Catalysis Today 57 (2000) 231–239
Vanadia/titania catalysts for gas phase partial toluene oxidation
Spectroscopic characterisation and transient kinetics study
D.A. Bulushev, L. Kiwi-Minsker
*
, A. Renken
Institute of Chemical Engineering, Swiss Federal Institute of Technology, CH-1015 Lausanne, Switzerland
Abstract
Formation of vanadia species during the calcination of ball milled mixture of V
2
O
5
with TiO
2
was studied by Raman
spectroscopy in situ and at ambient conditions. It is found that calcination in air leads to fast (1–3 h) spreading of vanadia over
TiO
2
followed by a slower process leading to the formation of a monolayer vanadia. The calcinated catalyst showed higher
activity during toluene oxidation than the uncalcinated one, but the selectivity towards C
7
-oxygenated products (benzaldehyde
and benzoic acid) remains unchanged. The activity of the catalysts is ascribed to the formation of vanadia species in the
monolayer. The details of the parallel–consecutive reaction scheme of toluene oxidation are presented from steady-state and
transient kinetics studies. Different oxygen species seem to participate in the deep and partial oxidation of toluene. Coke
formation was observed during the reaction presenting an average composition C
2n
H
1.1n
. The amount of coke on the catalyst
was not dependent on the calcination step and the vanadium content in the catalyst. Coke formation was seen to be responsible
for the deactivation of the catalyst. ©2000 Elsevier Science B.V. All rights reserved.
Keywords: Raman spectroscopy; Transient response technique; V/Ti oxide catalysts; Toluene partial oxidation
1. Introduction
Vanadia/titania (V/Ti) catalysts are promising
materials for the selective side chain oxidation of
alkyl-aromatics [1,2]. It is known that the perfor-
mance of V/Ti catalysts is sensitive to the nature
and coverage by vanadia species, which depend on
the method of the catalyst preparation. The choice
of the vanadium precursor, the temperature and time
of calcination, conditions of catalyst activation and
surface impurities have also been shown to be impor-
tant for catalyst performance. Due to the industrial
application of V/Ti catalyst in the o-xylene oxidation
to phthalic anhydride many attempts have been made
*
Corresponding author. Tel.: +41-21-693-31-82; fax:+41-21-
693-31-90.
E-mail address: lioubov.kiwi-minsker@epfl.ch (L. Kiwi-Minsker).
to correlate the catalytic performance of these cata-
lysts with their surface properties [2]. However, many
questions concerning the nature of the active sites
remain still open. The nature of the vanadium oxy-
gen bond, the specific role of the terminal (V=O) and
bridging (V–O–V) active sites for selective oxidation
of organic compounds has been discussed intensively
in literature [1–3]. No clear consensus has emerged.
FT-Raman or FT-IR spectroscopy of the catalyst sur-
face coupled with transient technique studies should
provide valuable information about the catalytic cycle
and the active species leading to product formation
[4,5]. This knowledge seems essential for the under-
standing of the reaction mechanism and development
of a more effective catalyst.
Catalytic toluene oxidation on vanadia/titania
catalysts gives benzaldehyde and benzoic acid as the
important products, however CO
x
products are formed
0920-5861/00/$ – see front matter ©2000 Elsevier Science B.V. All rights reserved.
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