Environment - simulationEnvironment:
startTime=0
stopTime=10000
tolerance=1e-06
numberOfIntervals=2500
stepSize=4
Regular simulation: ./ClaRa_ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning  -abortSlowSimulation -alarm=480  -emit_protected -lv LOG_STATS
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=inf J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.90799e+16 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=inf J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.90799e+16 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=inf J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.90799e+16 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=inf J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.27148e+15 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=inf J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_NLS           | error   | residualFunc2930: Iteration variable `deSO_ideal_L1_1.chemicalReactions.m_flow_aux` is inf or nan.
LOG_ASSERT        | debug   | residualFunc2930 failed at time=0.
|                 | |       | For more information please use -lv LOG_NLS.
LOG_STDOUT        | warning | While solving non-linear system an assertion failed during initialization.
|                 | |       | | The non-linear solver tries to solve the problem that could take some time.
|                 | |       | | It could help to provide better start-values for the iteration variables.
|                 | |       | | For more information simulate with -lv LOG_NLS_V
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.66945e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.12773e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.21702e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.20344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.21349e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.30324e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.48765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.60054e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.57077e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55629e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55629e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55629e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.13381e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=5.83382e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-3.2008e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.13381e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.65472e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89713e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5925e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89714e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89713e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.65921e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89713e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.77031e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.69468e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.77032e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.77031e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.75079e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.33533e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.15662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=7.7259e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.15662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.2494e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.79432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.61854e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54282e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.57978e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54886e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.15369e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=9.75856e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=7.45723e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=5.06385e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.07909e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=9.06003e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.07909e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.40655e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.93404e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.50982e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5285e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5574e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04482e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04482e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.64061e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.63908e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-354660 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.66945e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.12773e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.21702e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.20344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.21349e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.30324e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.48765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.60054e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5235e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55152e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.66945e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.12773e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.21702e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.20344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.21349e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.30324e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.48765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.60054e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5235e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55152e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04256e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04256e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.6444e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.64282e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-354720 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04256e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04256e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.6444e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.64282e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-354720 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.13381e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=5.83382e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-3.2008e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.13381e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.65472e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89713e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5925e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89714e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89713e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.65921e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.89713e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.77031e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.69468e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.81068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.77032e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.77031e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.75079e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.33533e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.15662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=7.7259e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.15662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.2494e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.79432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.61854e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54282e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.57978e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54886e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.15369e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=9.75856e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=7.45723e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=5.06385e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.07909e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=9.06003e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=3.07909e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.40655e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.93404e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.50982e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.62919e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5285e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.58739e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5574e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04482e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.53802e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04482e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.64061e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.63908e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-354660 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.66945e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.12773e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.21702e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.20344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.21349e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.30324e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.48765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.60054e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5235e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55152e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.03803e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.81573e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.66945e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.12773e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.21702e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.26928e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.20344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.21349e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.30324e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.73168e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.48765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.60054e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5235e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.55152e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.56108e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54206e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54678e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04256e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.5539e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-7.04256e+06 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.6444e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.64282e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-354720 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.25669e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.25669e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.25669e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.02556e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.79004e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.25669e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.25669e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.02556e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-2.79004e+07 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.62103e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-1.11678e+08 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.15328e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.25669e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.19131e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.19135e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54541e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.29012e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.71432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54541e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.54541e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.49329e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.39881e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.24126e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.01196e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=7.36564e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=4.72904e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=2.6993e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=1.38352e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=6.23027e+06 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-326347 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-771839 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_STDOUT        | info    | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=1): h (=-592993 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((deSO_ideal_L1_1.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.summary.outline.H, has value: -150.781"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((deNOx.flueGasInlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.flueGasInlet.p_i[10], has value: -89.5172"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((deNOx.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.summary.outline.H, has value: -5.65921"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((e_Filter_dynamic.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.summary.outline.H, has value: -26.1711"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((e_Filter_dynamic1.flueGasInlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.flueGasInlet.p_i[10], has value: -1.35007e-11"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((e_Filter_dynamic1.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.summary.outline.H, has value: -1.13184"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((e_Filter_dynamic2.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.summary.outline.H, has value: -1.33713"
LOG_ASSERT        | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L4.mo:36:5-36:81:writable]
|                 | |       | The following assertion has been violated at time 0.000000
|                 | |       | ((pipeFlowGas_L4_Simple.summary.outline.H_tot >= 0.0)) --> "Variable violating min constraint: 0.0 <= pipeFlowGas_L4_Simple.summary.outline.H_tot, has value: -0.267508"
LOG_SUCCESS       | info    | The initialization finished successfully with 3 homotopy steps.
