The oxidation kinetics of methanol and hydrogen in a supercritical wat
er medium were investigated. Numerical analyses were performed using a
n isobaric, plug-flow reactor model coupled with the Chemkin Real-Gas
software package to handle real-gas thermodynamic effects and elementa
ry kinetics. In the present work, select unimolecular reactions that i
nvolve thermal decomposition have been corrected for the high-pressure
conditions found in supercritical reactors. Predictions of fuel destr
uction rates obtained using an elementary reaction mechanism for hydro
gen oxidation under isobaric, isothermal supercritical conditions (P >
22.1 MPa, and T > 374 C) were verified by comparison with previous ex
perimental results obtained in a laboratory-scale supercritical water
reactor. The H-2-O-2 model is a subset of a proposed elementary reacti
on mechanism for methanol oxidation which was also verified by compari
ng the present model predictions of the kinetic rate calculations with
previous measurements. The mechanism was validated over a temperature
range of 726 to 873 K, a fuel concentration range of 0.001 to 0.004 m
ole/L, and at a pressure of 246 bar. To facilitate future computationa
l fluid dynamic (CFD) modeling efforts in SCWO, a two-step reduced rea
ction mechanism was constructed to simulate the oxidation process of m
ethanol in supercritical water and H2O. The reduced model reflects the
sequential oxidation of methanol into carbon monoxide, and eventually
into final products consisting primarily of carbon dioxide and H2O. T
he calculations of the two-step reduced mechanism matched the elementa
ry reaction model well with respect to major species concentration pro
files.