In order to reveal the role of alkali in the carbon-free CO2 reforming of m
ethane, the kinetics of the individual steps involved in the reforming were
examined on Ni/Al2O3 catalysts with 0, 1, 5, and 10 wt% K. Although the ad
sorption of CO2 was enhanced by the presence of potassium, the dissociation
of CO2 to CO and O-ads was not significantly influenced. This suggests tha
t the enhancement of the oxidation of CHX,ads by increasing the concentrati
on of O-ads is not the cause for the carbon-free CO2 reforming. The carbon-
free reforming was mainly ascribed to the ensemble control; i.e., potassium
plays a role in dividing the nickel surface into the smaller ensembles and
, thereby, the carbon deposition is suppressed. On the other hand, the rate
-determining step, ascribed to the dissociation of CHXOads to CO and x/2H(2
), was not affected by potassium below the threshold coverage of Theta (K)
= ca. 0.4, but above it, the rate became slow. The number of surface nickel
atoms (nickel ensemble) required for the reforming was estimated from a si
mple Langmuir form, r = r(0)(1 - Theta (K))(n), to be ca. 2.9. The number w
as similar to that obtained on sulfur-passivated Ni catalysts in H2O reform
ing of methane, suggesting that the retardation of the rate-determining ste
p at Theta (K) > 0.4 is ascribed to the physical blockage of the nickel ens
emble by potassium. (C) 2001 Academic Press.