet.xi_dryGas.8.|hex_2ph.shell.flueGasOutlet.xi_gas|hex_2ph.shell.flueGasOutlet.xi_s|hex_2ph.shell.geo.A_cross|hex_2ph.shell.geo.A_front|hex_2ph.shell.geo.A_heat.1.|hex_2ph.shell.geo.A_heat.2.|hex_2ph.shell.geo.A_heat_CF.1.|hex_2ph.shell.geo.A_heat_CF.2.|hex_2ph.shell.geo.A_hor|hex_2ph.shell.geo.A_narrowed_ort|hex_2ph.shell.geo.A_narrowed_par|hex_2ph.shell.geo.CF_geo.1.|hex_2ph.shell.geo.CF_geo.2.|hex_2ph.shell.geo.Delta_l_ort|hex_2ph.shell.geo.Delta_l_par|hex_2ph.shell.geo.Delta_z_ort|hex_2ph.shell.geo.Delta_z_par|hex_2ph.shell.geo.MIN|hex_2ph.shell.geo.N_heat|hex_2ph.shell.geo.N_inlet|hex_2ph.shell.geo.N_outlet|hex_2ph.shell.geo.N_passes|hex_2ph.shell.geo.N_rows|hex_2ph.shell.geo.N_tubes|hex_2ph.shell.geo.N_tubes_parallel|hex_2ph.shell.geo.a|hex_2ph.shell.geo.b|hex_2ph.shell.geo.diameter_t|hex_2ph.shell.geo.fa|hex_2ph.shell.geo.flowOrientation|hex_2ph.shell.geo.height|hex_2ph.shell.geo.height_fill|hex_2ph.shell.geo.interior|hex_2ph.shell.geo.length|hex_2ph.shell.geo.length_bundle_ort|hex_2ph.shell.geo.length_bundle_par|hex_2ph.shell.geo.length_tubes|hex_2ph.shell.geo.psi|hex_2ph.shell.geo.shape.1,1.|hex_2ph.shell.geo.shape.1,2.|hex_2ph.shell.geo.shape.2,1.|hex_2ph.shell.geo.shape.2,2.|hex_2ph.shell.geo.staggeredAlignment|hex_2ph.shell.geo.tubeOrientation|hex_2ph.shell.geo.volume|hex_2ph.shell.geo.width|hex_2ph.shell.geo.z_in.1.|hex_2ph.shell.geo.z_out.1.|hex_2ph.shell.h_nom|hex_2ph.shell.h_start|hex_2ph.shell.heat.Q_flow|hex_2ph.shell.heat.T|hex_2ph.shell.heatSurfaceAlloc|hex_2ph.shell.heattransfer.A_finned|hex_2ph.shell.heattransfer.A_tubes|hex_2ph.shell.heattransfer.CF_fouling|hex_2ph.shell.heattransfer.Delta_T_L|hex_2ph.shell.heattransfer.Delta_T_U|hex_2ph.shell.heattransfer.Delta_T_mean|hex_2ph.shell.heattransfer.Delta_T_wi|hex_2ph.shell.heattransfer.Delta_T_wo|hex_2ph.shell.heattransfer.HR|hex_2ph.shell.heattransfer.HR_nom|hex_2ph.shell.heattransfer.HT_type|hex_2ph.shell.heattransfer.N_f|hex_2ph.shell.heattransfer.N_tubes_p|hex_2ph.shell.heattransfer.Nu|hex_2ph.shell.heattransfer.Re|hex_2ph.shell.heattransfer.T_f|hex_2ph.shell.heattransfer.alpha|hex_2ph.shell.heattransfer.h_f|hex_2ph.shell.heattransfer.heat.Q_flow|hex_2ph.shell.heattransfer.heat.T|hex_2ph.shell.heattransfer.heatSurfaceAlloc|hex_2ph.shell.heattransfer.s_f|hex_2ph.shell.heattransfer.t_f|hex_2ph.shell.heattransfer.w|hex_2ph.shell.heattransfer.w_0|hex_2ph.shell.initOption|hex_2ph.shell.inlet.T_outflow|hex_2ph.shell.inlet.m_flow|hex_2ph.shell.inlet.p|hex_2ph.shell.inlet.xi_outflow.1.|hex_2ph.shell.inlet.xi_outflow.2.|hex_2ph.shell.inlet.xi_outflow.3.|hex_2ph.shell.inlet.xi_outflow.4.|hex_2ph.shell.inlet.xi_outflow.5.|hex_2ph.shell.inlet.xi_outflow.6.|hex_2ph.shell.inlet.xi_outflow.7.|hex_2ph.shell.inlet.xi_outflow.8.|hex_2ph.shell.inlet.xi_outflow.9.|hex_2ph.shell.m_flow_nom|hex_2ph.shell.outlet.T_outflow|hex_2ph.shell.outlet.m_flow|hex_2ph.shell.outlet.p|hex_2ph.shell.outlet.xi_outflow.1.|hex_2ph.shell.outlet.xi_outflow.2.|hex_2ph.shell.outlet.xi_outflow.3.|hex_2ph.shell.outlet.xi_outflow.4.|hex_2ph.shell.outlet.xi_outflow.5.|hex_2ph.shell.outlet.xi_outflow.6.|hex_2ph.shell.outlet.xi_outflow.7.|hex_2ph.shell.outlet.xi_outflow.8.|hex_2ph.shell.outlet.xi_outflow.9.|hex_2ph.shell.p_nom|hex_2ph.shell.p_start|hex_2ph.shell.pressureLoss.Delta_p|hex_2ph.shell.pressureLoss.Delta_p_nom|hex_2ph.shell.pressureLoss.Delta_p_smooth|hex_2ph.shell.pressureLoss.zeta|hex_2ph.shell.summary.inlet.H_flow|hex_2ph.shell.summary.inlet.T|hex_2ph.shell.summary.inlet.h|hex_2ph.shell.summary.inlet.m_flow|hex_2ph.shell.summary.inlet.p|hex_2ph.shell.summary.inlet.xi.1.|hex_2ph.shell.summary.inlet.xi.2.|hex_2ph.shell.summary.inlet.xi.3.|hex_2ph.shell.summary.inlet.xi.4.|hex_2ph.shell.summary.inlet.xi.5.|hex_2ph.shell.summary.inlet.xi.6.|hex_2ph.shell.summary.inlet.xi.7.|hex_2ph.shell.summary.inlet.xi.8.|hex_2ph.shell.summary.inlet.xi.9.|hex_2ph.shell.summary.outlet.H_flow|hex_2ph.shell.summary.outlet.T|hex_2ph.shell.summary.outlet.h|hex_2ph.shell.summary.outlet.m_flow|hex_2ph.shell.summary.outlet.p|hex_2ph.shell.summary.outlet.xi.1.|hex_2ph.shell.summary.outlet.xi.2.|hex_2ph.shell.summary.outlet.xi.3.|hex_2ph.shell.summary.outlet.xi.4.|hex_2ph.shell.summary.outlet.xi.5.|hex_2ph.shell.summary.outlet.xi.6.|hex_2ph.shell.summary.outlet.xi.7.|hex_2ph.shell.summary.outlet.xi.8.|hex_2ph.shell.summary.outlet.xi.9.|hex_2ph.shell.summary.outline.A_heat|hex_2ph.shell.summary.outline.Delta_p|hex_2ph.shell.summary.outline.H|hex_2ph.shell.summary.outline.Q_flow_tot|hex_2ph.shell.summary.outline.T|hex_2ph.shell.summary.outline.h|hex_2ph.shell.summary.outline.mass|hex_2ph.shell.summary.outline.p|hex_2ph.shell.summary.outline.rho|hex_2ph.shell.summary.outline.volume_tot|hex_2ph.shell.useHomotopy|hex_2ph.shell.use_dynamicMassbalance|hex_2ph.shell.xi_nom.1.|hex_2ph.shell.xi_nom.2.|hex_2ph.shell.xi_nom.3.|hex_2ph.shell.xi_nom.4.|hex_2ph.shell.xi_nom.5.|hex_2ph.shell.xi_nom.6.|hex_2ph.shell.xi_nom.7.|hex_2ph.shell.xi_nom.8.|hex_2ph.shell.xi_nom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ph.tubes.summary.outline.level_rel|hex_2ph.tubes.summary.outline.showExpertSummary|hex_2ph.tubes.summary.outline.volume.1.|hex_2ph.tubes.summary.outline.volume.2.|hex_2ph.tubes.summary.outline.volume_tot|hex_2ph.tubes.summary.outline.yps.1.|hex_2ph.tubes.summary.outline.yps.2.|hex_2ph.tubes.useHomotopy|hex_2ph.tubes.volume_liq|hex_2ph.tubes.volume_vap|hex_2ph.tubes.yps.1.|hex_2ph.tubes.yps.2.|hex_2ph.useHomotopy|hex_2ph.wall.A_heat.1.|hex_2ph.wall.A_heat.2.|hex_2ph.wall.A_heat.3.|hex_2ph.wall.A_heat.4.|hex_2ph.wall.A_heat.5.|hex_2ph.wall.A_heat.6.|hex_2ph.wall.A_heat_m|hex_2ph.wall.A_heat_m_rad.1.|hex_2ph.wall.A_heat_m_rad.2.|hex_2ph.wall.A_heat_m_rad.3.|hex_2ph.wall.CF_lambda|hex_2ph.wall.Delta_radius.1.|hex_2ph.wall.Delta_radius.2.|hex_2ph.wall.Delta_radius.3.|hex_2ph.wall.HR|hex_2ph.wall.HR_nom|hex_2ph.wall.HR_rad.1.|hex_2ph.wall.HR_rad.2.|hex_2ph.wall.HR_rad.3.|hex_2ph.wall.N_passes|hex_2ph.wall.N_rad|hex_2ph.wall.N_tubes|hex_2ph.wall.Q_flow.1.|hex_2ph.wall.Q_flow.2.|hex_2ph.wall.Q_flow.3.|hex_2ph.wall.Q_flow.4.|hex_2ph.wall.T.1.|hex_2ph.wall.T.2.|hex_2ph.wall.T.3.|hex_2ph.wall.T_mean|hex_2ph.wall.T_start.1.|hex_2ph.wall.T_start.2.|hex_2ph.wall.T_start.3.|hex_2ph.wall.Tdr.1.|hex_2ph.wall.Tdr.2.|hex_2ph.wall.Tdr.3.|hex_2ph.wall.Tdr.4.|hex_2ph.wall.U.1.|hex_2ph.wall.U.2.|hex_2ph.wall.U.3.|der.hex_2ph.wall.U.1..|der.hex_2ph.wall.U.2..|der.hex_2ph.wall.U.3..|hex_2ph.wall.diameter_i|hex_2ph.wall.diameter_o|hex_2ph.wall.initOption|hex_2ph.wall.innerPhase.Q_flow|hex_2ph.wall.innerPhase.T|hex_2ph.wall.length|hex_2ph.wall.mass|hex_2ph.wall.mass_struc|hex_2ph.wall.outerPhase.Q_flow|hex_2ph.wall.outerPhase.T|hex_2ph.wall.radius.1.|hex_2ph.wall.radius.2.|hex_2ph.wall.radius.3.|hex_2ph.wall.radius.4.|hex_2ph.wall.radius_m.1.|hex_2ph.wall.radius_m.2.|hex_2ph.wall.radius_m.3.|hex_2ph.wall.radius_m.4.|hex_2ph.wall.radius_m.5.|hex_2ph.wall.radius_m.6.|hex_2ph.wall.radius_v.1.|hex_2ph.wall.radius_v.2.|hex_2ph.wall.radius_v.3.|hex_2ph.wall.radius_v.4.