Environment - simulationEnvironment: startTime=0 stopTime=10000 tolerance=1e-06 numberOfIntervals=2500 stepSize=4 Regular simulation: ./ClaRa_ClaRa.Components.FlueGasCleaning.Desulfurization.Check.Test_FlueGasCleaning -abortSlowSimulation -alarm=480 -emit_protected -lv LOG_STATS stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-1.27148e+15 J/kg) < h_min (-262868 J/kg at T=141 K), T limited to 141 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} LOG_NLS | error | residualFunc2930: Iteration variable xloc[0] is nan. assert | debug | residualFunc2930 failed at time=0. | | | | For more information please use -lv LOG_NLS. stdout | warning | While solving non-linear system an assertion failed during initialization. | | | | | The non-linear solver tries to solve the problem that could take some time. | | | | | It could help to provide better start-values for the iteration variables. | | | | | For more information simulate with -lv LOG_NLS_V stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.35949e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.13381e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.83382e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.19753e+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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=2.09705e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.282e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.5925e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.42073e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.50179e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46015e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.48068e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47035e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.4755e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=6.33533e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.15662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=7.7259e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.15662e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.2494e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.79432e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.31632e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56727e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.43104e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.4961e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46286e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.44149e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46286e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46286e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45904e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45145e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.43651e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.15369e+09 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.75856e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=7.45723e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=5.06385e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.07909e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=9.06003e+07 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=3.07909e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.71967e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.40655e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.18885e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.54765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.54765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.54765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.3451e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.54765e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.43939e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.49158e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46503e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.44784e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.47378e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46503e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46503e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46069e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.46503e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.44784e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.44784e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.44784e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-591120 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-386469 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-306536 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.35949e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.73169e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.56109e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.35949e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-591120 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-386471 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-306538 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45344e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=1.45343e+08 J/kg) > h_max (3.44685e+06 J/kg at T=3000 K), T limited to 3000 K, p=102840 Pa, xi={0, 0, 0.21, 0.00099, 0.7, 0.0393, 0, 0.0367, 0, 0.01301} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-591120 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-386471 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} stdout | info | TILMedia-Error(Test_FlueGasCleaning.deSO_ideal_L1_1.chemicalReactions.gasAux, GM_GasMixtureModel_computeSimpleCondensingProperties_phxi, mediumPointerID=6): h (=-306538 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} assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((deSO_ideal_L1_1.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.summary.outline.H, has value: -150.781" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((deNOx.flueGasInlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.flueGasInlet.p_i[10], has value: -89.5172" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((deNOx.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.summary.outline.H, has value: -5.65921" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((e_Filter_dynamic.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.summary.outline.H, has value: -26.1711" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((e_Filter_dynamic1.flueGasInlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.flueGasInlet.p_i[10], has value: -1.35007e-11" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((e_Filter_dynamic1.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.summary.outline.H, has value: -1.13184" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L2_chem.mo:143:5-143:85:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((e_Filter_dynamic2.summary.outline.H >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.summary.outline.H, has value: -1.33713" assert | warning | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/GasVolumes/VolumeGas_L4.mo:36:5-36:81:writable] | | | | The following assertion has been violated at time 0.000000 | | | | ((pipeFlowGas_L4_Simple.summary.outline.H_tot >= 0.0)) --> "Variable violating min constraint: 0.0 <= pipeFlowGas_L4_Simple.summary.outline.H_tot, has value: -0.267508" LOG_SUCCESS | info | The initialization finished successfully with 3 homotopy steps. assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi[9] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[9] <= 1.0, has value: -9.62291e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[8] <= 1.0, has value: -1.03132e-20" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.x[9] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[9] <= 1.0, has value: -1.65853e-20" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[9], has value: -1.68838e-15" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.bulk.xi[9] >= 0.0 and deSO_ideal_L1_1.bulk.