Flow reactor studies of methyl radical oxidation reactions in methane-perturbed moist carbon monoxide oxidation at high pressure with model sensitivity analysis
Jj. Scire et al., Flow reactor studies of methyl radical oxidation reactions in methane-perturbed moist carbon monoxide oxidation at high pressure with model sensitivity analysis, INT J CH K, 33(2), 2001, pp. 75-100
New rate constant determinations for the reactions
CH3 + HO2 --> CH3O + OH (1)
CH3 + HO2 --> CH4 + O-2 (2)
CH3 + O-2 --> CH2O + OH (3)
were made at 1000 K by fitting species profiles from high-pressure flow rea
ctor experiments on moist CO oxidation perturbed with methane. These reacti
ons are important steps in the intermediate-temperature burnout of hydrocar
bon pollutants, especially at super-atmospheric pressure. The experiments u
sed in the fit were selected to minimize the uncertainty in the determinati
ons. These uncertainties were estimated using model sensitivity coefficient
s, derived for time-shifted flow reactor experiments, along with literature
uncertainties for the unfitted rate constants. The experimental optimizati
on procedure significantly reduced the uncertainties in each of these rate
constants over the current literature values. The new rate constants and th
eir uncertainties were determined to be, at 1000 K:
k(1) = 1.48(10)(13) cm(3) mol(-1) s(-1) (UF=2.24)
k(2) = 3.16(10)(12) cm(3) mol(-1) s(-1) (UF= 2.89)
k(3) =2.36(10)(8) cm3 mol(-1) s(-1) (UF = 4.23)
There are no direct and few indirect measurements of reactions (1) and (2)
in the literature. There are few measurements of reaction (3) near 1000 K.
These results therefore represent an important refinement to radical oxidat
ion chemistry of significance to methane and higher alkane oxidation.
The model sensitivity analysis used in the experimental design was also use
d to characterize the mechanistic dependence of the new rate constant value
s. Linear sensitivities of the fitted rate constants to the unfitted rate c
onstants were given. The sensitivity analysis was used to show that the det
erminations above are primarily dependent on the rate constants chosen for
the reactions CH3 + CH3 + M --> C2H6 + M and CH2O + HO2 --> HCO + H2O2. Unc
ertainties in the rate constants of these two reactions are the primary con
tributors to the uncertainty factors given above. Further reductions in the
uncertainties of these kinetics would lead to significant reductions in th
e uncertainties in our determinations of k(1), k(2), and k(3). (C) 2001 Joh
n Wiley & Sons, Inc.