|hex_2ph.wall.radius_v.5.|hex_2ph.wall.sizefunc|hex_2ph.wall.solid.1..T|hex_2ph.wall.solid.1..cp|hex_2ph.wall.solid.1..cp_nominal|hex_2ph.wall.solid.1..d|hex_2ph.wall.solid.1..lambda|hex_2ph.wall.solid.1..lambda_nominal|hex_2ph.wall.solid.2..T|hex_2ph.wall.solid.2..cp|hex_2ph.wall.solid.2..cp_nominal|hex_2ph.wall.solid.2..d|hex_2ph.wall.solid.2..lambda|hex_2ph.wall.solid.2..lambda_nominal|hex_2ph.wall.solid.3..T|hex_2ph.wall.solid.3..cp|hex_2ph.wall.solid.3..cp_nominal|hex_2ph.wall.solid.3..d|hex_2ph.wall.solid.3..lambda|hex_2ph.wall.solid.3..lambda_nominal|hex_2ph.wall.summary.A_heat.1.|hex_2ph.wall.summary.A_heat.2.|hex_2ph.wall.summary.A_heat.3.|hex_2ph.wall.summary.A_heat.4.|hex_2ph.wall.summary.A_heat.5.|hex_2ph.wall.summary.A_heat.6.|hex_2ph.wall.summary.Delta_radius.1.|hex_2ph.wall.summary.Delta_radius.2.|hex_2ph.wall.summary.Delta_radius.3.|hex_2ph.wall.summary.N_A_heat|hex_2ph.wall.summary.N_rad|hex_2ph.wall.summary.N_tubes|hex_2ph.wall.summary.Q_flow.1.|hex_2ph.wall.summary.Q_flow.2.|hex_2ph.wall.summary.Q_flow.3.|hex_2ph.wall.summary.Q_flow.4.|hex_2ph.wall.summary.T.1.|hex_2ph.wall.summary.T.2.|hex_2ph.wall.summary.T.3.|hex_2ph.wall.summary.U.1.|hex_2ph.wall.summary.U.2.|hex_2ph.wall.summary.U.3.|hex_2ph.wall.summary.cp.1.|hex_2ph.wall.summary.cp.2.|hex_2ph.wall.summary.cp.3.|hex_2ph.wall.summary.d.1.|hex_2ph.wall.summary.d.2.|hex_2ph.wall.summary.d.3.|hex_2ph.wall.summary.diameter_i|hex_2ph.wall.summary.diameter_o|hex_2ph.wall.summary.length|hex_2ph.wall.summary.mass|hex_2ph.wall.summary.radius.1.|hex_2ph.wall.summary.radius.2.|hex_2ph.wall.summary.radius.3.|hex_2ph.wall.summary.radius.4.|hex_2ph.wall.summary.radius_m.1.|hex_2ph.wall.summary.radius_m.2.|hex_2ph.wall.summary.radius_m.3.|hex_2ph.wall.summary.radius_m.4.|hex_2ph.wall.summary.radius_m.5.|hex_2ph.wall.summary.radius_m.6.|hex_2ph.wall.summary.radius_v.1.|hex_2ph.wall.summary.radius_v.2.|hex_2ph.wall.summary.radius_v.3.|hex_2ph.wall.summary.radius_v.4.|hex_2ph.wall.summary.radius_v.5.|hex_2ph.width|hex_2ph.width_hotwell|hex_2ph.xi_shell_start.1.|hex_2ph.xi_shell_start.2.|hex_2ph.xi_shell_start.3.|hex_2ph.xi_shell_start.4.|hex_2ph.xi_shell_start.5.|hex_2ph.xi_shell_start.6.|hex_2ph.xi_shell_start.7.|hex_2ph.xi_shell_start.8.|hex_2ph.xi_shell_start.9.|hex_2ph.yps_liq_nom|hex_2ph.yps_nom.1.|hex_2ph.yps_nom.2.|hex_2ph.z_in_shell|hex_2ph.z_in_tubes|hex_2ph.z_out_shell|hex_2ph.z_out_tubes|hex_ntu.CF_geo|hex_ntu.Delta_z_ort|hex_ntu.Delta_z_par|hex_ntu.In1.T_outflow|hex_ntu.In1.m_flow|hex_ntu.In1.p|hex_ntu.In1.xi_outflow.1.|hex_ntu.In1.xi_outflow.2.|hex_ntu.In1.xi_outflow.3.|hex_ntu.In1.xi_outflow.4.|hex_ntu.In1.xi_outflow.5.|hex_ntu.In1.xi_outflow.6.|hex_ntu.In1.xi_outflow.7.|hex_ntu.In1.xi_outflow.8.|hex_ntu.In1.xi_outflow.9.|hex_ntu.In2.h_outflow|hex_ntu.In2.m_flow|hex_ntu.In2.p|hex_ntu.N_passes|hex_ntu.N_rows|hex_ntu.N_tubes|hex_ntu.Out1.T_outflow|hex_ntu.Out1.m_flow|hex_ntu.Out1.p|hex_ntu.Out1.xi_outflow.1.|hex_ntu.Out1.xi_outflow.2.|hex_ntu.Out1.xi_outflow.3.|hex_ntu.Out1.xi_outflow.4.|hex_ntu.Out1.xi_outf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.2.|hex_simple.shell.bulk.xi_dryGas.3.|hex_simple.shell.bulk.xi_dryGas.4.|hex_simple.shell.bulk.xi_dryGas.5.|hex_simple.shell.bulk.xi_dryGas.6.|hex_simple.shell.bulk.xi_dryGas.7.|hex_simple.shell.bulk.xi_dryGas.8.|hex_simple.shell.bulk.xi_gas|hex_simple.shell.bulk.xi_s|hex_simple.shell.flueGasInlet.M|hex_simple.shell.flueGasInlet.M_i.10.|hex_simple.shell.flueGasInlet.M_i.1.|hex_simple.shell.flueGasInlet.M_i.2.|hex_simple.shell.flueGasInlet.M_i.3.|hex_simple.shell.flueGasInlet.M_i.4.|hex_simple.shell.flueGasInlet.M_i.5.|hex_simple.shell.flueGasInlet.M_i.6.|hex_simple.shell.flueGasInlet.M_i.7.|hex_simple.shell.flueGasInlet.M_i.8.|hex_simple.shell.flueGasInlet.M_i.9.|hex_simple.shell.flueGasInlet.T|hex_simple.shell.flueGasInlet.beta|hex_simple.shell.flueGasInlet.computeTransportProperties|hex_simple.shell.flueGasInlet.cp|hex_simple.shell.flueGasInlet.cv|hex_simple.shell.flueGasInlet.d|hex_simple.shell.flueGasInlet.delta_hd|hex_simple.shell.flueGasInlet.delta_hv|hex_simple.shell.flueGasInlet.drhodh_pxi|hex_simple.shell.flueGasInlet.drhodp_hxi|hex_simple.shell.flueGasInlet.drhodxi_ph.1.|hex_simple.shell.flueGasInlet.drhodxi_ph.2.|hex_simple.shell.flueGasInlet.drhodxi_ph.3.|hex_simple.shell.flueGasInlet.drhodxi_ph.4.|hex_simple.shell.flueGasInlet.drhodxi_ph.5.|hex_simple.shell.flueGasInlet.drhodxi_ph.6.|hex_simple.shell.flueGasInlet.drhodxi_ph.7.|hex_simple.shell.flueGasInlet.drhodxi_ph.8.|hex_simple.shell.flueGasInlet.drhodxi_ph.9.|hex_simple.shell.flueGasInlet.gasPointer.id|hex_simple.shell.flueGasInlet.h|hex_simple.shell.flueGasInlet.h1px|hex_simple.shell.flueGasInlet.h_i.10.|hex_simple.shell.flueGasInlet.h_i.1.|hex_simple.shell.flueGasInlet.h_i.2.|hex_simple.shell.flueGasInlet.h_i.3.|hex_simple.shell.flueGasInlet.h_i.4.|hex_simple.shell.flueGasInlet.h_i.5.|hex_simple.shell.flueGasInlet.h_i.6.|hex_simple.shell.flueGasInlet.h_i.7.|hex_simple.shell.flueGasInlet.h_i.8.|hex_simple.shell.flueGasInlet.h_i.9.|hex_simple.shell.flueGasInlet.humRatio|hex_simple.shell.flueGasInlet.humRatio_s|hex_simple.shell.flueGasInlet.kappa|hex_simple.shell.flueGasInlet.p|hex_simple.shell.flueGasInlet.p_i.10.|hex_simple.shell.flueGasInlet.p_i.1.|hex_simple.shell.flueGasInlet.p_i.2.|hex_simple.shell.flueGasInlet.p_i.3.|hex_simple.shell.flueGasInlet.p_i.4.|hex_simple.shell.flueGasInlet.p_i.5.|hex_simple.shell.flueGasInlet.p_i.6.|hex_simple.shell.flueGasInlet.p_i.7.|hex_simple.shell.flueGasInlet.p_i.8.|hex_simple.shell.flueGasInlet.p_i.9.|hex_simple.shell.flueGasInlet.p_s|hex_simple.shell.flueGasInlet.phi|hex_simple.shell.flueGasInlet.s|hex_simple.shell.flueGasInlet.stateSelectPreferForInputs|hex_simple.shell.flueGasInlet.transp.Pr|hex_simple.shell.flueGasInlet.transp.eta|hex_simple.shell.flueGasInlet.transp.lambda|hex_simple.shell.flueGasInlet.transp.sigma|hex_simple.shell.flueGasInlet.w|hex_simple.shell.flueGasInlet.x.1.|hex_simple.shell.flueGasInlet.x.2.|hex_simple.shell.flueGasInlet.x.3.|hex_simple.shell.flueGasInlet.x.4.|hex_simple.shell.flueGasInlet.x.5.|hex_simple.shell.flueGasInlet.x.6.|hex_simple.shell.flueGasInlet.x.7.|hex_simple.shell.flueGasInlet.x.8.|hex_simple.shell.flueGasInlet.x.9.|hex_simple.shell.flueGasInlet.xi.1.|hex_simple.shell.flueGasInlet.xi.2.|hex_simple.shell.flueGasInlet.xi.3.|hex_simple.shell.flueGasInlet.xi.4.|hex_simple.shell.flueGasInlet.xi.5.|hex_simple.shell.flueGasInlet.xi.6.|hex_simple.shell.flueGasInlet.xi.7.|hex_simple.shell.flueGasInlet.xi.8.|hex_simple.shell.flueGasInlet.xi.9.|hex_simple.shell.flueGasInlet.xi_dryGas.1.|hex_simple.shell.flueGasInlet.xi_dryGas.2.|hex_simple.shell.flueGasInlet.xi_dryGas.3.|hex_simple.shell.flueGasInlet.xi_dryGas.4.|hex_simple.shell.flueGasInlet.xi_dryGas.5.|hex_simple.shell.flueGasInlet.xi_dryGas.6.|hex_simple.shell.flueGasInlet.xi_dryGas.7.|hex_simple.shell.flueGasInlet.xi_dryGas.8.|hex_simple.shell.flueGasInlet.xi_gas|hex_simple.shell.flueGasInlet.xi_s|hex_simple.shell.flueGasOutlet.M|hex_simple.shell.flueGasOutlet.M_i.10.