Deactivation kinetics of a V/Ti-oxide catalyst was studied in partial oxida
tion of toluene to benzaldehyde (BA) and benzoic acid (BAc) at 523-573 K. T
he catalyst consisted of 0.37 monolayer of VOx species and after oxidative
pre-treatment contained isolated monomeric and polymeric metavanadate-like
vanadia species under dehydrated conditions as was shown by FT Raman spectr
oscopy. Under the reaction conditions via in situ DRIFTS fast formation of
adsorbed carboxylate and benzoate species was observed accompanied by disap
pearance of the band of the monomeric species (2038 cm(-1)) (polymeric spec
ies were not controlled). Slow accumulation of maleic anhydride, coupling p
roducts and/or BAc on the surface caused deactivation of the catalyst durin
g the reaction. Temperature-programmed oxidation (TPO) after the reaction s
howed formation of high amounts of CO, CO2 and water. Rate constants for th
e steps of the toluene oxidation were derived via mathematical modelling of
reaction kinetics at low conversion and constant oxygen/toluene ratio of 2
0:1. The model allows predicting deactivation dynamics, steady-state rates
and selectivity. The highest rate constant was found for the transformation
of BA into BAc explaining a low BA yield in the reaction. (C) 2001 Elsevie
r Science B.V. All rights reserved.