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[9] <= 1.0, has value: -9.62291e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.bulk.xi_dryGas[8] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[8] <= 1.0, has value: -1.03132e-20" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.bulk.x[9] >= 0.0 and deSO_ideal_L1_1.bulk.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[9] <= 1.0, has value: -1.65853e-20" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((deSO_ideal_L1_1.bulk.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[9], has value: -1.68838e-15" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi[9] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[9] <= 1.0, has value: -6.42166e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[8] <= 1.0, has value: -7.38126e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.x[9] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[9] <= 1.0, has value: -1.33704e-20" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[9], has value: -1.36538e-15" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.bulk.xi[9] >= 0.0 and e_Filter_dynamic2.bulk.xi[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[9] <= 1.0, has value: -6.42166e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.bulk.xi_dryGas[8] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[8] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[8] <= 1.0, has value: -7.38126e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.bulk.x[9] >= 0.0 and e_Filter_dynamic2.bulk.x[9] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[9] <= 1.0, has value: -1.33704e-20" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 1.000000 | | | | ((e_Filter_dynamic2.bulk.p_i[9] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[9], has value: -1.36538e-15" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[2] <= 1.0, has value: -1.92518e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[4] <= 1.0, has value: -1.32956e-25" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi[7] <= 1.0, has value: -7.35164e-28" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[2] <= 1.0, has value: -2.21287e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[4] <= 1.0, has value: -1.52824e-25" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -8.45021e-28" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.x[2] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[2] <= 1.0, has value: -2.43712e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.x[4] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[4] <= 1.0, has value: -7.35891e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.x[7] >= 0.0 and e_Filter_dynamic2.flueGasOutlet.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.x[7] <= 1.0, has value: -5.92275e-28" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[2], has value: -2.48878e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.p_i[4] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[4], has value: -7.5149e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.flueGasOutlet.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.flueGasOutlet.p_i[7], has value: -6.04831e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.xi[2] >= 0.0 and e_Filter_dynamic2.bulk.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[2] <= 1.0, has value: -1.92518e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.xi[4] >= 0.0 and e_Filter_dynamic2.bulk.xi[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[4] <= 1.0, has value: -1.32956e-25" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.xi[7] >= 0.0 and e_Filter_dynamic2.bulk.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi[7] <= 1.0, has value: -7.35164e-28" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.xi_dryGas[2] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[2] <= 1.0, has value: -2.21287e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.xi_dryGas[4] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[4] <= 1.0, has value: -1.52824e-25" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.xi_dryGas[7] >= 0.0 and e_Filter_dynamic2.bulk.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.xi_dryGas[7] <= 1.0, has value: -8.45021e-28" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.x[2] >= 0.0 and e_Filter_dynamic2.bulk.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[2] <= 1.0, has value: -2.43712e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.x[4] >= 0.0 and e_Filter_dynamic2.bulk.x[4] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[4] <= 1.0, has value: -7.35891e-26" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.x[7] >= 0.0 and e_Filter_dynamic2.bulk.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic2.bulk.x[7] <= 1.0, has value: -5.92275e-28" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[2], has value: -2.48878e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.p_i[4] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[4], has value: -7.5149e-21" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 2.000000 | | | | ((e_Filter_dynamic2.bulk.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic2.bulk.p_i[7], has value: -6.04831e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 4.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[1] <= 1.0, has value: -6.16236e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 4.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[1] <= 1.0, has value: -6.61527e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 4.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.x[1] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[1] <= 1.0, has value: -4.10598e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 4.000000 | | | | ((deSO_ideal_L1_1.bulk.xi[1] >= 0.0 and deSO_ideal_L1_1.bulk.xi[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[1] <= 1.0, has value: -6.16236e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 4.000000 | | | | ((deSO_ideal_L1_1.bulk.xi_dryGas[1] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[1] <= 1.0, has value: -6.61527e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 4.000000 | | | | ((deSO_ideal_L1_1.bulk.x[1] >= 0.0 and deSO_ideal_L1_1.bulk.