|hex_simple.shell.flueGasOutlet.M_i.1.|hex_simple.shell.flueGasOutlet.M_i.2.|hex_simple.shell.flueGasOutlet.M_i.3.|hex_simple.shell.flueGasOutlet.M_i.4.|hex_simple.shell.flueGasOutlet.M_i.5.|hex_simple.shell.flueGasOutlet.M_i.6.|hex_simple.shell.flueGasOutlet.M_i.7.|hex_simple.shell.flueGasOutlet.M_i.8.|hex_simple.shell.flueGasOutlet.M_i.9.|hex_simple.shell.flueGasOutlet.T|hex_simple.shell.flueGasOutlet.beta|hex_simple.shell.flueGasOutlet.computeTransportProperties|hex_simple.shell.flueGasOutlet.cp|hex_simple.shell.flueGasOutlet.cv|hex_simple.shell.flueGasOutlet.d|hex_simple.shell.flueGasOutlet.delta_hd|hex_simple.shell.flueGasOutlet.delta_hv|hex_simple.shell.flueGasOutlet.drhodh_pxi|hex_simple.shell.flueGasOutlet.drhodp_hxi|hex_simple.shell.flueGasOutlet.drhodxi_ph.1.|hex_simple.shell.flueGasOutlet.drhodxi_ph.2.|hex_simple.shell.flueGasOutlet.drhodxi_ph.3.|hex_simple.shell.flueGasOutlet.drhodxi_ph.4.|hex_simple.shell.flueGasOutlet.drhodxi_ph.5.|hex_simple.shell.flueGasOutlet.drhodxi_ph.6.|hex_simple.shell.flueGasOutlet.drhodxi_ph.7.|hex_simple.shel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ensityDerivatives|hex_simple.tubes.fluidIn.deactivateTwoPhaseRegion|hex_simple.tubes.fluidIn.drhodh_pxi|hex_simple.tubes.fluidIn.drhodp_hxi|hex_simple.tubes.fluidIn.gamma|hex_simple.tubes.fluidIn.h|hex_simple.tubes.fluidIn.interpolateTransportProperties|hex_simple.tubes.fluidIn.kappa|hex_simple.tubes.fluidIn.p|hex_simple.tubes.fluidIn.q|hex_simple.tubes.fluidIn.s|hex_simple.tubes.fluidIn.stateSelectPreferForInputs|hex_simple.tubes.fluidIn.transp.Pr|hex_simple.tubes.fluidIn.transp.eta|hex_simple.tubes.fluidIn.transp.lambda|hex_simple.tubes.fluidIn.transp.sigma|hex_simple.tubes.fluidIn.vleFluidPointer.id|hex_simple.tubes.fluidIn.w|hex_simple.tubes.fluidOut.M|hex_simple.tubes.fluidOut.M_i.1.|hex_simple.tubes.fluidOut.T|hex_simple.tubes.fluidOut.VLE.T_l|hex_simple.tubes.fluidOut.VLE.T_v|hex_simple.tubes.fluidOut.VLE.d_l|hex_simple.tubes.fluidOut.VLE.d_v|hex_simple.tubes.fluidOut.VLE.h_l|hex_simple.tubes.fluidOut.VLE.h_v|hex_simple.tubes.fluidOut.VLE.nc|hex_simple.tubes.fluidOut.VLE.p_l|hex_simple.tubes.fluidOut.VLE.p_v|hex_simple.tubes.fluidOut.VLE.s_l|hex_simple.tubes.fluidOut.VLE.s_v|hex_simple.tubes.fluidOut.VLEAdditional.beta_l|hex_simple.tubes.fluidOut.VLEAdditional.beta_v|hex_simple.tubes.fluidOut.VLEAdditional.cp_l|hex_simple.tubes.fluidOut.VLEAdditional.cp_v|hex_simple.tubes.fluidOut.VLEAdditional.kappa_l|hex_simple.tubes.fluidOut.VLEAdditional.kappa_v|hex_simple.tubes.fluidOut.VLETransp.Pr_l|hex_simple.tubes.fluidOut.VLETransp.Pr_v|hex_simple.tubes.fluidOut.VLETransp.eta_l|hex_simple.tubes.fluidOut.VLETransp.eta_v|hex_simple.tubes.fluidOut.VLETransp.lambda_l|hex_simple.tubes.fluidOut.VLETransp.lambda_v|hex_simple.tubes.fluidOut.beta|hex_simple.tubes.fluidOut.computeSurfaceTension|hex_simple.tubes.fluidOut.computeTransportProperties|hex_simple.tubes.fluidOut.computeVLEAdditionalProperties|hex_simple.tubes.fluidOut.computeVLETransportProperties|hex_simple.tubes.fluidOut.cp|hex_simple.tubes.fluidOut.crit.T|hex_simple.tubes.fluidOut.crit.d|hex_simple.tubes.fluidOut.crit.h|hex_simple.tubes.fluidOut.crit.p|hex_simple.tubes.fluidOut.crit.s|hex_simple.tubes.fluidOut.cv|hex_simple.tubes.fluidOut.d|hex_simple.tubes.fluidOut.deactivateDensityDerivatives|hex_simple.tubes.fluidOut.deactivateTwoPhaseRegion|hex_simple.tubes.fluidOut.drhodh_pxi|hex_simple.tubes.fluidOut.drhodp_hxi|hex_simple.tubes.fluidOut.gamma|hex_simple.tubes.fluidOut.h|hex_simple.tubes.fluidOut.interpolateTransportProperties|hex_simple.tubes.fluidOut.kappa|hex_simple.tubes.fluidOut.p|hex_simple.tubes.fluidOut.q|hex_simple.tubes.fluidOut.s|hex_simple.tubes.fluidOut.stateSelectPreferForInputs|hex_simple.tubes.fluidOut.transp.Pr|hex_simple.tubes.fluidOut.transp.eta|hex_simple.tubes.fluidOut.transp.lambda|hex_simple.tubes.fluidOut.transp.sigma|hex_simple.tubes.fluidOut.vleFluidPointer.id|hex_simple.tubes.fluidOut.w|hex_simple.tubes.geo.A_cross|hex_simple.tubes.geo.A_front|hex_simple.tubes.geo.A_heat.1.|hex_simple.tubes.geo.A_heat_CF.1.|hex_simple.tubes.geo.A_hor|hex_simple.tubes.geo.CF_geo.1.|hex_simple.tubes.geo.N_heat|hex_simple.tubes.geo.N_inlet|hex_simple.tubes.geo.N_outlet|hex_simple.tubes.geo.N_passes|hex_simple.tubes.geo.N_tubes|hex_simple.tubes.geo.diameter|hex_simple.tubes.geo.diameter_hyd|hex_simple.tubes.geo.height_fill|hex_simple.tubes.geo.length|hex_simple.tubes.geo.orientation|hex_simple.tubes.geo.shape.1,1.|hex_simple.tubes.geo.shape.1,2.|hex_simple.tubes.geo.shape.2,1.|hex_simple.tubes.geo.shape.2,2.|hex_simple.tubes.geo.volume|hex_simple.tubes.geo.z_in.1.|hex_simple.tubes.geo.z_out.1.|hex_simple.tubes.h_nom|hex_simple.tubes.h_start|hex_simple.tubes.heat.Q_flow|hex_simple.tubes.heat.T|hex_simple.tubes.heatSurfaceAlloc|hex_simple.tubes.heattransfer.CF_alpha_tubes|hex_simple.tubes.heattransfer.Delta_T_L|hex_simple.tubes.heattransfer.Delta_T_U|hex_simple.tubes.heattransfer.Delta_T_mean|hex_simple.tubes.heattransfer.Delta_T_wi|hex_simple.tubes.heattransfer.Delta_T_wo|hex_simple.tubes.heattransfer.HR|hex_simple.tubes.heattransfer.HR_nom|hex_simple.tubes.heattransfer.Pr|hex_simple.tubes.heattransfer.Re|hex_simple.tubes.heattransfer.alpha|hex_simple.tubes.heattransfer.alpha_lam|hex_simple.tubes.heattransfer.alpha_nom|hex_simple.tubes.heattransfer.alpha_turb|hex_simple.tubes.heattransfer.boundary|hex_simple.tubes.heattransfer.correlation|hex_simple.tubes.heattransfer.failureStatus|hex_simple.tubes.heattransfer.heat.Q_flow|hex_simple.tubes.heattransfer.heat.T|hex_simple.tubes.heattransfer.heatSurfaceAlloc|hex_simple.tubes.heattransfer.m_flow|hex_simple.tubes.heattransfer.velocity|hex_simple.tubes.initOption|hex_simple.tubes.inlet.h_outflow|hex_simple.tubes.inlet.m_flow|hex_simple.tubes.inlet.p|hex_simple.tubes.m_flow_nom|hex_simple.tubes.mass|hex_simple.tubes.outlet.h_outflow|hex_simple.tubes.outlet.m_flow|hex_simple.tubes.outlet.p|hex_simple.tubes.p|hex_simple.tubes.p_nom|hex_simple.tubes.p_start|hex_simple.tubes.phaseBorder.Delta_p_geo_in|hex_simple.tubes.phaseBorder.Delta_p_geo_out|hex_simple.tubes.phaseBorder.h_inflow|hex_simple.tubes.phase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Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/SMArtIInt 0.2.2-main/package.mo): time 0.01009/0.01009, allocations: 1.437 MB / 17.74 MB, free: 5.297 MB / 14.72 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/package.mo): time 0.1258/0.1258, allocations: 22.37 MB / 41.16 MB, free: 7.758 MB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ModelicaServices 4.0.0+maint.om/package.mo): time 0.001148/0.001148, allocations: 112 kB / 48.66 MB, free: 236 kB / 34.91 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Complex 4.0.0+maint.om/package.mo): time 0.001419/0.001419, allocations: 197 kB / 56.26 MB, free: 9.441 MB / 46.55 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/Modelica 4.0.0+maint.om/package.mo): time 1.368/1.368, allocations: 222.9 MB / 286.6 MB, free: 13.92 MB / 222.1 MB
