Abiraj et al.
519
Table 2. Recycling of polymer-supported
formate for the reduction of azobenzene.
pounds to obtain the corresponding amines in pure form
with no work-up.
Cycle
Time (h)
Yield (%)
1
2
3
4
5
6
7
8
2.0
2.0
3.0
3.5
3.5
4.0
4.0
4.0
98
97
97
97
97
95
93
92
Experimental
Preparation of polymer-supported formate
The aminomethyl polystyrene (Advanced Chemtech, 1%
DVB cross-linked, 100–200 mesh, 2 mmol/g) was washed
with an excess of a 50% solution of formic acid in dichloro-
methane. The resulting polymer was washed thoroughly and
successively with dichloromethane and ether, and dried un-
der vacuum. The obtained resin was used as such for the re-
duction.
the separation of products from the reaction mixture is sim-
ple and involves, in most of the cases, direct removal of the
catalyst and resin by filtration and evaporation of the solvent
under vacuum. The crude product, so isolated, was of excel-
lent purity for most purposes. Hence, this procedure is highly
advantageous to obtain water-soluble aromatic amines in
high yields (Table 1, entries 2, 8, 11–13). Further, it is note-
worthy here that the polymer-supported formate was regen-
erated and could be reused for further hydrogenolysis
process. In total, 10 successive recycle runs were possible
before there was an appreciable decrease in the reaction
yield (Table 2).
To obtain optimum reduction conditions, a number of
trails with a range of solvents, which are commonly em-
ployed for CTH reactions, were carried out. Methanol is
found to be the best one as far as the solubility of substrate
and rate of reaction is concerned. To examine the effects of
catalyst loading, the reduction was attempted using different
ratios of catalyst and substrate. We observed the optimal ra-
tio of catalyst to substrate to be 1:4 by weight (approxi-
mately 0.05 mmol catalyst for 1 mmol of substrate). However,
the rate of reduction was significantly slower when smaller
amounts of catalyst were used. During the recycle runs, an-
other 0.025 mmol of catalyst was added after the fifth cycle
to increase the rate of reduction.
Determination of polymer-supported formate loading
The polymer-supported formate (1 g) was placed in a
manually operated solid phase vessel and washed thoroughly
with dil. HCl (0.05 N). The HCl washing containing formic
acid (released from the resin) was collected and diluted to
50 mL in a volumetric flask. An aliquot (10 mL) of this
solution was titrated potentiometrically against a standard
NaOH solution. The formate loading was calculated to be
1.92 mmol/g.
General procedure for the reduction of azo compounds
To a solution of the azo compound (1 mmol) in methanol
(15 mL) taken in a horizontal solid phase vessel, polymer-
supported formate (1 g) and 10% Pd-C (50 mg, 0.05 mmol)
were added. The suspension was shaken well2 for the speci-
fied time at room temperature (Table 1). After consumption
of the starting material, as monitored by TLC, the reaction
mixture was filtered and washed thoroughly with methanol.
The combined washings and filtrate were evaporated under
reduced pressure. The crude product was found to be analyt-
ically pure in most cases. Where necessary, the crude prod-
uct was taken into the organic layer and washed with
saturated sodium chloride. For recycling purposes, the resi-
due containing the polymer-supported formate and the cata-
lyst was washed thoroughly and successively with DMF,
dichloromethane, a 50% solution of formic acid in dichloro-
methane, dichloromethane, and ether. The activated resin
along with the catalyst were dried under vacuum and used as
obtained for further reduction reactions.
The reductive cleavage of azo compounds proceeds smoothly
despite the dual heterogeneity of catalyst and polymer sup-
port. The initial step in the reduction would be the formation
of palladium diformate by the reaction of palladium with the
formate released from the polymeric support (10a, 10b). The
palladium formate can then transfer two hydrogen atoms to
the azo compound. In addition to this essential feature, the
In the case of the reduction of unsymmetrically substi-
tuted azo compounds, the crude product was subjected either
to preparative TLC or to column chromatography to separate
two different constituent amines.
+
polymer-supported NH3 may also provide H+ to complete
the reduction process (10c).
In conclusion, a highly facile polymer-supported formate –
10% Pd-C system was developed for the smooth reduction
of azo compounds to the corresponding amine(s). The use of
polymer-supported formate combines the advantages of
polymer-supported chemistry with the flexibility of the CTH
technique. The advantages include a safe reaction medium,
high selectivity, rapidity, ease of operation, and simple re-
covery of the hydrogen donor. In addition, this approach is
highly helpful for the reduction of symmetric azo com-
Acknowledgements
We gratefully acknowledge financial support from the
University Grants Commission, New Delhi. We also ac-
knowledge the Council of Scientific and Industrial Research,
New Delhi for a research fellowship (to KA).
2 The reaction mixture was subjected to shaking using a manual shaker as the shaking of the polymer-supported formate instead of stirring in-
creases its life for recycling purposes.
© 2005 NRC Canada