Cobalt(III)-oxo clusters as catalysts for oxidation
171
attractive. Suitable modification of reaction conditions
as well as experimental set-up is expected to improve
yields and selectivities of products in these catalysed
oxidation processes. The survival of the cubane com-
plexes through the course of the oxidation reactions also
suggests that under appropriate conditions the reuse of
the catalysts may be possible.
Scheme 3. Aerobic oxidation of ethylbenzene catalysed by
Co4O4(O2CMe)4(py) .
4
Typically cobalt-catalysed autoxidation of p-xylene
in the liquid phase is carried out in acetic acid medium
at very high temperature (195–205 C) and pressure
Co(III) initially in a sluggish manner,22 no induction
period is observed in the use of the present Co(III)-
based reaction. Product selectivities are also much bet-
◦
(
∼ 30 bar) in the presence of halide ion promoter
that significantly changes the reaction kinetics of such
processes.
ter with our cubane complexes compared even to the
2,22
Co(III) complexes which are reported23 to be highly
Since the oxidation of Co(II) to Co(III)
is a slow process, use of promoters is necessary in
cobalt(II)-catalysed processes to prevent a possible
induction period during which no desired conversion
takes place. The avoidance of induction period and
polluting promoters, redundancy of solvents and the
usability of water as a solvent in alkyl aromatic oxida-
tion thus make these conversions quite friendly from an
environmental point of view.
active in the oxidation of ethylbenzene to acetophenone
at 150 C. The acetophenone productivity calculated for
◦
the present study is 2310 moles per mole of catalyst,
while the turnover frequency calculated for the first four
−1
hours of the reaction is 212 h . Our results obtained
under homogeneous conditions by making use of the
cobalt(III) cubane clusters also compare well with the
highly active heterogeneous catalyst, also based on a
Co(III)-oxo species.16
Oxidation of renewable feedstock to produce value-
The cubane complexes has also been found to be use- added chemicals constitutes an important area of
24
ful in the autoxidation of p-xylene with air under atmo- research. Transition metal based catalysts for such
25
spheric pressure and in absence of any co-catalysts or transformations are quite important. In the above con-
additives under solvent-free condition (scheme 4). Dur- text, oxidation of α-pinene, which occurs widely in the
ing autoxidation of p-xylene with compressed air for- plant kingdom, may be viewed as an important reaction
mation of solid product starts immediately. Due to the because oxidation products of α-pinene find use as the
build-up of a large quantity of solid product the reaction starting materials for fragrance, flavour and therapeu-
26
needs to be stopped at the end of 7 h. The isolated yields tic agents including taxol. The tetrameric cubane-like
of p-toluic acid and terephthalic acid are found to be complex [Co O (O CC H ) (4-CNpy) ] was examined
4
4
2
6
5
4
4
∼
25% and ∼ 1%. The compound Co O (O CMe) (4- as a catalyst for the homogeneous air oxidation of
4
4
2
4
CNpy) is also active under moderate O pressure in α-pinene under atmospheric pressure (scheme 5) and
4
2
aqueous medium. In this case also, p-toluic acid is the found to favour the preferential formation of the epox-
main product with only traces of terephthalic acid form- ide product.
ing as the other product.12 Our results thus indicate that
This reaction was carried out under homogeneous
the cobalt(III)-oxo clusters may be active as catalysts conditions at an elevated temperature using 1,4-dioxane
13
for p-xylene oxidation in highly polar (water) as well as the solvent. The effect of reaction temperature was
as non-polar (p-xylene) media. Further studies are how- studied by taking 25 mg (0.08 mol%) of the catalyst
◦
◦
ever necessary to make these findings commercially and allowing the reaction to take place at 60 C, 80 C
◦
or 100 C, respectively. By monitoring the progress of
the reaction by GC it was found that an increase in the
reaction temperature accelerates air oxidation of α-
pinene with the highest conversion of 66.8% being
◦
observed at 100 C after 24 h. At all the three temper-
atures air oxidation commenced quickly with a prefer-
ential formation of α-pinene oxide over other oxidation
products.
In order to evaluate the optimum catalyst require-
ment in the air oxidation of α-pinene, the catalyst con-
centration was varied between 0.01 mol% to 0.5 mol%.
Scheme 4. Aerobic oxidation of p-xylene catalysed by
Co4O4(O2CMe)4(py) .
4