Recent studies have focused on the promotion of methanol
synthesis
by CeO2 and the inhibition of the reverse water gas shift
reaction (r-WGSR) by TiO2 support from the perspective
of the nature of active sites and morphology. Nevertheless, the rational
design of catalysts needs to account additionally for the reaction
mechanism, a topic that has not yet been addressed for CuCeO
x
/TiO2. Herein, methanol and CO formation
pathways over this catalytic system were unraveled. Kinetic, isotopic,
and spectroscopic techniques were combined to obtain mechanistic insights
from both reactions. Particularly, H2/D2 kinetic
isotopic effect (KIE), gas hourly space velocity (GHSV) effect, cofeeding
of products, operando-diffuse reflectance infrared Fourier transform
spectroscopy (operando-DRIFTS) under steady-state, transient, and
H2/D2 exchange conditions, and 12CO2/13CO2 steady-state isotopic-transient
kinetic analysis-DRIFT/mass spectrometry (SSITKA-DRIFTS/MS) were performed.
The results unequivocally ruled out an r-WGSR + CO hydrogenation pathway
for methanol synthesis and, furthermore, demonstrated that this species
is formed through the stepwise hydrogenation of formates over Cu–Ce
interfacial sites. Moreover, it was concluded that the formation of
CO occurs assisted by hydrogen on a site different from that involved
in the methanol synthesis. Likewise, the kinetic relevance of surface-detected
carbonate species was discarded. From these mechanistic insights,
a formal kinetic model was derived, which accurately fitted the experimental
data and correctly predicted the properties of the active sites and
the behavior of CuCeO
x
/TiO2 catalysts with different CeO2 concentrations. This study
highlights the importance of combining kinetic and spectroscopic analyses
with isotopic labeling in order to elucidate reaction mechanisms over
catalysts in which the interface between a metal and metal-oxide plays
a relevant role.