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[1] <= 1.0, has value: -4.10598e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[7] <= 1.0, has value: -7.93386e-22" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[7] <= 1.0, has value: -8.51698e-22" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.x[7] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[7] <= 1.0, has value: -5.2848e-22" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[7], has value: -5.37993e-17" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.bulk.xi[7] >= 0.0 and deSO_ideal_L1_1.bulk.xi[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[7] <= 1.0, has value: -7.93386e-22" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.bulk.xi_dryGas[7] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[7] <= 1.0, has value: -8.51698e-22" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.bulk.x[7] >= 0.0 and deSO_ideal_L1_1.bulk.x[7] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[7] <= 1.0, has value: -5.2848e-22" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 8.000000 | | | | ((deSO_ideal_L1_1.bulk.p_i[7] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[7], has value: -5.37993e-17" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi[2] <= 1.0, has value: -1.11264e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.xi_dryGas[2] <= 1.0, has value: -1.19441e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.x[2] >= 0.0 and deSO_ideal_L1_1.flueGasOutlet.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.x[2] <= 1.0, has value: -1.16456e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.flueGasOutlet.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.flueGasOutlet.p_i[2], has value: -1.18552e-18" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.bulk.xi[2] >= 0.0 and deSO_ideal_L1_1.bulk.xi[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi[2] <= 1.0, has value: -1.11264e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.bulk.xi_dryGas[2] >= 0.0 and deSO_ideal_L1_1.bulk.xi_dryGas[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.xi_dryGas[2] <= 1.0, has value: -1.19441e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.bulk.x[2] >= 0.0 and deSO_ideal_L1_1.bulk.x[2] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= deSO_ideal_L1_1.bulk.x[2] <= 1.0, has value: -1.16456e-23" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((deSO_ideal_L1_1.bulk.p_i[2] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deSO_ideal_L1_1.bulk.p_i[2], has value: -1.18552e-18" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Components/BoundaryConditions/BoundaryGas_pTxi.mo:46:3-46:42:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((idealGasPressureSink1.s_port >= 0.0)) --> "Variable violating min constraint: 0.0 <= idealGasPressureSink1.s_port, has value: -589.924" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((e_Filter_dynamic1.flueGasOutlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.flueGasOutlet.p_i[10], has value: -1.64736e-11" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/Fundamentals/PressureLoss/Generic_PL/PressureLoss_L2.mo:7:3-7:34:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((e_Filter_dynamic.pressureLoss.Delta_p >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic.pressureLoss.Delta_p, has value: -6.13376e-12" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/Fundamentals/PressureLoss/Generic_PL/PressureLoss_L2.mo:7:3-7:34:writable] | | | | The following assertion has been violated at time 10.000000 | | | | ((e_Filter_dynamic1.pressureLoss.Delta_p >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.pressureLoss.Delta_p, has value: -7.6672e-12" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Components/BoundaryConditions/BoundaryGas_Txim_flow.mo:48:3-48:42:writable] | | | | The following assertion has been violated at time 14.000000 | | | | ((idealGasFlowSource_XRG4.s_port >= 0.0)) --> "Variable violating min constraint: 0.0 <= idealGasFlowSource_XRG4.s_port, has value: -26.7462" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Components/BoundaryConditions/BoundaryGas_Txim_flow.mo:48:3-48:42:writable] | | | | The following assertion has been violated at time 24.000000 | | | | ((idealGasFlowSource_XRG.s_port >= 0.0)) --> "Variable violating min constraint: 0.0 <= idealGasFlowSource_XRG.s_port, has value: -29.7172" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 50.000000 | | | | ((e_Filter_dynamic1.bulk.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= e_Filter_dynamic1.bulk.p_i[10], has value: -2.4406e-12" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 680.000000 | | | | ((deNOx.flueGasOutlet.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.flueGasOutlet.p_i[10], has value: -0.0894366" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:44:3-44:56:writable] | | | | The following assertion has been violated at time 680.000000 | | | | ((deNOx.bulk.p_i[10] >= 0.0)) --> "Variable violating min constraint: 0.0 <= deNOx.bulk.p_i[10], has value: -0.0894366" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/ClaRa 1.8.1/Basics/ControlVolumes/Fundamentals/ChemicalReactions/ChemicalReactionsBaseGas.mo:32:3-32:66:writable] | | | | The following assertion has been violated at time 1116.000000 | | | | ((e_Filter_dynamic.chemicalReactions.xi_aux[1] >= 0.0 and e_Filter_dynamic.chemicalReactions.xi_aux[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.chemicalReactions.xi_aux[1] <= 1.0, has value: -3.05661e-19" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 1116.000000 | | | | ((e_Filter_dynamic.flueGasInlet.xi_dryGas[1] >= 0.0 and e_Filter_dynamic.flueGasInlet.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.xi_dryGas[1] <= 1.0, has value: -3.51335e-19" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_pT.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 1116.000000 | | | | ((e_Filter_dynamic.flueGasInlet.x[1] >= 0.0 and e_Filter_dynamic.flueGasInlet.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.flueGasInlet.x[1] <= 1.0, has value: -2.46124e-19" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:25:3-26:39:writable] | | | | The following assertion has been violated at time 1116.000000 | | | | ((e_Filter_dynamic.bulk.xi[1] >= 0.0 and e_Filter_dynamic.bulk.xi[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi[1] <= 1.0, has value: -3.05661e-19" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:27:3-28:20:writable] | | | | The following assertion has been violated at time 1116.000000 | | | | ((e_Filter_dynamic.bulk.xi_dryGas[1] >= 0.0 and e_Filter_dynamic.bulk.xi_dryGas[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.xi_dryGas[1] <= 1.0, has value: -3.51335e-19" assert | info | [/home/hudson/saved_omc/libraries/.openmodelica/libraries/TILMedia 1.8.1-main/BaseClasses/PartialGas_ph.mo:29:3-29:50:writable] | | | | The following assertion has been violated at time 1116.000000 | | | | ((e_Filter_dynamic.bulk.x[1] >= 0.0 and e_Filter_dynamic.bulk.x[1] <= 1.0)) --> "Variable violating min/max constraint: 0.0 <= e_Filter_dynamic.bulk.x[1] <= 1.0, has value: -2.46124e-19" LOG_STATS | info | ### STATISTICS ### | | | | | timer | | | | | | 0.103852s reading init.xml | | | | | | 0.00828503s reading info.xml | | | | | | 0.00328949s [ 0.2%] pre-initialization | | | | | | 0.0384051s [ 2.1%] initialization | | | | | | 0.000229891s [ 0.0%] steps | | | | | | 0.0359973s [ 2.0%] solver (excl. callbacks) | | | | | | 0.0240528s [ 1.3%] creating output-file | | | | | | 0.321625s [ 17.4%] event-handling | | | | | | 0.0187649s [ 1.0%] overhead | | | | | | 1.40363s [ 76.0%] simulation | | | | | | 1.84599s [100.0%] total | | | | | events | | | | | | 13 state events | | | | | | 0 time events | | | | | solver: dassl | | | | | | 1190 steps taken | | | | | | 2003 calls of functionODE | | | | | | 403 evaluations of jacobian | | | | | | 94 error test failures | | | | | | 18 convergence test failures | | | | | | 0.391454s time of jacobian evaluation LOG_SUCCESS | info | The simulation finished successfully.