ISSN 0023ꢀ1584, Kinetics and Catalysis, 2011, Vol. 52, No. 4, pp. 493–498. © Pleiades Publishing, Ltd., 2011.
Original Russian Text © A.G. Galstyan, S.G. Galstyan, V.V. Lysak, 2011, published in Kinetika i Kataliz, 2011, Vol. 52, No. 4, pp. 504–509.
Kinetics and Products of the Reactions of Ozone with Toluene
and Its Derivatives in Acetic Anhydride
A. G. Galstyan, S. G. Galstyan, and V. V. Lysak
Institute of Chemical Technologies, EastꢀUkrainian National University, Rubezhnoe Branch,
Rubezhnoe, Lugansk oblast, Ukraine
eꢀmail: ozon@megabit.com.ua
Received December 14, 2009
Abstract—The reactions of ozone with toluene and its derivatives in acetic anhydride were studied. It was
found that competing parallel reactions of ozone with the aromatic ring and substituents occurred in the
ozone–arene–acetic anhydride system. The ratio between these reaction paths depended on the arene strucꢀ
ture and reaction conditions. The selectivity of the oxidation of toluene and its derivatives at the methyl group
varied from 0 to 40%. The fraction of aromatic products decreased as the number of methyl groups at the ring
was increased. Triꢀ and tetramethylbenzenes were oxidized only at the aromatic ring. The stability of an aroꢀ
matic system increased upon the introduction of electronꢀacceptor substituents into the benzene ring. Amiꢀ
notoluenes and hydroxytoluenes were oxidized with ozone mainly at the NH2 and HO groups; however, as in
the case of toluene, the aromatic ring and methyl group became the main directions upon their acylation. The
oxidation of the methyl group in acetic anhydride in the presence of sulfuric acid was finished at the step of
the formation of the acylated derivatives of benzyl alcohols and benzaldehydes, which are resistant to the
action of ozone.
DOI: 10.1134/S0023158411040033
INTRODUCTION
displacement along the horizontal axis. Acetic anhyꢀ
dride (chemically pure) was used as a solvent without
preliminary purification. Liquid methylbenzenes
(chemically pure) were purified on a column with aluꢀ
minum oxide. Solid methylbenzenes were recrystalꢀ
lized from appropriate solvents before use. Sulfuric
acid (chemically pure) was used as a mineral acid.
The ozone–air mixture with an ozone concentration
of 10–6–10–4 mol/l was obtained using a laboratory
ozone generator [4].
It is well known [1] that, in the ozone–methylbenꢀ
zene–acetic acid system, oxidation develops mainly at
the aromatic ring with the formation of ozonides. The
products of oxidation at the methyl group—benzoic
acids—are formed to a lesser extent (0–40%). Under
these conditions, the reaction of methyl group oxidaꢀ
tion cannot be stopped at the step of the formation of
aromatic alcohols because they are prone to further
oxidation [2]. However, previous studies [3] demonꢀ
strated the possibility of controlling the degrees of oxiꢀ
dation of toluene and its derivatives with ozone by
adding stop reagents to the system.
Acetic anhydride and sulfuric acid were loaded into
a thermostatically controlled reactor, and the resulting
mixture was saturated with ozone on shaking; thereafꢀ
ter, methylbenzene was introduced into the apparatus
(see Table 2 for concentration). The course of the
reaction was monitored based on changes in the conꢀ
centration of ozone in a gas phase and the analysis of
reaction products. Ozone concentrations in the gas
phase at the apparatus inlet and outlet were measured
automatically with the use of a spectrophotometric
technique in the absorption region of 254–290 nm. An
SFꢀ26 spectrophotometer equipped with a flow cell
7 cm in length coupled to an EPN potentiometer was
used for the measurements. The sensitivity to ozone
Here, we report the results of a study of the reacꢀ
tions of ozone with toluene and its derivatives in acetic
anhydride, which is a strong acylating agent. From sciꢀ
entific and practical points of view, this study is imporꢀ
tant for the development of promising methods for
controlling the selectivity and degree of oxidation of
alkylbenzenes with ozone in a liquid phase.
EXPERIMENTAL
The oxidation of toluene and its derivatives was was 1.8
performed in a thermostatically controlled catalytic calculated using a calibration curve constructed with
reactor as a longꢀnecked flask 0.1 l in volume under the use of the equation [O3]g = , where [O3]g is the
conditions of the kinetic regime of oxidation, which ozone concentration in a gas phase, mol/l; is the
was observed at a reactor shaking frequency higher absorbance of ozoneꢀcontaining gas; is the molar
than 7–9 s–1 (depending on the nature of the arene absorption coefficient (
= 3025 at = 254 nm [5]);
is the optical path length of the cell (2–7 cm).
×
10–7 mol/l. The concentration of ozone was
A/ l
ε
A
ε
ε
λ
and reaction conditions) and a 0.04ꢀm amplitude of its and
493
l