CO CHEMISORPTION AND HYDROGENATION OF SURFACE CARBON SPECIES FORMED AFTER CO HE REACTION ON RH/MGO - A TRANSIENT KINETIC-STUDY USING FTIR AND MASS-SPECTROSCOPY/
Am. Efstathiou et al., CO CHEMISORPTION AND HYDROGENATION OF SURFACE CARBON SPECIES FORMED AFTER CO HE REACTION ON RH/MGO - A TRANSIENT KINETIC-STUDY USING FTIR AND MASS-SPECTROSCOPY/, Journal of catalysis, 147(1), 1994, pp. 24-37
The chemisorption of CO and hydrogenation of surface adsorbed carbon s
pecies formed after reaction of CO/He with Rh/MgO catalyst in the rang
e 300-573 K were studied by transient methods employing both FTIR and
mass spectroscopy in separate flow and reactor systems. Exposure of Rh
/MgO to CO/He at 523 K results in a rapid formation of linear and brid
ged CO species. It was found that formation of gem-dicarbonyl CO speci
es during CO chemisorption at 300 K is strongly affected by CO/He trea
tment at 523 K and H-2 reduction conditions. Experiments with labelled
CO ((CO)-C-13 and (CO)-O-18) indicate that linear and bridged CO spec
ies readily exchange with gaseous CO species. Transient hydrogenation
results for adsorbed carbon-containing species formed after CO/He reac
tion at 523 K provide evidence that H-2 chemisorption decreases after
cycles of reaction in CO/He at 523 K followed by H2 reduction at 673 K
. However, the surface coverages of adsorbed CO species are not affect
ed by such treatments. Oxygen pretreatment of the catalyst at 623 K fo
llowed by H-2 reduction, after CO/He reaction at 523 K, greatly affect
s the transient kinetics of hydrogenation of adsorbed CO species at 52
3 K but not their respective surface coverages. This result is related
to a change in the hydrogen chemisorption sites by oxygen treatment w
hich resulted in the removal of inactive carbon not hydrogenated at 72
3 K. A kinetic model for the hydrogenation of the various adsorbed car
bon-containing species is proposed which accounts for the interpretati
on of the CH4 transient responses obtained. (C) 1994 Academic Press, I
nc.