Notification: Performance of loadFile(/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/package.mo): time 0.892/0.892, allocations: 127.8 MB / 471.3 MB, free: 0.5625 MB / 366.1 MB
Notification: Performance of FrontEnd - loaded program: time 0.002268/0.002268, allocations: 123.8 kB / 0.6364 GB, free: 12.71 MB / 478.1 MB
Notification: Performance of FrontEnd - Absyn->SCode: time 0.4387/0.4409, allocations: 82.34 MB / 0.7168 GB, free: 9.43 MB / 0.5138 GB
Notification: Performance of NFInst.instantiate(ClaRa.Components.HeatExchangers.Check.Test_HEXvle2gas_L3_1ph_BU): time 0.04947/0.4905, allocations: 51.23 MB / 0.7668 GB, free: 12.32 MB / 0.5607 GB
Notification: Performance of NFInst.instExpressions: time 0.06106/0.5516, allocations: 36.41 MB / 0.8024 GB, free: 7.801 MB / 0.5919 GB
Notification: Performance of NFInst.updateImplicitVariability: time 0.0156/0.5672, allocations: 203.2 kB / 0.8026 GB, free: 7.602 MB / 0.5919 GB
Notification: Performance of NFTyping.typeComponents: time 0.0141/0.5814, allocations: 5.395 MB / 0.8079 GB, free: 2.188 MB / 0.5919 GB
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/GasFunctions.mo:238:23-242:17:writable] Warning: Pure function 'TILMedia.GasFunctions.density_pTxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.density_pTxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:177:13-181:19:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.density_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.density_phxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:202:13-206:40:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.specificIsobaricHeatCapacity_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.specificIsobaricHeatCapacity_phxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:257:13-261:28:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.dynamicViscosity_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.dynamicViscosity_phxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:252:13-256:31:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.thermalConductivity_phxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.thermalConductivity_phxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/GasFunctions.mo:243:23-247:26:writable] Warning: Pure function 'TILMedia.GasFunctions.specificEnthalpy_pTxi' contains a call to impure function 'TILMedia.Internals.GasFunctions.specificEnthalpy_pTxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:777:13-781:24:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.bubbleDensity_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.bubbleDensity_pxi'.
[/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/VLEFluidFunctions.mo:772:13-776:21:writable] Warning: Pure function 'TILMedia.Internals.VLEFluidConfigurations.FullyMixtureCompatible.VLEFluidFunctions.dewDensity_pxi' contains a call to impure function 'TILMedia.Internals.VLEFluidFunctions.dewDensity_pxi'.
Notification: Performance of NFTyping.typeBindings: time 0.02497/0.6064, allocations: 8.728 MB / 0.8164 GB, free: 9.422 MB / 0.6075 GB
Notification: Performance of NFTyping.typeClassSections: time 0.02087/0.6273, allocations: 8.752 MB / 0.8249 GB, free: 0.6641 MB / 0.6075 GB
Notification: Performance of NFFlatten.flatten: time 0.03616/0.6635, allocations: 26.87 MB / 0.8512 GB, free: 5.734 MB / 0.6388 GB
Notification: Performance of NFFlatten.resolveConnections: time 0.02565/0.6892, allocations: 17.06 MB / 0.8678 GB, free: 4.535 MB / 0.6544 GB
Notification: Performance of NFEvalConstants.evaluate: time 0.02162/0.7108, allocations: 12.31 MB / 0.8799 GB, free: 8.184 MB / 0.67 GB
Notification: Performance of NFSimplifyModel.simplify: time 0.02183/0.7327, allocations: 15.6 MB / 0.8951 GB, free: 8.535 MB / 0.6857 GB
Notification: Performance of NFPackage.collectConstants: time 0.01111/0.7438, allocations: 3.945 MB / 0.899 GB, free: 4.59 MB / 0.6857 GB
Notification: Performance of NFFlatten.collectFunctions: time 0.01982/0.7637, allocations: 7.478 MB / 0.9063 GB, free: 13.11 MB / 0.7013 GB
Notification: Performance of NFScalarize.scalarize: time 0.02029/0.784, allocations: 13.51 MB / 0.9195 GB, free: 15.57 MB / 0.7169 GB
Notification: Performance of NFVerifyModel.verify: time 0.0343/0.8183, allocations: 17.03 MB / 0.9361 GB, free: 14.47 MB / 0.7325 GB
Notification: Performance of NFConvertDAE.convert: time 0.8512/1.67, allocations: 55.27 MB / 0.9901 GB, free: 93 MB / 0.7483 GB
Notification: Performance of FrontEnd - DAE generated: time 6.372e-06/1.67, allocations: 3.031 kB / 0.9901 GB, free: 93 MB / 0.7483 GB
Notification: Performance of FrontEnd: time 1.733e-06/1.67, allocations: 0.5 kB / 0.9901 GB, free: 93 MB / 0.7483 GB
Notification: Performance of Transformations before backend: time 0.001452/1.671, allocations: 2.188 kB / 0.9901 GB, free: 93 MB / 0.7483 GB
Notification: Model statistics after passing the front-end and creating the data structures used by the back-end:
 * Number of equations: 3841
 * Number of variables: 3841
Notification: Performance of Generate backend data structure: time 0.1111/1.782, allocations: 33.79 MB / 1.023 GB, free: 79.1 MB / 0.7483 GB
Notification: Performance of prepare preOptimizeDAE: time 4.942e-05/1.782, allocations: 7.812 kB / 1.023 GB, free: 79.1 MB / 0.7483 GB
Notification: Performance of preOpt normalInlineFunction (simulation): time 0.021/1.803, allocations: 3.259 MB / 1.026 GB, free: 77.32 MB / 0.7483 GB
Notification: Performance of preOpt evaluateParameters (simulation): time 0.08488/1.888, allocations: 35.62 MB / 1.061 GB, free: 60.23 MB / 0.7483 GB
Notification: Performance of preOpt simplifyIfEquations (simulation): time 0.001643/1.89, allocations: 0.9137 MB / 1.062 GB, free: 59.68 MB / 0.7483 GB
Notification: Performance of preOpt expandDerOperator (simulation): time 0.008701/1.899, allocations: 0.9549 MB / 1.063 GB, free: 58.73 MB / 0.7483 GB
Notification: Performance of preOpt clockPartitioning (simulation): time 0.07025/1.969, allocations: 33.43 MB / 1.096 GB, free: 21.72 MB / 0.7483 GB
Notification: Performance of preOpt findStateOrder (simulation): time 0.0005166/1.969, allocations: 60.38 kB / 1.096 GB, free: 21.7 MB / 0.7483 GB
Notification: Performance of preOpt replaceEdgeChange (simulation): time 0.007862/1.977, allocations: 0.59 MB / 1.096 GB, free: 21.12 MB / 0.7483 GB
Notification: Performance of preOpt inlineArrayEqn (simulation): time 0.001131/1.978, allocations: 1.085 MB / 1.097 GB, free: 20.03 MB / 0.7483 GB
Notification: Performance of preOpt removeEqualRHS (simulation): time 0.06239/2.041, allocations: 33.95 MB / 1.13 GB, free: 2.379 MB / 0.7639 GB
Warning: The model contains alias variables with redundant start and/or conflicting nominal values. It is recommended to resolve the conflicts, because otherwise the system could be hard to solve. To print the conflicting alias sets and the chosen candidates please use -d=aliasConflicts.
