Environment - simulationEnvironment:
startTime=0
stopTime=10000
tolerance=1e-06
numberOfIntervals=2500
stepSize=4
Regular simulation: ./ClaRa_dev_ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning  -abortSlowSimulation -alarm=480 -s cvode -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 xloc[0] is 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/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/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_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
|                 | |       | ((e_Filter_dynamic.flueGasOutlet.xi[7] >= 0.0 and e_Filter_dynamic.flueGasOutlet.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasOutlet.xi[7] <= 1.0, has value: -5.68669e-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_dynamic.flueGasOutlet.xi_dryGas[7] >= 0.0 and e_Filter_dynamic.flueGasOutlet.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -6.5368e-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
|                 | |       | ((e_Filter_dynamic.flueGasOutlet.x[7] >= 0.0 and e_Filter_dynamic.flueGasOutlet.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasOutlet.x[7] <= 1.0, has value: -4.57751e-20"
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_dynamic.flueGasOutlet.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.flueGasOutlet.p_i[7], has value: -4.70929e-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 1.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi[7] >= 0.0 and e_Filter_dynamic.bulk.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[7] <= 1.0, has value: -5.68669e-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_dynamic.bulk.xi_dryGas[7] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[7] <= 1.0, has value: -6.5368e-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
|                 | |       | ((e_Filter_dynamic.bulk.x[7] >= 0.0 and e_Filter_dynamic.bulk.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[7] <= 1.0, has value: -4.57751e-20"
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_dynamic.bulk.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.bulk.p_i[7], has value: -4.70929e-15"
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[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: -8.36273e-23"
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: -8.11706e-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[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: -8.97737e-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[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: -8.71364e-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[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: -8.75299e-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[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: -1.39734e-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[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[2], has value: -8.91055e-18"
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: -1.42249e-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[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: -8.36273e-23"
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: -8.11706e-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[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: -8.97737e-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[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: -8.71364e-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[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: -8.75299e-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[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: -1.39734e-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[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[2], has value: -8.91055e-18"
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: -1.42249e-18"
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 8.000000
|                 | |       | ((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: -1.97704e-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 8.000000
|                 | |       | ((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: -2.12234e-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 8.000000
|                 | |       | ((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: -1.31692e-24"
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 8.000000
|                 | |       | ((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: -1.34062e-19"
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 8.000000
|                 | |       | ((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: -1.97704e-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 8.000000
|                 | |       | ((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: -2.12234e-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 8.000000
|                 | |       | ((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: -1.31692e-24"
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 8.000000
|                 | |       | ((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: -1.34062e-19"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/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/ClaRa 1.8.2-main/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: -2.89782e-70"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 10.000000
|                 | |       | ((e_Filter_dynamic.chemicalReactions.xi_aux[7] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[7] <= 1.0, has value: -4.41988e-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 10.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.xi_dryGas[7] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[7] <= 1.0, has value: -5.08225e-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 10.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.x[7] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[7] <= 1.0, has value: -3.55692e-20"
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_dynamic.flueGasInlet.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.p_i[7], has value: -3.55692e-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 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 1.8.2-main/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: -5.29354e-12"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 10.000000
|                 | |       | ((e_Filter_dynamic.chemicalReactions.xi_aux[4] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[4] <= 1.0, has value: -1.98581e-35"
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 10.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.xi_dryGas[4] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[4] <= 1.0, has value: -2.28341e-35"
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 10.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.x[4] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[4] <= 1.0, has value: -1.09791e-35"
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_dynamic.flueGasInlet.p_i[4] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.p_i[4], has value: -1.09791e-30"
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 10.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi[4] >= 0.0 and e_Filter_dynamic.bulk.xi[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[4] <= 1.0, has value: -1.98581e-35"
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 10.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi_dryGas[4] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[4] <= 1.0, has value: -2.28341e-35"
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 10.000000
|                 | |       | ((e_Filter_dynamic.bulk.x[4] >= 0.0 and e_Filter_dynamic.bulk.x[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[4] <= 1.0, has value: -1.09791e-35"
