pHEMA-supported Mn(III)salen catalyst for epoxidation of olefin
styrene and 1-octene, the polymer-immobilized Mn(III)salen
catalyst led to a 65% ee value of styrene epoxide and 70%
ee value of 1-octene epoxide – lower than that of the homoge-
neous catalyst. The possible reason is that Mn(III)salen immobi-
lized on to pHEMA supports led to a low selectivity of styrene
epoxide with phenyl aldehyde and acetophenone as
by-products.
Since catalysts had been used to perform reactions, much
effort has been devoted not only to develop superior catalysts
but also to find methods for their reuse or use in continuously
operated reactors. With this aim in mind, the recycling of
pHEMA–Mn(III)salen was investigated with the a-methylstyrene
as an example.
Table 2. Effect of temperature on the epoxidation of indene by
pHEMA–Mn(salen)
a
ꢀ
b
Entry
Temperature ( C)
ee (%)
Yield (%)
Time (h)
1
2
3
4
5
À9
À5
0
95
93
93
87
82
67
81
94
95
98
7
6
5.5
5
15
25
4.5
a
Reaction conditions: indene (2 mmol), catalyst (0.2 mmol, 10 mol%),
NH OAc (0.4 mmol, 20 mol%), NaClO (5.8 mmol).
Monitored by thin-layer chromatography every other half hour.
4
b
Blank experiments with Na@pHEMA as catalyst showed
no significant turnover frequencies. After the first run,
pHEMA–Mn(III)salen was filtered and directly added to a
second run, leading to 51% ee conversion (65% epoxide
yield). With isolation of the catalyst after the second run
followed by washing with dichloromethane, a subsequent
run led to 92% ee value (88% epoxide yield). This regenera-
tion process could be repeated four times, and the values
of ee were nearly constant (decreasing only 2% between the
first and the fourth times). After the eighth run, the ee value
still remained at 80% (75% epoxide yield). This proved
the stability of the catalysts under our experimental condi-
tions. Thus the reuse of catalyst was possible after isolating
and washing the catalyst. This washing step was presumably
effective in removing the inorganic waste from the catalyst,
which began to block access to the active site. Even though
the yield increasing from 82% to 94%, and ee values increased
from 68% to 93% (entries 3 and 4). The increases in activity
and ee values might be due to the presence of the partial
interaction between Mn(III)salen and NH OAc. Meanwhile, the
4
ee value of 93% corresponded to the ee value of 94% for
the homogeneous case. Here, the axial immobilization of Mn
(III)salen compounds contributed to the coordination of
NH OAc, leading to corresponding ee values with a homoge-
4
neous result.
To the best of our knowledge, the heterogeneous
pHEMA–Mn(III)salen catalyst showed more activity than the
corresponding homogeneous catalyst in the epoxidation of
olefins. Despite the limitations of heterogeneous catalytic
systems, such as slow reactant diffusion to the catalytic site,
pHEMA probably acted as a mediator of the reaction between
the substrate (organic phase) and the oxidant dissolved in the
aqueous phase. The substrate and the oxidant were brought
together by the pHEMA–Mn(III)salen system, which promoted
the diffusion of these compounds to the catalytic site where
the reaction took place.
the recycled heterogeneous catalyst showed
a slightly
decreasing activity, the selectivity of epoxide was not
changed during the reuse process. The data showed that
the supported catalysts exhibited excellent catalytic activity
and enantioselectivity and could be reused several times
without significant loss of its catalytic activity.
Effect of Reaction Temperature
Conclusions
The results of the enantioselective epoxidation of indene
catalyzed by the pHEMA–Mn(III)salen complex at different
reaction temperatures are summarized in Table 2. As
expected, the catalytic activity and enantioselectivity were
relevant to the reaction temperatures. A decrease of reaction
Chiral Mn(III)salen compound was axially immobilized on
to pHEMA via a hydroxy group, which efficiently catalyzed
asymmetric epoxidation of olefins with NaClO as oxidant in
the biphasic system. Compared to the homogeneous catalyst,
the heterogeneous Mn(III)salen catalysts also exhibited high
activity and enantioselectivity for the disubstituted cyclic
indene and 6-cyano-2,2-dimethylchromene. Moreover, the
polymer-immobilized Mn(III)salen catalysts can be easily
recycled by simple filtration. These heterogeneous catalysts,
which were recycled at least five times for the asymmetric
ꢀ
temperature from 25 to À9 C led to a decrease of epoxide
yield from 98% to 67%. However, an increase of enantioselec-
tivity with the best ee value of 95% was observed, which was
[
17]
similar to the results reported in Yao et al.
The reason
might be an increase in enantiofacial selectivity in the initial
C-O bond-forming step and suppression of the trans path-
way in the second step at low temperature. After consider-
ꢀ
ing two aspects of the yield and ee value, 0 C was selected
Table 3. Effect of co-catalyst NH OAc on epoxidation of indene by
4
a
pHEMA–Mn(III)salen
in this work.
b
Entry
Catalyst
Mn(III)salen
pHEMA–Mn(III)salen
NH
4
OAc ee (%) Yield (%) Time (h)
Effect of Co-catalyst NH OAc
4
1
2
3
4
P
94
75
93
82
92
82
94
68
4.5
4.5
5.5
5.5
The pHEMA–Mn(III)salen catalyst was active and enantioselec-
tive for the asymmetric epoxidation of indene. In Table 3, the
indene was quantitatively converted into its epoxide with
A
P
A
7
5% ee (without NH OAc) and 93% ee (with NH OAc) catalyzed
4 4
a
Reaction conditions: indene (2 mmol), catalyst (0.2 mmol, 10 mol%),
NaClO (5.8 mmol). The reaction temperature was 0 C.
by homogeneous Mn(III)salen Cl catalyst (entries 1 and 2). In
the absence of NH OAc, the heterogeneous pHEMA–Mn(III)
salen catalyst gave 68% yield. The addition of NH OAc led to
ꢀ
4
b
4
P, NH OAc present (0.4 mmol, 20 mol%); A, absent.
4
Appl. Organometal. Chem. 2012, 26, 114–120
Copyright © 2012 John Wiley & Sons, Ltd.
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