Notification: Performance of preOpt removeSimpleEquations (simulation): time 0.2006/2.241, allocations: 111.2 MB / 1.239 GB, free: 2.57 MB / 0.8733 GB
Notification: Performance of preOpt comSubExp (simulation): time 0.03833/2.28, allocations: 21.2 MB / 1.26 GB, free: 13.26 MB / 0.9045 GB
Notification: Performance of preOpt resolveLoops (simulation): time 0.02978/2.31, allocations: 16.24 MB / 1.276 GB, free: 12.96 MB / 0.9202 GB
Notification: Performance of preOpt evalFunc (simulation): time 0.004254/2.314, allocations: 0.9117 MB / 1.276 GB, free: 12.02 MB / 0.9202 GB
Notification: Performance of preOpt encapsulateWhenConditions (simulation): time 0.0002778/2.314, allocations: 187.9 kB / 1.277 GB, free: 11.84 MB / 0.9202 GB
Notification: Performance of pre-optimization done (n=2022): time 5.391e-05/2.314, allocations: 0 / 1.277 GB, free: 11.84 MB / 0.9202 GB
Notification: Performance of matching and sorting (n=2024): time 0.7956/3.11, allocations: 163.5 MB / 1.436 GB, free: 256.5 MB / 0.9358 GB
Notification: Performance of inlineWhenForInitialization (initialization): time 0.0005473/3.11, allocations: 2.149 MB / 1.438 GB, free: 253.9 MB / 0.9358 GB
Notification: Performance of selectInitializationVariablesDAE (initialization): time 0.05269/3.163, allocations: 22.05 MB / 1.46 GB, free: 235.3 MB / 0.9358 GB
Notification: Performance of collectPreVariables (initialization): time 0.006188/3.169, allocations: 209.7 kB / 1.46 GB, free: 235.1 MB / 0.9358 GB
Notification: Performance of collectInitialEqns (initialization): time 0.01388/3.183, allocations: 10.08 MB / 1.47 GB, free: 225.5 MB / 0.9358 GB
Notification: Performance of collectInitialBindings (initialization): time 0.01039/3.194, allocations: 6.903 MB / 1.477 GB, free: 218.8 MB / 0.9358 GB
Notification: Performance of simplifyInitialFunctions (initialization): time 0.02432/3.218, allocations: 3.302 MB / 1.48 GB, free: 215.5 MB / 0.9358 GB
Notification: Performance of setup shared object (initialization): time 5.346e-05/3.218, allocations: 301.1 kB / 1.48 GB, free: 215.2 MB / 0.9358 GB
Notification: Performance of preBalanceInitialSystem (initialization): time 0.0246/3.243, allocations: 14.19 MB / 1.494 GB, free: 201 MB / 0.9358 GB
Notification: Performance of partitionIndependentBlocks (initialization): time 0.02761/3.27, allocations: 18.24 MB / 1.512 GB, free: 181.2 MB / 0.9358 GB
Error: Initialization problem is structural singular. Please, check the initial conditions.
Notification: Performance of analyzeInitialSystem (initialization): time 1.252/4.522, allocations: 175.5 MB / 1.683 GB, free: 299.3 MB / 0.9358 GB
Notification: Performance of solveInitialSystemEqSystem (initialization): time 0.0001243/4.522, allocations: 33.91 kB / 1.683 GB, free: 299.3 MB / 0.9358 GB
Notification: Performance of matching and sorting (n=2560) (initialization): time 0.0809/4.603, allocations: 38.18 MB / 1.721 GB, free: 285.1 MB / 0.9358 GB
Notification: Performance of prepare postOptimizeDAE: time 0.0001225/4.603, allocations: 80.16 kB / 1.721 GB, free: 285.1 MB / 0.9358 GB
Notification: Performance of postOpt simplifyComplexFunction (initialization): time 0.001308/4.605, allocations: 381.9 kB / 1.721 GB, free: 285.1 MB / 0.9358 GB
Notification: Performance of postOpt tearingSystem (initialization): time 0.1954/4.8, allocations: 24.25 MB / 1.745 GB, free: 282 MB / 0.9358 GB
Notification: Performance of postOpt solveSimpleEquations (initialization): time 0.0308/4.831, allocations: 3.161 MB / 1.748 GB, free: 281.7 MB / 0.9358 GB
Notification: Performance of postOpt calculateStrongComponentJacobians (initialization): time 0.01948/4.85, allocations: 18.44 MB / 1.766 GB, free: 265.1 MB / 0.9358 GB
Notification: Performance of postOpt simplifyAllExpressions (initialization): time 0.02165/4.872, allocations: 0.5787 MB / 1.766 GB, free: 264.7 MB / 0.9358 GB
Notification: Performance of postOpt collapseArrayExpressions (initialization): time 0.007333/4.879, allocations: 0.6811 MB / 1.767 GB, free: 264.1 MB / 0.9358 GB
Warning: Assuming fixed start value for the following 37 variables:
         hex_ntu.wall.T_w_i:VARIABLE(min = 0.0 start = hex_ntu.wall.T_w_i_start unit = "K" fixed = true nominal = 300.0 protected = true )  "Wall temperature at inner phase" type: Real
         hex_ntu.wall.T_w_a:VARIABLE(min = 0.0 start = hex_ntu.wall.T_w_a_start unit = "K" fixed = true nominal = 300.0 protected = true )  "Wall temperature at outer phase" type: Real
         hex_ntu.tubes.h:VARIABLE(start = hex_ntu.tubes.h_start unit = "J/kg" fixed = true nominal = 1000.0 protected = true )  "spec. enthalpy state" type: Real
         hex_ntu.tubes.p:VARIABLE(min = 0.0 start = hex_ntu.tubes.p_start unit = "Pa" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer )  "System pressure" type: Real
         hex_ntu.shell.bulk.h:VARIABLE(start = hex_ntu.shell.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         hex_ntu.shell.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_ntu.shell.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.h:VARIABLE(start = hex_simple.shell.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         hex_simple.shell.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_simple.shell.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.tubes.h_liq:VARIABLE(start = hex_2ph.tubes.h_liq_start unit = "J/kg" fixed = true nominal = 1000.0 )  "Specific enthalpy of liquid phase" type: Real
         hex_2ph.tubes.h_vap:VARIABLE(start = hex_2ph.tubes.h_vap_start unit = "J/kg" fixed = true nominal = 1000.0 )  "Specific enthalpy of vapour phase" type: Real
         hex_2ph.tubes.p_vap:VARIABLE(min = 0.0 start = hex_2ph.tubes.p_start unit = "Pa" fixed = true nominal = 1e5 stateSelect=StateSelect.prefer )  "Vapour pressure" type: Real
         hex_2ph.shell.bulk.h:VARIABLE(start = hex_2ph.shell.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
         hex_2ph.shell.bulk.xi[1]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[2]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[3]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[4]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[5]:VARIABLE(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[6]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[7]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[8]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
         hex_2ph.shell.bulk.xi[9]:VARIABLE(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
Warning: The initial conditions are over specified. The following 1 initial equations are redundant, so they are removed from the initialization system:
         $DER.hex_simple.tubes.p = 0.0.
