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 -lv LOG_STATS


TILMedia-Error: Product license not valid

TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.10492e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.87027e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.21819e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.00135e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.87496e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.4119e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.78828e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=8.39998e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-919778 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.10492e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.87027e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.21819e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.00135e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.87496e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.4119e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.78828e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=8.39998e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-919778 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.10492e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.87027e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.21819e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.00135e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.87496e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.4119e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.78828e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=8.39998e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-919778 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.10492e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.87027e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.21819e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.00135e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.87496e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.4119e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.78828e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=8.39998e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-919778 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.26927e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.26927e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.50536e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.53272e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.10492e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.87027e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.47102e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.65092e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.21819e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.00135e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.87496e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.4119e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.78828e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=8.39998e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-919778 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-3.35654e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.23681e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-3.35654e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.16041e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-1.94412e+09 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.66125e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-2.81508e+10 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=7.36507e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.76345e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27148e+15 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): 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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27125e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.27126e+10 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.79315e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.12577e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=7.85893e+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}
TILMedia-Error(ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, Gas_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-323103 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}
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
TILMedia-Fatal-Error(CModelMap::getGasModel): No valid product license found, medium name "TILMedia.Ash|TILMediaXTR.Carbon_Monoxide|TILMediaXTR.Carbon_Dioxide|TILMediaXTR.Sulfur_Dioxide|TILMediaXTR.Nitrogen|TILMediaXTR.Oxygen|TILMediaXTR.Nitrous_Oxide|TILMediaXTR.Water|TILMediaXTR.Ammonia|TILMediaXTR.Argon" is not allowed
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | deSO_ideal_L1_1.summary.outline.H >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.summary.outline.H, has value: -150.781
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | deNOx.flueGasInlet.p_i[10] >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= deNOx.flueGasInlet.p_i[10], has value: -89.5172
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | deNOx.summary.outline.H >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= deNOx.summary.outline.H, has value: -5.65921
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | e_Filter_dynamic.summary.outline.H >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= e_Filter_dynamic.summary.outline.H, has value: -26.1711
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | e_Filter_dynamic1.flueGasInlet.p_i[10] >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= e_Filter_dynamic1.flueGasInlet.p_i[10], has value: -1.35007e-11
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | e_Filter_dynamic1.summary.outline.H >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= e_Filter_dynamic1.summary.outline.H, has value: -1.13184
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | e_Filter_dynamic2.summary.outline.H >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.summary.outline.H, has value: -1.33713
assert            | warning | The following assertion has been violated at time 0.000000
|                 | |       | pipeFlowGas_L4_Simple.summary.outline.H_tot >= 0.0
assert            | warning | Variable violating min constraint: 0.0 <= pipeFlowGas_L4_Simple.summary.outline.H_tot, has value: -0.267508
LOG_SUCCESS       | info    | The initialization finished successfully with 3 homotopy steps.
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[4] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[4] <= 1.0, has value: -9.47953e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[7] <= 1.0, has value: -7.5944e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] <= 1.0, has value: -1.08961e-22
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -8.72925e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.x[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[4] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[4] <= 1.0, has value: -5.24678e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.x[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[7] <= 1.0, has value: -6.11833e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.p_i[4] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[4], has value: -5.358e-18