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[1] <= 1.0, has value: -2.97585e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] <= 1.0, has value: -3.1893e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.x[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[1] <= 1.0, has value: -1.98516e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi[1] >= 0.0 and deSO_ideal_L1_1.bulk.xi[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[1] <= 1.0, has value: -2.97585e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi_dryGas[1] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[1] <= 1.0, has value: -3.1893e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.x[1] >= 0.0 and deSO_ideal_L1_1.bulk.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[1] <= 1.0, has value: -1.98516e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[2] <= 1.0, has value: -8.16735e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[4] <= 1.0, has value: -3.27601e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi[9] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[9] <= 1.0, has value: -6.70946e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] <= 1.0, has value: -9.38781e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] <= 1.0, has value: -3.76555e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] <= 1.0, has value: -7.71206e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.x[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[2] <= 1.0, has value: -1.03392e-19"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.x[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[4] <= 1.0, has value: -1.81322e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.x[9] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[9] <= 1.0, has value: -1.39696e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[2], has value: -1.05583e-14"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.p_i[4] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[4], has value: -1.85166e-17"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[9], has value: -1.42658e-16"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi[2] >= 0.0 and e_Filter_dynamic2.bulk.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[2] <= 1.0, has value: -8.16735e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi[4] >= 0.0 and e_Filter_dynamic2.bulk.xi[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[4] <= 1.0, has value: -3.27601e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi[9] >= 0.0 and e_Filter_dynamic2.bulk.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[9] <= 1.0, has value: -6.70946e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi_dryGas[2] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[2] <= 1.0, has value: -9.38781e-20"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi_dryGas[4] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[4] <= 1.0, has value: -3.76555e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi_dryGas[8] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[8] <= 1.0, has value: -7.71206e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.x[2] >= 0.0 and e_Filter_dynamic2.bulk.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[2] <= 1.0, has value: -1.03392e-19"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.x[4] >= 0.0 and e_Filter_dynamic2.bulk.x[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[4] <= 1.0, has value: -1.81322e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.x[9] >= 0.0 and e_Filter_dynamic2.bulk.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[9] <= 1.0, has value: -1.39696e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[2], has value: -1.05583e-14"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.p_i[4] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[4], has value: -1.85166e-17"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 1.000000
|                 | |       | ((e_Filter_dynamic2.bulk.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[9], has value: -1.42658e-16"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[2] <= 1.0, has value: -1.81662e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] <= 1.0, has value: -1.95004e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.x[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[2] <= 1.0, has value: -1.90148e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[2], has value: -1.9357e-16"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi[2] >= 0.0 and deSO_ideal_L1_1.bulk.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[2] <= 1.0, has value: -1.81662e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi_dryGas[2] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[2] <= 1.0, has value: -1.95004e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.x[2] >= 0.0 and deSO_ideal_L1_1.bulk.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[2] <= 1.0, has value: -1.90148e-21"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[2], has value: -1.9357e-16"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[7] <= 1.0, has value: -8.2496e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -9.48235e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.x[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[7] <= 1.0, has value: -6.64619e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.flueGasOutlet.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[7], has value: -6.78708e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi[7] >= 0.0 and e_Filter_dynamic2.bulk.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[7] <= 1.0, has value: -8.2496e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.bulk.xi_dryGas[7] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[7] <= 1.0, has value: -9.48235e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.bulk.x[7] >= 0.0 and e_Filter_dynamic2.bulk.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[7] <= 1.0, has value: -6.64619e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 2.000000
|                 | |       | ((e_Filter_dynamic2.bulk.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[7], has value: -6.78708e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[7] <= 1.0, has value: -5.86783e-24"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi[9] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[9] <= 1.0, has value: -3.34595e-23"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -6.2991e-24"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] <= 1.0, has value: -3.59187e-23"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.x[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[7] <= 1.0, has value: -3.9086e-24"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.x[9] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[9] <= 1.0, has value: -5.75999e-23"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[7], has value: -3.97896e-19"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.flueGasOutlet.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[9], has value: -5.86366e-18"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi[7] >= 0.0 and deSO_ideal_L1_1.bulk.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[7] <= 1.0, has value: -5.86783e-24"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi[9] >= 0.0 and deSO_ideal_L1_1.bulk.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[9] <= 1.0, has value: -3.34595e-23"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi_dryGas[7] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[7] <= 1.0, has value: -6.2991e-24"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.xi_dryGas[8] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[8] <= 1.0, has value: -3.59187e-23"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.x[7] >= 0.0 and deSO_ideal_L1_1.bulk.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[7] <= 1.0, has value: -3.9086e-24"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.x[9] >= 0.0 and deSO_ideal_L1_1.bulk.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[9] <= 1.0, has value: -5.75999e-23"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[7], has value: -3.97896e-19"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 4.000000
