The hydrogenation of CO and CO2 over Rh/SiO2 have been investigated fo
r the purpose of identifying the similarities and differences between
these two reaction systems. In situ infrared spectroscopy was used to
characterize the surface of the catalyst. Exposure of the catalyst to
CO or CO2 produced very similar infrared spectra in which the principa
l features are those for linearly and bridge-bonded CO. In the case of
CO2 adsorption, a band for weakly adsorbed CO2 could also be observed
. For identical reaction conditions the rate of CO2 hydrogenation to m
ethane is higher than that for CO hydrogenation. The activation energy
for CO hydrogenation is 23.2 kcal/mol and that for CO2 hydrogenation
is 16.6 kcal/mol. The partial pressure dependances on H-2 and COz (z =
1, 2) are 0.67 and -0.80, respectively, for CO hydrogenation, and 0.5
3 and -0.46, respectively, for CO2 hydrogenation. Infrared spectroscop
y reveals that under reaction conditions the catalyst surface is nearl
y saturated by adsorbed CO. The spectra observed during CO and CO2 hyd
rogenation are similar, the principal difference being that the CO cov
erage during CO hydrogenation is somewhat higher than that during CO2
hydrogenation. The CO coverage is insensitive to Hz partial pressure,
but increases slightly with increasing COz partial pressure. Transient
-response experiments demonstrate that the adsorbed CO is a critical i
ntermediate in both reaction systems. It is proposed that the rate det
ermining step in the formation of methane is the dissociation of H2CO,
produced by the stepwise hydrogenation of adsorbed CO. A rate express
ion derived from the proposed mechanism properly describes the experim
entally observed reaction kinetics both under steady-state and transie
nt-response conditions. (C) 1996 Academic Press, Inc.