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.p_i[7] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[7], has value: -6.24803e-18
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.xi[4] >= 0.0 and e_Filter_dynamic2.bulk.xi[4] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[4] <= 1.0, has value: -9.47953e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.xi[7] >= 0.0 and e_Filter_dynamic2.bulk.xi[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[7] <= 1.0, has value: -7.5944e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.xi_dryGas[4] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[4] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[4] <= 1.0, has value: -1.08961e-22
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.xi_dryGas[7] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[7] <= 1.0, has value: -8.72925e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.x[4] >= 0.0 and e_Filter_dynamic2.bulk.x[4] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[4] <= 1.0, has value: -5.24678e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.x[7] >= 0.0 and e_Filter_dynamic2.bulk.x[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[7] <= 1.0, has value: -6.11833e-23
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.p_i[4] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[4], has value: -5.358e-18
assert            | info    | The following assertion has been violated at time 1.000000
|                 | |       | e_Filter_dynamic2.bulk.p_i[7] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[7], has value: -6.24803e-18
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[7] <= 1.0, has value: -7.0924e-22
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi[9] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[9] <= 1.0, has value: -1.92415e-23
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -7.61327e-22
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] <= 1.0, has value: -2.06546e-23
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.x[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[7] <= 1.0, has value: -4.72449e-22
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.x[9] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[9] <= 1.0, has value: -3.31252e-23
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.p_i[7] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[7], has value: -4.80953e-17
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.p_i[9] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[9], has value: -3.37215e-18
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi[7] >= 0.0 and deSO_ideal_L1_1.bulk.xi[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[7] <= 1.0, has value: -7.0924e-22
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi[9] >= 0.0 and deSO_ideal_L1_1.bulk.xi[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[9] <= 1.0, has value: -1.92415e-23
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi_dryGas[7] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[7] <= 1.0, has value: -7.61327e-22
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi_dryGas[8] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[8] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[8] <= 1.0, has value: -2.06546e-23
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.x[7] >= 0.0 and deSO_ideal_L1_1.bulk.x[7] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[7] <= 1.0, has value: -4.72449e-22
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.x[9] >= 0.0 and deSO_ideal_L1_1.bulk.x[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[9] <= 1.0, has value: -3.31252e-23
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.p_i[7] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[7], has value: -4.80953e-17
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | deSO_ideal_L1_1.bulk.p_i[9] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[9], has value: -3.37215e-18
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[2] <= 1.0, has value: -8.85041e-26
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi[9] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[9] <= 1.0, has value: -1.72879e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] <= 1.0, has value: -1.01729e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] <= 1.0, has value: -1.98712e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.x[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[2] <= 1.0, has value: -1.12038e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.x[9] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[9] <= 1.0, has value: -3.59947e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.p_i[2] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[2], has value: -1.14414e-20
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.flueGasOutlet.p_i[9] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[9], has value: -3.67577e-20
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.xi[2] >= 0.0 and e_Filter_dynamic2.bulk.xi[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[2] <= 1.0, has value: -8.85041e-26
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.xi[9] >= 0.0 and e_Filter_dynamic2.bulk.xi[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[9] <= 1.0, has value: -1.72879e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.xi_dryGas[2] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[2] <= 1.0, has value: -1.01729e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.xi_dryGas[8] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[8] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[8] <= 1.0, has value: -1.98712e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.x[2] >= 0.0 and e_Filter_dynamic2.bulk.x[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[2] <= 1.0, has value: -1.12038e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.x[9] >= 0.0 and e_Filter_dynamic2.bulk.x[9] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[9] <= 1.0, has value: -3.59947e-25
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.p_i[2] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[2], has value: -1.14414e-20
assert            | info    | The following assertion has been violated at time 2.000000
|                 | |       | e_Filter_dynamic2.bulk.p_i[9] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[9], has value: -3.67577e-20
assert            | info    | The following assertion has been violated at time 4.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[1] <= 1.0, has value: -4.64084e-23
assert            | info    | The following assertion has been violated at time 4.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] <= 1.0, has value: -4.98193e-23
assert            | info    | The following assertion has been violated at time 4.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.x[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[1] <= 1.0, has value: -3.0922e-23
assert            | info    | The following assertion has been violated at time 4.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi[1] >= 0.0 and deSO_ideal_L1_1.bulk.xi[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[1] <= 1.0, has value: -4.64084e-23