Notification: Model statistics after passing the back-end for initialization:
 * Number of independent subsystems: 441
 * Number of states: 0 ()
 * Number of discrete variables: 0 ()
 * Number of discrete states: 0 ()
 * Number of clocked states: 0 ()
 * Top-level inputs: 0
Notification: Strong component statistics for initialization (1411):
 * Single equations (assignments): 1289
 * Array equations: 0
 * Algorithm blocks: 1
 * Record equations: 111
 * When equations: 0
 * If-equations: 0
 * Equation systems (not torn): 3
 * Torn equation systems: 7
 * Mixed (continuous/discrete) equation systems: 0
Notification: Equation system details (not torn):
 * Constant Jacobian (size): 0 systems
 * Linear Jacobian (size,density): 0 systems
 * Non-linear Jacobian (size): 3 systems
   {1, 1, 1}
 * Without analytic Jacobian (size): 0 systems
Notification: Torn system details for strict tearing set:
 * Linear torn systems (#iteration vars, #inner vars, density): 3 systems
   {(4,3,87.5%), (1,6,100.0%), (1,1,100.0%)}
 * Non-linear torn systems (#iteration vars, #inner vars): 4 systems
   {(4,39), (4,39), (3,38), (2,32)}
Notification: Performance of prepare postOptimizeDAE: time 0.02507/4.904, allocations: 7.176 MB / 1.774 GB, free: 257.8 MB / 0.9358 GB
Notification: Performance of postOpt lateInlineFunction (simulation): time 0.01209/4.917, allocations: 2.47 MB / 1.776 GB, free: 256.8 MB / 0.9358 GB
Notification: Performance of postOpt wrapFunctionCalls (simulation): time 0.1059/5.023, allocations: 39.28 MB / 1.815 GB, free: 222.9 MB / 0.9358 GB
Notification: Performance of postOpt simplifysemiLinear (simulation): time 0.07347/5.096, allocations: 32.86 MB / 1.847 GB, free: 193 MB / 0.9358 GB
Notification: Performance of postOpt simplifyComplexFunction (simulation): time 0.001094/5.097, allocations: 287.7 kB / 1.847 GB, free: 192.7 MB / 0.9358 GB
Notification: Performance of postOpt removeConstants (simulation): time 0.01977/5.117, allocations: 6.297 MB / 1.853 GB, free: 187.7 MB / 0.9358 GB
Notification: Performance of postOpt simplifyTimeIndepFuncCalls (simulation): time 0.01267/5.13, allocations: 267.5 kB / 1.854 GB, free: 187.4 MB / 0.9358 GB
Notification: Performance of postOpt simplifyAllExpressions (simulation): time 0.02014/5.15, allocations: 376.2 kB / 1.854 GB, free: 187.1 MB / 0.9358 GB
Notification: Performance of postOpt findZeroCrossings (simulation): time 0.007348/5.157, allocations: 0.7377 MB / 1.855 GB, free: 186.3 MB / 0.9358 GB
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (4): (hex_2ph.shell.heattransfer.properties.transp.Pr, hex_2ph.shell.heattransfer.properties.transp.lambda, hex_2ph.shell.heattransfer.properties.transp.eta, hex_2ph.shell.heattransfer.properties.transp.sigma) = TILMedia.Internals.GasObjectFunctions.transportProperties_pTxi(hex_2ph.shell.heattransfer.properties.p, hex_2ph.shell.heattransfer.T_prop_am, {hex_2ph.shell.bulk.xi[1], hex_2ph.shell.bulk.xi[2], hex_2ph.shell.bulk.xi[3], hex_2ph.shell.bulk.xi[4], hex_2ph.shell.bulk.xi[5], hex_2ph.shell.bulk.xi[6], hex_2ph.shell.bulk.xi[7], hex_2ph.shell.bulk.xi[8], hex_2ph.shell.bulk.xi[9]}, hex_2ph.shell.heattransfer.properties.gasPointer)

Variables:
1: hex_2ph.shell.heattransfer.properties.transp.sigma:VARIABLE(unit = "N/m" protected = true )  "Surface tension" type: Real
2: hex_2ph.shell.heattransfer.properties.transp.lambda:VARIABLE(unit = "W/(m.K)" protected = true )  "Thermal conductivity" type: Real
3: hex_2ph.shell.heattransfer.properties.transp.Pr:VARIABLE(unit = "1" protected = true )  "Prandtl number" type: Real
4: hex_2ph.shell.heattransfer.properties.transp.eta:VARIABLE(min = -1.0 unit = "Pa.s" protected = true )  "Dynamic viscosity" type: Real
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/DAEMode.mo:528:7-530:90:writable] Error: Internal error DAEMode.traverserStrongComponents failed on equation:
1/1 (24): (hex_2ph.shell.heattransfer.properties.d, hex_2ph.shell.heattransfer.properties.kappa, hex_2ph.shell.heattransfer.properties.drhodp_hxi, hex_2ph.shell.heattransfer.properties.drhodh_pxi, hex_2ph.shell.heattransfer.properties.drhodxi_ph, hex_2ph.shell.heattransfer.properties.p_i, hex_2ph.shell.heattransfer.properties.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(hex_2ph.shell.heattransfer.properties.p, hex_2ph.shell.heattransfer.T_prop_am, {hex_2ph.shell.bulk.xi[1], hex_2ph.shell.bulk.xi[2], hex_2ph.shell.bulk.xi[3], hex_2ph.shell.bulk.xi[4], hex_2ph.shell.bulk.xi[5], hex_2ph.shell.bulk.xi[6], hex_2ph.shell.bulk.xi[7], hex_2ph.shell.bulk.xi[8], hex_2ph.shell.bulk.xi[9]}, hex_2ph.shell.heattransfer.properties.gasPointer)
2/25 (1): hex_2ph.shell.heattransfer.Re = max(1e-15, hex_2ph.shell.heattransfer.properties.d * hex_2ph.shell.heattransfer.w * hex_2ph.shell.geo.diameter_t / hex_2ph.shell.heattransfer.properties.transp.eta)
3/26 (1): hex_2ph.shell.heattransfer.Nu = 0.38 * hex_2ph.shell.heattransfer.Re ^ 0.6 * hex_2ph.shell.heattransfer.properties.transp.Pr ^ 0.3333333333333333 * (hex_2ph.shell.heattransfer.A_tubes / hex_2ph.shell.heattransfer.A_finned) ^ 0.15
4/27 (1): hex_2ph.shell.heattransfer.alpha = hex_2ph.shell.heattransfer.Nu * hex_2ph.shell.heattransfer.properties.transp.lambda / hex_2ph.shell.geo.diameter_t
5/28 (1): hex_2ph.wall.Q_flow[4] = hex_2ph.shell.heattransfer.alpha * (hex_2ph.shell.heattransfer.A_ts * (1.0 + hex_2ph.shell.heattransfer.N_f) + hex_2ph.shell.heattransfer.eff_fins * hex_2ph.shell.heattransfer.A_f * hex_2ph.shell.heattransfer.N_f) * hex_2ph.shell.heattransfer.Delta_T_mean
6/29 (1): hex_2ph.shell.heattransfer.Delta_T_mean = $cse70 * $cse71 * $cse72
7/30 (1): $cse71 = ClaRa.Basics.Functions.Stepsmoother(0.01, 1e-15, hex_2ph.shell.heattransfer.Delta_T_U * hex_2ph.shell.heattransfer.Delta_T_L)
8/31 (1): hex_2ph.shell.heattransfer.Delta_T_L = ClaRa.Basics.Functions.minAbs(hex_2ph.shell.heattransfer.Delta_T_wi, hex_2ph.shell.heattransfer.Delta_T_wo, 1e-6)
9/32 (1): hex_2ph.shell.heattransfer.Delta_T_U = ClaRa.Basics.Functions.maxAbs(hex_2ph.shell.heattransfer.Delta_T_wi, hex_2ph.shell.heattransfer.Delta_T_wo, 1e-6)
10/33 (1): $cse72 = ClaRa.Basics.Functions.SmoothZeroTransition((hex_2ph.shell.heattransfer.Delta_T_U - hex_2ph.shell.heattransfer.Delta_T_L) / $cse73, hex_2ph.shell.heattransfer.Delta_T_wi, abs(hex_2ph.shell.heattransfer.Delta_T_U) - abs(hex_2ph.shell.heattransfer.Delta_T_L) - 0.01, 0.001)
11/34 (1): $cse73 = log(abs(hex_2ph.shell.heattransfer.Delta_T_U) / (abs(hex_2ph.shell.heattransfer.Delta_T_L) + 1e-9))
12/35 (1): hex_2ph.shell.heattransfer.Delta_T_wi = hex_2ph.shell.heat.T - hex_2ph.shell.flueGasInlet.T
13/36 (1): hex_2ph.wall.Q_flow[4] = 80.0 * hex_2ph.wall.A_heat[6] * (hex_2ph.wall.T[3] - hex_2ph.shell.heat.T) / hex_2ph.wall.Delta_radius[3]
14/37 (1): der(hex_2ph.shell.bulk.h) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.h - hex_2ph.shell.bulk.h) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.h - hex_2ph.shell.bulk.h) + hex_2ph.wall.Q_flow[4]) / hex_2ph.shell.summary.outline.mass
15/38 (1): hex_2ph.shell.drhodt = hex_2ph.shell.bulk.drhodh_pxi * der(hex_2ph.shell.bulk.h) + hex_2ph.shell.bulk.drhodxi_ph[1] * der(hex_2ph.shell.bulk.xi[1]) + hex_2ph.shell.bulk.drhodxi_ph[2] * der(hex_2ph.shell.bulk.xi[2]) + hex_2ph.shell.bulk.drhodxi_ph[3] * der(hex_2ph.shell.bulk.xi[3]) + hex_2ph.shell.bulk.drhodxi_ph[4] * der(hex_2ph.shell.bulk.xi[4]) + hex_2ph.shell.bulk.drhodxi_ph[5] * der(hex_2ph.shell.bulk.xi[5]) + hex_2ph.shell.bulk.drhodxi_ph[6] * der(hex_2ph.shell.bulk.xi[6]) + hex_2ph.shell.bulk.drhodxi_ph[7] * der(hex_2ph.shell.bulk.xi[7]) + hex_2ph.shell.bulk.drhodxi_ph[8] * der(hex_2ph.shell.bulk.xi[8]) + hex_2ph.shell.bulk.drhodxi_ph[9] * der(hex_2ph.shell.bulk.xi[9])
16/39 (1): der(hex_2ph.shell.bulk.xi[4]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[4] - hex_2ph.shell.bulk.xi[4]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[4] - hex_2ph.shell.bulk.xi[4])) / hex_2ph.shell.summary.outline.mass
17/40 (1): hex_2ph.shell.iCom.V_flow_out = abs(hex_2ph.Out1.m_flow / hex_2ph.shell.flueGasOutlet.d)
18/41 (1): hex_2ph.shell.heattransfer.x2 = ClaRa.Basics.Functions.Stepsmoother(0.0, 0.01, -hex_2ph.shell.iCom.V_flow_out)
19/42 (1): $cse67 = max(hex_2ph.shell.heattransfer.x1 + hex_2ph.shell.heattransfer.x2, 1.0)