|                 | |       | ((deSO_ideal_L1_1.bulk.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[9], has value: -5.86366e-18"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Components/BoundaryConditions/BoundaryGas_pTxi.mo:46:3-46:42:writable]
|                 | |       | The following assertion has been violated at time 10.000000
|                 | |       | ((idealGasPressureSink1.s_port >= 0.0)) --> "Variable violating min constraint: 0.0 <= idealGasPressureSink1.s_port, has value: -589.924"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 10.000000
|                 | |       | ((e_Filter_dynamic1.flueGasOutlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.flueGasOutlet.p_i[10], has value: -1.64736e-11"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/Fundamentals/PressureLoss/Generic_PL/PressureLoss_L2.mo:7:3-7:34:writable]
|                 | |       | The following assertion has been violated at time 10.000000
|                 | |       | ((e_Filter_dynamic.pressureLoss.Delta_p >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.pressureLoss.Delta_p, has value: -4.23128e-12"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/Fundamentals/PressureLoss/Generic_PL/PressureLoss_L2.mo:7:3-7:34:writable]
|                 | |       | The following assertion has been violated at time 10.000000
|                 | |       | ((e_Filter_dynamic1.pressureLoss.Delta_p >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.pressureLoss.Delta_p, has value: -5.2891e-12"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Components/BoundaryConditions/BoundaryGas_Txim_flow.mo:48:3-48:42:writable]
|                 | |       | The following assertion has been violated at time 14.000000
|                 | |       | ((idealGasFlowSource_XRG4.s_port >= 0.0)) --> "Variable violating min constraint: 0.0 <= idealGasFlowSource_XRG4.s_port, has value: -26.7417"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Components/BoundaryConditions/BoundaryGas_Txim_flow.mo:48:3-48:42:writable]
|                 | |       | The following assertion has been violated at time 24.000000
|                 | |       | ((idealGasFlowSource_XRG.s_port >= 0.0)) --> "Variable violating min constraint: 0.0 <= idealGasFlowSource_XRG.s_port, has value: -29.7215"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 44.000000
|                 | |       | ((e_Filter_dynamic1.bulk.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.bulk.p_i[10], has value: -2.4406e-12"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 594.000000
|                 | |       | ((e_Filter_dynamic.chemicalReactions.xi_aux[1] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[1] <= 1.0, has value: -7.65063e-15"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 594.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.xi_dryGas[1] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[1] <= 1.0, has value: -8.79383e-15"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 594.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.x[1] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[1] <= 1.0, has value: -6.16044e-15"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable]
|                 | |       | The following assertion has been violated at time 594.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi[1] >= 0.0 and e_Filter_dynamic.bulk.xi[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[1] <= 1.0, has value: -7.65063e-15"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable]
|                 | |       | The following assertion has been violated at time 594.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi_dryGas[1] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[1] <= 1.0, has value: -8.79383e-15"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable]
|                 | |       | The following assertion has been violated at time 594.000000
|                 | |       | ((e_Filter_dynamic.bulk.x[1] >= 0.0 and e_Filter_dynamic.bulk.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[1] <= 1.0, has value: -6.16044e-15"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 680.000000
|                 | |       | ((deNOx.flueGasOutlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.flueGasOutlet.p_i[10], has value: -0.0905043"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable]
|                 | |       | The following assertion has been violated at time 680.000000
|                 | |       | ((deNOx.bulk.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.bulk.p_i[10], has value: -0.0905043"
LOG_STATS         | info    | ### STATISTICS ###
|                 | |       | | timer
|                 | |       | | |     0.106311s          reading init.xml
|                 | |       | | |    0.0083668s          reading info.xml
|                 | |       | | |    0.0031118s [  0.2%] pre-initialization
|                 | |       | | |    0.0430035s [  2.2%] initialization
|                 | |       | | |  0.000223049s [  0.0%] steps
|                 | |       | | |    0.0378872s [  2.0%] solver (excl. callbacks)
|                 | |       | | |    0.0226442s [  1.2%] creating output-file
|                 | |       | | |     0.317033s [ 16.3%] event-handling
|                 | |       | | |    0.0192267s [  1.0%] overhead
|                 | |       | | |      1.49895s [ 77.2%] simulation
|                 | |       | | |      1.94208s [100.0%] total
|                 | |       | | events
|                 | |       | | |    13 state events
|                 | |       | | |     0 time events
|                 | |       | | solver: dassl
|                 | |       | | |  1240 steps taken
|                 | |       | | |  2094 calls of functionODE
|                 | |       | | |   423 evaluations of jacobian
|                 | |       | | |   107 error test failures
|                 | |       | | |    18 convergence test failures
|                 | |       | | | 0.440254s time of jacobian evaluation
LOG_SUCCESS       | info    | The simulation finished successfully.