This work studies
the effect of zirconia structure on the performance
of Pd/ZrO2 catalysts for hydrodeoxygenation of phenol at
300 °C and 1 atm using a fixed bed reactor. Benzene was the major
product over Pd/t-ZrO2, while significant formation of
cyclohexanone was observed over Pd/m-ZrO2. On the other
hand, Pd/m,t-ZrO2 exhibited intermediary behavior. DRIFTS
of adsorbed pyridine, NH3-TPD, and the dehydration of the
cyclohexanol reaction revealed that the Pd/t-ZrO2 catalyst
exhibits a higher density of oxophilic sites than Pd/m-ZrO2 and Pd/m,t-ZrO2. This promoted the formation of deoxygenated
products. However, a mechanism involving dehydration of cyclohexanol
to cyclohexene, followed by dehydrogenation to benzene, may not be
ruled out. Pd/ZrO2 catalysts significantly deactivated
as a function of time on stream. Results of dehydrogenation of cyclohexane
and dehydration of cyclohexanol indicate that the Pd particle size
increased and the density of oxophilic sites decreased during the
hydrodeoxygenation of the phenol reaction. In addition, the DRIFTS
spectra under reaction conditions demonstrated that the coverage of
oxophilic sites by phenoxy and intermediate species increased during
the reaction. The growth of Pd particles is likely responsible for
the losses in the metal–support interface that gradually inhibits
the ability of the adsorbed species to turnover at the metal–support
boundary.