Oxidation of aldehydes to acids
837
TBHP in the absence of any solvent (table 1). No
product other than benzoic acid was observed. The
MnO−4 1-exchanged hydrotalcites were characterized for
their XRD phases, d(001) spacing and pH of water
slurry (table 2). The characterization of the hydrotalcite
catalysts before their MnO−4 1-exchange was reported in
talcites. Because of the immobilization of the
active catalyst component, the separation/removal
of the catalyst from the reaction mixture is easy,
simply by filtration. Moreover, the catalyst can
be reused in the reaction several times without a
significant loss in its activity.
our earlier studies.11–14 From these results, the follow- (iv) The MnO−4 1-exchanged Mg–Al–HT (Mg/Al = 10)
ing important observations are made.
also showed good oxidation activity when molec-
ular oxygen is used as the oxidizing agent (entry
no.19). However, in this case, the reaction was
found to be relatively quite slow.
(i) The hydrotalcites without MnO−4 1-exchange
showed very poor catalytic activity in the oxida-
tion. However, after the MnO−4 1-exchange, their
activity was drastically increased (from 11–23% to
81–99.9% conversion).
The XRD analysis of all the catalysts (entry nos. 1–
16 in table 1) showed the presence of pure hydrotal-
cite phase in all the catalysts except for the MnO−4 1-
exchanged Cu–Al–HT (which was found to contain
hydrotalcite phase along with copper hydroxide and
aluminum hydroxide phases).
The surface area of the catalyst before use was
26 m2/g. After the use in the oxidation (entry no.18),
the surface area of the catalyst remained almost the
same. Also the concentration of Mn in the catalyst
(0.40 mmol/g) was not changed. Moreover, the XRD
spectra for the MnO−4 1-exchanged Mg–Al–HT (before
and after its 5th reuse in the benzaldehyde oxidation
reaction) were found to be almost similar. These facts
revealed that, after its 5th use in the oxidation, the cata-
lyst retained its hydrotalcite structure and also had high
stability during the oxidation.
(ii) The Mg–Al–HT (Mg/Al = 10) showed a little
or no activity in the oxidation (the benzaldehyde
conversion is almost the same as that observed
in the absence of any catalyst). However, after
the MnO−4 1-exchange, it showed highest activity
(99.9% conversion) in the oxidation. The catalyst
also showed excellent reusability in the reaction;
after its fifth reuse, it showed no significant loss in
its activity (entry no. 18). Other MnO−4 1-exchanged
hydrotalcites with Ni/Al, Co/Al and Mg/Fe = 10
(entry nos. 2, 6 and 9) also showed good activity
(92.7, 95.5 and 99.0%, respectively). It is interest-
ing to note that all these MnO−4 1-exchanged hydro-
talcites showed better activity when their diva-
lent/trivalent metal ratio was higher. This may be
attributed to their higher basicity.11–14
Since the MnO−4 1-exchanged Mg–Al–HT (Mg/Al =
10) showed the best performance in the benzaldehyde
to benzoic acid oxidation, further work on the oxida-
tion of other aromatic and aliphatic aldehydes by TBHP
to their corresponding acids (scheme 1) in the absence
of any solvent was carried out using this catalyst. The
results are presented in table 3. In this case, the prod-
uct was isolated from the reaction mixture and purified
using column chromatography. The results in table 3
reveal that the catalyst shows high activity even in the
(iii) When KMnO4 [equivalent to the MnO−4 1 ions
present in the MnO−4 1-exchanged Mg–Al–HT
(Mg/Al = 10)] was used as a homogeneous cat-
alyst in the reaction, the conversion under the
similar reaction conditions was 50.5%; which is
much lower than that obtained using the differ-
ent MnO−4 1-exchanged hydrotalcites. This reveals
that the catalytic activity of MnO−4 1 ions increases
appreciably after their immobilization in the hydro-
Table 2. Characterization of different MnO−4 1-exchanged hydrotalcite catalysts.
XRD
phases
d(001)
spacing (nm)
pH of water
slurry
Catalyst
MnO−4 1(1.55 mmol/g)/ Ni-Al HT (Ni/Al = 3)
MnO−4 1(0.94 mmol/g)/ Ni-Al HT (Ni/Al = 10)
MnO−4 1(0.23 mmol/g)/ Co-Al HT (Co/Al = 3)
MnO−4 1(0.14 mmol/g)/ Co-Al HT (Co/Al = 10)
MnO−4 1(0.77 mmol/g)/ Mg-Fe HT (Mg/Fe = 3)
MnO−4 1(0.71 mmol/g)/ Mg-Fe HT (Mg/Fe = 10)
MnO−4 1(0.80 mmol/g)/ Mg-Al HT (Mg/Al = 3)
MnO−4 1(0.40 mmol/g)/ Mg-Al HT (Mg/Al = 10)
Pure HT
Pure HT
Pure HT
Pure HT
Pure HT
Pure HT
Pure HT
Pure HT
0.780
0.784
0.752
0.756
0.764
0.769
0.765
0.767
8.0
8.0
7.8
7.8
9.6
9.6
9.7
10.5