Four alternative ways to describe methane oxidation that all can be used in
computational fluid dynamics (CFD) have been investigated. The purpose has
been to investigate how advanced a description of the methane oxidation is
needed for an accurate description of the main components in practical CFD
calculations. Especially the prediction of the intermediate combustion pro
ducts CO and H-2 has been stressed, The four alternative approaches are: I)
thermodynamic equilibrium, II) a three-step simplified mechanism including
infinitely fast in;eversible global reaction steps for the oxidation of me
thane and hydrogen, and a global, kinetically controlled, reaction step for
carbon monoxide oxidation, III) a four-step simplified mechanism including
two global reaction steps for the break-down of the hydrocarbon, a global
reaction step for the oxidation of hydrogen and a global reaction step desc
ribing the reversible water-shift reaction and IV) a comprehensive reaction
mechanism including 32 chemical species and 156 reversible elementary reac
tions. The comparison has been made by studying the concentration predictio
ns for perfectly stirred reactor (PSR) conditions as a function of nominal
residence time and by a CFD study of a diffusion flame. The results from th
e PSR computations indicate that the three-step simplified mechanism is a g
ood alternative for the fuel lean conditions and for flames far from extinc
tion. The four-step simplified mechanism was found to be a good compromise
between accuracy and computational speed. The four-step simplified mechanis
m also performed well at moderately fuel rich conditions. However, in the C
FD study of the diffusion flame, the difference in the results obtained wit
h the four-step simplified formulation and the comprehensive mechanism was
surprisingly large. The assumption of instantaneous local thermodynamic equ
ilibrium in the reacting fraction of the fluid proved to be an unsuccessful
alternative in the CFD modeling.