20/43 (1): hex_2ph.shell.heattransfer.w_0 = (hex_2ph.shell.heattransfer.x1 * hex_2ph.shell.iCom.V_flow_in + hex_2ph.shell.heattransfer.x2 * hex_2ph.shell.iCom.V_flow_out) / ($cse67 * hex_2ph.shell.geo.A_front)
21/44 (1): hex_2ph.shell.heattransfer.w = hex_2ph.shell.heattransfer.w_0 * hex_2ph.shell.geo.A_front / hex_2ph.shell.heattransfer.A_narrowed
22/45 (1): hex_2ph.shell.flueGasOutlet.T = if noEvent(hex_2ph.Out1.m_flow > 0.0) then flueGasPressureSink2.T_const else hex_2ph.shell.bulk.T
23/46 (24): (hex_2ph.shell.flueGasOutlet.d, hex_2ph.shell.flueGasOutlet.kappa, hex_2ph.shell.flueGasOutlet.drhodp_hxi, hex_2ph.shell.flueGasOutlet.drhodh_pxi, hex_2ph.shell.flueGasOutlet.drhodxi_ph, hex_2ph.shell.flueGasOutlet.p_i, hex_2ph.shell.flueGasOutlet.xi_gas) = TILMedia.Internals.GasObjectFunctions.additionalProperties_pTxi(flueGasPressureSink2.p_const, hex_2ph.shell.flueGasOutlet.T, hex_2ph.shell.flueGasOutlet.xi, hex_2ph.shell.flueGasOutlet.gasPointer)
24/70 (1): hex_2ph.shell.flueGasOutlet.h = TILMedia.Internals.GasObjectFunctions.specificEnthalpy_pTxi(flueGasPressureSink2.p_const, hex_2ph.shell.flueGasOutlet.T, hex_2ph.shell.flueGasOutlet.xi, hex_2ph.shell.flueGasOutlet.gasPointer)
25/71 (1): hex_2ph.shell.heattransfer.Delta_T_wo = hex_2ph.shell.heat.T - hex_2ph.shell.flueGasOutlet.T
26/72 (1): hex_2ph.shell.heattransfer.T_prop_am = 0.5 * (hex_2ph.shell.flueGasOutlet.T + hex_2ph.shell.flueGasInlet.T)
27/73 (4): (hex_2ph.shell.heattransfer.properties.transp.Pr, hex_2ph.shell.heattransfer.properties.transp.lambda, hex_2ph.shell.heattransfer.properties.transp.eta, hex_2ph.shell.heattransfer.properties.transp.sigma) = TILMedia.Internals.GasObjectFunctions.transportProperties_pTxi(hex_2ph.shell.heattransfer.properties.p, hex_2ph.shell.heattransfer.T_prop_am, {hex_2ph.shell.bulk.xi[1], hex_2ph.shell.bulk.xi[2], hex_2ph.shell.bulk.xi[3], hex_2ph.shell.bulk.xi[4], hex_2ph.shell.bulk.xi[5], hex_2ph.shell.bulk.xi[6], hex_2ph.shell.bulk.xi[7], hex_2ph.shell.bulk.xi[8], hex_2ph.shell.bulk.xi[9]}, hex_2ph.shell.heattransfer.properties.gasPointer)
28/77 (1): der(hex_2ph.shell.bulk.xi[9]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[9] - hex_2ph.shell.bulk.xi[9]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[9] - hex_2ph.shell.bulk.xi[9])) / hex_2ph.shell.summary.outline.mass
29/78 (1): der(hex_2ph.shell.bulk.xi[8]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[8] - hex_2ph.shell.bulk.xi[8]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[8] - hex_2ph.shell.bulk.xi[8])) / hex_2ph.shell.summary.outline.mass
30/79 (1): der(hex_2ph.shell.bulk.xi[7]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[7] - hex_2ph.shell.bulk.xi[7]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[7] - hex_2ph.shell.bulk.xi[7])) / hex_2ph.shell.summary.outline.mass
31/80 (1): der(hex_2ph.shell.bulk.xi[6]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[6] - hex_2ph.shell.bulk.xi[6]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[6] - hex_2ph.shell.bulk.xi[6])) / hex_2ph.shell.summary.outline.mass
32/81 (1): der(hex_2ph.shell.bulk.xi[5]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[5] - hex_2ph.shell.bulk.xi[5]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[5] - hex_2ph.shell.bulk.xi[5])) / hex_2ph.shell.summary.outline.mass
33/82 (1): der(hex_2ph.shell.bulk.xi[3]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[3] - hex_2ph.shell.bulk.xi[3]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[3] - hex_2ph.shell.bulk.xi[3])) / hex_2ph.shell.summary.outline.mass
34/83 (1): der(hex_2ph.shell.bulk.xi[2]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[2] - hex_2ph.shell.bulk.xi[2]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[2] - hex_2ph.shell.bulk.xi[2])) / hex_2ph.shell.summary.outline.mass
35/84 (1): der(hex_2ph.shell.bulk.xi[1]) = (flueGasFlowSource2.m_flow_const * (hex_2ph.shell.flueGasInlet.xi[1] - hex_2ph.shell.bulk.xi[1]) + hex_2ph.Out1.m_flow * (hex_2ph.shell.flueGasOutlet.xi[1] - hex_2ph.shell.bulk.xi[1])) / hex_2ph.shell.summary.outline.mass
36/85 (1): flueGasFlowSource2.m_flow_const + hex_2ph.Out1.m_flow = hex_2ph.shell.drhodt * hex_2ph.shell.geo.volume
37/86 (1): hex_2ph.shell.flueGasOutlet.xi[9] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[9]
38/87 (1): hex_2ph.shell.flueGasOutlet.xi[8] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[8]
39/88 (1): hex_2ph.shell.flueGasOutlet.xi[7] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[7]
40/89 (1): hex_2ph.shell.flueGasOutlet.xi[6] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[6]
41/90 (1): hex_2ph.shell.flueGasOutlet.xi[5] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 0.9910802775024783 else hex_2ph.shell.bulk.xi[5]
42/91 (1): hex_2ph.shell.flueGasOutlet.xi[4] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[4]
43/92 (1): hex_2ph.shell.flueGasOutlet.xi[3] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[3]
44/93 (1): hex_2ph.shell.flueGasOutlet.xi[2] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[2]
45/94 (1): hex_2ph.shell.flueGasOutlet.xi[1] = if noEvent(hex_2ph.Out1.m_flow > 0.0) then 9.910802775024783e-4 else hex_2ph.shell.bulk.xi[1]
46/95 (1): $cse70 = ClaRa.Basics.Functions.Stepsmoother(0.1, 1e-15, abs(hex_2ph.shell.heattransfer.Delta_T_L))
47/96 (1): hex_2ph.shell.heattransfer.X = 0.5 * hex_2ph.shell.heattransfer.phi * hex_2ph.shell.geo.diameter_t * sqrt(2.0 * hex_2ph.shell.heattransfer.alpha / (215.0 * hex_2ph.shell.heattransfer.s_f))
48/97 (1): $cse68 = tanh(hex_2ph.shell.heattransfer.X)
49/98 (1): hex_2ph.shell.heattransfer.eff_fins * hex_2ph.shell.heattransfer.X = $cse68

Variables:
1: hex_2ph.shell.heattransfer.eff_fins:VARIABLE(protected = true )  "Fin efficiency" type: Real
2: $cse68:VARIABLE(protected = true )  type: Real unreplaceable
3: hex_2ph.shell.heattransfer.X:VARIABLE(protected = true )  "Parameter for fin efficiency calculation" type: Real
4: $cse70:VARIABLE(protected = true )  type: Real unreplaceable
5: hex_2ph.shell.flueGasOutlet.xi[1]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
6: hex_2ph.shell.flueGasOutlet.xi[2]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
7: hex_2ph.shell.flueGasOutlet.xi[3]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
8: hex_2ph.shell.flueGasOutlet.xi[4]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
9: hex_2ph.shell.flueGasOutlet.xi[5]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
10: hex_2ph.shell.flueGasOutlet.xi[6]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
11: hex_2ph.shell.flueGasOutlet.xi[7]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
12: hex_2ph.shell.flueGasOutlet.xi[8]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
13: hex_2ph.shell.flueGasOutlet.xi[9]:VARIABLE(min = 0.0 max = 1.0 unit = "1" nominal = 1.0 )  "Mass fraction" type: Real [9]
14: hex_2ph.shell.drhodt:VARIABLE(protected = true )  "Density derivative" type: Real
15: hex_2ph.shell.bulk.xi[1]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
16: hex_2ph.shell.bulk.xi[2]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
17: hex_2ph.shell.bulk.xi[3]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
18: hex_2ph.shell.bulk.xi[5]:STATE(1)(min = 0.0 max = 1.0 start = 0.9910802775024783 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
19: hex_2ph.shell.bulk.xi[6]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
20: hex_2ph.shell.bulk.xi[7]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
21: hex_2ph.shell.bulk.xi[8]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
22: hex_2ph.shell.bulk.xi[9]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
23: hex_2ph.shell.heattransfer.properties.transp.sigma:VARIABLE(unit = "N/m" protected = true )  "Surface tension" type: Real
24: hex_2ph.shell.heattransfer.properties.transp.lambda:VARIABLE(unit = "W/(m.K)" protected = true )  "Thermal conductivity" type: Real
25: hex_2ph.shell.heattransfer.properties.transp.Pr:VARIABLE(unit = "1" protected = true )  "Prandtl number" type: Real
26: hex_2ph.shell.heattransfer.properties.transp.eta:VARIABLE(min = -1.0 unit = "Pa.s" protected = true )  "Dynamic viscosity" type: Real
27: hex_2ph.shell.heattransfer.T_prop_am:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 protected = true )  "Arithmetic mean for calculation of substance properties" type: Real
28: hex_2ph.shell.heattransfer.Delta_T_wo:VARIABLE(min = 0.0 unit = "K" )  "Temperature difference between wall and fluid outlet temperature" type: Real