assert            | info    | The following assertion has been violated at time 4.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi_dryGas[1] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[1] <= 1.0, has value: -4.98193e-23
assert            | info    | The following assertion has been violated at time 4.000000
|                 | |       | deSO_ideal_L1_1.bulk.x[1] >= 0.0 and deSO_ideal_L1_1.bulk.x[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[1] <= 1.0, has value: -3.0922e-23
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[2] <= 1.0, has value: -3.43424e-22
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] <= 1.0, has value: -3.68665e-22
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.x[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[2] <= 1.0, has value: -3.59451e-22
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.flueGasOutlet.p_i[2] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[2], has value: -3.65921e-17
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi[2] >= 0.0 and deSO_ideal_L1_1.bulk.xi[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[2] <= 1.0, has value: -3.43424e-22
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.bulk.xi_dryGas[2] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[2] <= 1.0, has value: -3.68665e-22
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.bulk.x[2] >= 0.0 and deSO_ideal_L1_1.bulk.x[2] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[2] <= 1.0, has value: -3.59451e-22
assert            | info    | The following assertion has been violated at time 6.000000
|                 | |       | deSO_ideal_L1_1.bulk.p_i[2] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[2], has value: -3.65921e-17
assert            | info    | The following assertion has been violated at time 10.000000
|                 | |       | idealGasPressureSink1.s_port >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= idealGasPressureSink1.s_port, has value: -589.924
assert            | info    | The following assertion has been violated at time 10.000000
|                 | |       | e_Filter_dynamic1.flueGasOutlet.p_i[10] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic1.flueGasOutlet.p_i[10], has value: -1.64736e-11
assert            | info    | The following assertion has been violated at time 10.000000
|                 | |       | e_Filter_dynamic.pressureLoss.Delta_p >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic.pressureLoss.Delta_p, has value: -4.64162e-12
assert            | info    | The following assertion has been violated at time 10.000000
|                 | |       | e_Filter_dynamic1.pressureLoss.Delta_p >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic1.pressureLoss.Delta_p, has value: -5.80203e-12
assert            | info    | The following assertion has been violated at time 14.000000
|                 | |       | idealGasFlowSource_XRG4.s_port >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= idealGasFlowSource_XRG4.s_port, has value: -26.7446
assert            | info    | The following assertion has been violated at time 24.000000
|                 | |       | idealGasFlowSource_XRG.s_port >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= idealGasFlowSource_XRG.s_port, has value: -29.7154
assert            | info    | The following assertion has been violated at time 50.000000
|                 | |       | e_Filter_dynamic1.bulk.p_i[10] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= e_Filter_dynamic1.bulk.p_i[10], has value: -2.4406e-12
assert            | info    | The following assertion has been violated at time 556.000000
|                 | |       | e_Filter_dynamic.chemicalReactions.xi_aux[1] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[1] <= 1.0, has value: -6.21411e-15
assert            | info    | The following assertion has been violated at time 556.000000
|                 | |       | e_Filter_dynamic.flueGasInlet.xi_dryGas[1] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[1] <= 1.0, has value: -7.14266e-15
assert            | info    | The following assertion has been violated at time 556.000000
|                 | |       | e_Filter_dynamic.flueGasInlet.x[1] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[1] <= 1.0, has value: -5.00372e-15
assert            | info    | The following assertion has been violated at time 556.000000
|                 | |       | e_Filter_dynamic.bulk.xi[1] >= 0.0 and e_Filter_dynamic.bulk.xi[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[1] <= 1.0, has value: -6.21411e-15
assert            | info    | The following assertion has been violated at time 556.000000
|                 | |       | e_Filter_dynamic.bulk.xi_dryGas[1] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[1] <= 1.0, has value: -7.14266e-15
assert            | info    | The following assertion has been violated at time 556.000000
|                 | |       | e_Filter_dynamic.bulk.x[1] >= 0.0 and e_Filter_dynamic.bulk.x[1] <= 1.0
assert            | info    | Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[1] <= 1.0, has value: -5.00372e-15
assert            | info    | The following assertion has been violated at time 680.000000
|                 | |       | deNOx.flueGasOutlet.p_i[10] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deNOx.flueGasOutlet.p_i[10], has value: -0.0905016
assert            | info    | The following assertion has been violated at time 680.000000
|                 | |       | deNOx.bulk.p_i[10] >= 0.0
assert            | info    | Variable violating min constraint: 0.0 <= deNOx.bulk.p_i[10], has value: -0.0905016
LOG_STATS         | info    | ### STATISTICS ###
|                 | |       | | timer
|                 | |       | | |     0.116406s          reading init.xml
|                 | |       | | |    0.0107772s          reading info.xml
|                 | |       | | |  0.000585138s [  0.0%] pre-initialization
|                 | |       | | |    0.0626165s [  3.3%] initialization
|                 | |       | | |   0.00022914s [  0.0%] steps
|                 | |       | | |    0.0335191s [  1.7%] solver (excl. callbacks)
|                 | |       | | |            0s [  0.0%] creating output-file
|                 | |       | | |     0.323403s [ 16.8%] event-handling
|                 | |       | | |    0.0170368s [  0.9%] overhead
|                 | |       | | |      1.48725s [ 77.3%] simulation
|                 | |       | | |      1.92464s [100.0%] total
|                 | |       | | events
|                 | |       | | |    13 state events
|                 | |       | | |     0 time events
|                 | |       | | solver: dassl
|                 | |       | | |  1154 steps taken
|                 | |       | | |  1960 calls of functionODE
|                 | |       | | |   428 evaluations of jacobian
|                 | |       | | |    94 error test failures
|                 | |       | | |    24 convergence test failures
|                 | |       | | | 0.457466s time of jacobian evaluation
LOG_SUCCESS       | info    | The simulation finished successfully.