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 10.000000
|                 | |       | ((e_Filter_dynamic.bulk.p_i[4] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.bulk.p_i[4], has value: -1.09791e-30"
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 12.000000
|                 | |       | ((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: -2.35072e-17"
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 12.000000
|                 | |       | ((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: -2.52349e-17"
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 12.000000
|                 | |       | ((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: -1.56628e-17"
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 12.000000
|                 | |       | ((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: -2.35072e-17"
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 12.000000
|                 | |       | ((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: -2.52349e-17"
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 12.000000
|                 | |       | ((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: -1.56628e-17"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/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: -26.735"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/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: -29.718"
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 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 152.000000
|                 | |       | ((deSO_ideal_L1_1.chemicalReactions.xi_aux[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.chemicalReactions.xi_aux[7], has value: -1.61508e-28"
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: -0.0900742"
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: -0.0900742"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 4200.000000
|                 | |       | ((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: -1.33407e-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 4200.000000
|                 | |       | ((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: -1.53342e-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 4200.000000
|                 | |       | ((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: -1.07422e-27"
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 4200.000000
|                 | |       | ((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: -1.33407e-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 4200.000000
|                 | |       | ((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: -1.53342e-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 4200.000000
|                 | |       | ((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: -1.07422e-27"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 4202.000000
|                 | |       | ((e_Filter_dynamic.chemicalReactions.xi_aux[2] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[2] <= 1.0, has value: -3.78526e-28"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 4202.000000
|                 | |       | ((e_Filter_dynamic.chemicalReactions.xi_aux[9] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[9] <= 1.0, has value: -8.28341e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.xi_dryGas[2] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[2] <= 1.0, has value: -4.35088e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.xi_dryGas[8] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[8] <= 1.0, has value: -9.52116e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.x[2] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[2] <= 1.0, has value: -4.78793e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.x[9] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[9] <= 1.0, has value: -1.72328e-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 4202.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.p_i[2], has value: -6.28146e-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 4202.000000
|                 | |       | ((e_Filter_dynamic.flueGasInlet.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.p_i[9], has value: -2.26083e-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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi[2] >= 0.0 and e_Filter_dynamic.bulk.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[2] <= 1.0, has value: -3.78526e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi[9] >= 0.0 and e_Filter_dynamic.bulk.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[9] <= 1.0, has value: -8.28341e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi_dryGas[2] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[2] <= 1.0, has value: -4.35088e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.xi_dryGas[8] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[8] <= 1.0, has value: -9.52116e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.x[2] >= 0.0 and e_Filter_dynamic.bulk.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[2] <= 1.0, has value: -4.78793e-28"
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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.x[9] >= 0.0 and e_Filter_dynamic.bulk.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[9] <= 1.0, has value: -1.72328e-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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.bulk.p_i[2], has value: -6.28197e-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 4202.000000
|                 | |       | ((e_Filter_dynamic.bulk.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.bulk.p_i[9], has value: -2.26101e-22"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 6058.000000
|                 | |       | ((deSO_ideal_L1_1.chemicalReactions.xi_aux[1] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.chemicalReactions.xi_aux[1], has value: -2.85072e-32"
LOG_ASSERT        | info    | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.2-main/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable]
|                 | |       | The following assertion has been violated at time 6066.000000
|                 | |       | ((deSO_ideal_L1_1.chemicalReactions.xi_aux[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.chemicalReactions.xi_aux[2], has value: -2.9153e-31"
LOG_STATS         | info    | ### STATISTICS ###
|                 | |       | | timer
|                 | |       | | |     0.102071s          reading init.xml
|                 | |       | | |   0.00813023s          reading info.xml
|                 | |       | | |    0.0005862s [  0.0%] pre-initialization
|                 | |       | | |    0.0438488s [  2.1%] initialization
|                 | |       | | |  0.000285576s [  0.0%] steps
|                 | |       | | |     0.108421s [  5.1%] solver (excl. callbacks)
|                 | |       | | |            0s [  0.0%] creating output-file
|                 | |       | | |   0.00326809s [  0.2%] event-handling
|                 | |       | | |    0.0190363s [  0.9%] overhead
|                 | |       | | |      1.95642s [ 91.8%] simulation
|                 | |       | | |      2.13187s [100.0%] total
|                 | |       | | events
|                 | |       | | |    13 state events
|                 | |       | | |     0 time events
|                 | |       | | solver: cvode
|                 | |       | | |  6417 steps taken
|                 | |       | | |  8560 calls of functionODE
|                 | |       | | |   130 evaluations of jacobian
|                 | |       | | |    95 error test failures
|                 | |       | | |     6 convergence test failures
|                 | |       | | | 0s time of jacobian evaluation
LOG_SUCCESS       | info    | The simulation finished successfully.