29: hex_2ph.shell.flueGasOutlet.h:VARIABLE(unit = "J/kg" nominal = 1000.0 )  "Specific enthalpy" type: Real
30: hex_2ph.shell.flueGasOutlet.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
31: hex_2ph.shell.flueGasOutlet.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
32: hex_2ph.shell.flueGasOutlet.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
33: hex_2ph.shell.flueGasOutlet.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
34: hex_2ph.shell.flueGasOutlet.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
35: hex_2ph.shell.flueGasOutlet.d:VARIABLE(min = 0.0 unit = "kg/m3" )  "Density" type: Real
36: hex_2ph.shell.flueGasOutlet.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" )  "Mass fraction of gasoues condensing component" type: Real
37: hex_2ph.shell.flueGasOutlet.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
38: hex_2ph.shell.flueGasOutlet.kappa:VARIABLE(unit = "1/Pa" )  "Isothermal compressibility" type: Real
39: hex_2ph.shell.flueGasOutlet.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
40: hex_2ph.shell.flueGasOutlet.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
41: hex_2ph.shell.flueGasOutlet.drhodp_hxi:VARIABLE(unit = "s2/m2" )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
42: hex_2ph.shell.flueGasOutlet.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
43: hex_2ph.shell.flueGasOutlet.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
44: hex_2ph.shell.flueGasOutlet.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
45: hex_2ph.shell.flueGasOutlet.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
46: hex_2ph.shell.flueGasOutlet.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
47: hex_2ph.shell.flueGasOutlet.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
48: hex_2ph.shell.flueGasOutlet.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
49: hex_2ph.shell.flueGasOutlet.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
50: hex_2ph.shell.flueGasOutlet.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 )  "Partial pressure" type: Real [10]
51: hex_2ph.shell.flueGasOutlet.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
52: hex_2ph.shell.flueGasOutlet.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
53: hex_2ph.shell.flueGasOutlet.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
54: hex_2ph.shell.flueGasOutlet.T:VARIABLE(min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Temperature" type: Real
55: hex_2ph.shell.heattransfer.w:VARIABLE(unit = "m/s" nominal = 1.0 )  "Flue gas  velocity at free cross section" type: Real
56: hex_2ph.shell.heattransfer.w_0:VARIABLE(unit = "m/s" nominal = 1.0 )  "Flue gas  velocity at narrowed cross section" type: Real
57: $cse67:VARIABLE(protected = true )  type: Real unreplaceable
58: hex_2ph.shell.heattransfer.x2:VARIABLE(protected = true )  type: Real
59: hex_2ph.shell.iCom.V_flow_out:VARIABLE(unit = "m3/s" nominal = 1.0 protected = true )  "Outlet volume flow" type: Real
60: hex_2ph.Out1.m_flow:VARIABLE(flow=true max = 1e60 unit = "kg/s" nominal = 1.0 )  "Mass flow rate from the connection point into the component" type: Real
61: hex_2ph.shell.bulk.xi[4]:STATE(1)(min = 0.0 max = 1.0 start = 9.910802775024783e-4 unit = "1" fixed = true nominal = 1.0 stateSelect=StateSelect.prefer )  "Mass fraction" type: Real [9]
62: hex_2ph.shell.bulk.h:STATE(1)(start = hex_2ph.shell.h_start unit = "J/kg" fixed = true nominal = 1000.0 stateSelect=StateSelect.prefer )  "Specific enthalpy" type: Real
63: hex_2ph.wall.Q_flow[4]:VARIABLE(unit = "W" nominal = 1e5 )  "Heat flow through material" type: Real [4]
64: hex_2ph.shell.heat.T:VARIABLE(flow=false min = 0.0 start = 288.15 unit = "K" nominal = 300.0 )  "Port temperature" type: Real
65: $cse73:VARIABLE(protected = true )  type: Real unreplaceable
66: $cse72:VARIABLE(protected = true )  type: Real unreplaceable
67: hex_2ph.shell.heattransfer.Delta_T_U:VARIABLE(min = 0.0 unit = "K" )  "Upper temperature difference" type: Real
68: hex_2ph.shell.heattransfer.Delta_T_wi:VARIABLE(min = 0.0 unit = "K" )  "Temperature difference between wall and fluid inlet temperature" type: Real
69: hex_2ph.shell.heattransfer.Delta_T_L:VARIABLE(min = 0.0 unit = "K" )  "Lower temperature difference" type: Real
70: $cse71:VARIABLE(protected = true )  type: Real unreplaceable
71: hex_2ph.shell.heattransfer.Delta_T_mean:VARIABLE(min = 0.0 unit = "K" )  "Mean temperature" type: Real
72: hex_2ph.shell.heattransfer.alpha:VARIABLE(min = 0.0 unit = "W/(m2.K)" nominal = 1.0 )  type: Real
73: hex_2ph.shell.heattransfer.Nu:VARIABLE()  "Nusselt number" type: Real
74: hex_2ph.shell.heattransfer.Re:VARIABLE()  "Reynolds number" type: Real
75: hex_2ph.shell.heattransfer.properties.d:VARIABLE(min = 0.0 unit = "kg/m3" protected = true )  "Density" type: Real
76: hex_2ph.shell.heattransfer.properties.p_i[9]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
77: hex_2ph.shell.heattransfer.properties.xi_gas:VARIABLE(min = 0.0 max = 1.0 unit = "1" protected = true )  "Mass fraction of gasoues condensing component" type: Real
78: hex_2ph.shell.heattransfer.properties.drhodxi_ph[4]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
79: hex_2ph.shell.heattransfer.properties.p_i[5]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
80: hex_2ph.shell.heattransfer.properties.p_i[1]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
81: hex_2ph.shell.heattransfer.properties.drhodxi_ph[8]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
82: hex_2ph.shell.heattransfer.properties.p_i[2]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
83: hex_2ph.shell.heattransfer.properties.drhodxi_ph[1]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
84: hex_2ph.shell.heattransfer.properties.drhodp_hxi:VARIABLE(unit = "s2/m2" protected = true )  "Derivative of density wrt pressure at specific enthalpy and mass fraction" type: Real
85: hex_2ph.shell.heattransfer.properties.kappa:VARIABLE(unit = "1/Pa" protected = true )  "Isothermal compressibility" type: Real
86: hex_2ph.shell.heattransfer.properties.p_i[6]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
87: hex_2ph.shell.heattransfer.properties.drhodxi_ph[7]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
88: hex_2ph.shell.heattransfer.properties.p_i[8]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
89: hex_2ph.shell.heattransfer.properties.drhodxi_ph[5]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
90: hex_2ph.shell.heattransfer.properties.drhodxi_ph[9]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
91: hex_2ph.shell.heattransfer.properties.drhodxi_ph[2]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
92: hex_2ph.shell.heattransfer.properties.p_i[10]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
93: hex_2ph.shell.heattransfer.properties.drhodh_pxi:VARIABLE(unit = "kg.s2/m5" protected = true )  "Derivative of density wrt specific enthalpy at constant pressure and mass fraction" type: Real
94: hex_2ph.shell.heattransfer.properties.drhodxi_ph[3]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
95: hex_2ph.shell.heattransfer.properties.p_i[4]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
96: hex_2ph.shell.heattransfer.properties.p_i[3]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
97: hex_2ph.shell.heattransfer.properties.p_i[7]:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 protected = true )  "Partial pressure" type: Real [10]
98: hex_2ph.shell.heattransfer.properties.drhodxi_ph[6]:VARIABLE(unit = "kg/(m3)" protected = true )  "Derivative of density wrt mass fraction of water at constant pressure and specific enthalpy" type: Real [9]
[/var/lib/jenkins1/ws/OpenModelicaLibraryTestingWork/OpenModelica/OMCompiler/Compiler/BackEnd/BackendDAEUtil.mo:9805:5-9806:77:writable] Error: Internal error BackendDAEUtil.traverseEqSystemStrongComponents failed with function:
omc_DAEMode_traverserStrongComponents
Notification: Performance of <failed> postOpt createDAEmodeBDAE (simulation): time 0.00932/5.167, allocations: 7.12 MB / 1.862 GB, free: 177.9 MB / 0.9358 GB
Error: post-optimization module createDAEmodeBDAE (simulation) failed.
Error: Internal error SimCode DAEmode: The model ClaRa.Components.HeatExchangers.Check.Test_HEXvle2gas_L3_1ph_BU could not be translated