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functional groups derived from the sulphur and oxygen
groups could be responsible for the low ee. Also in the case
of SWNT, the presence of a residual population of free
carboxylic groups is the most likely factor responsible for
the moderate ee value. Some additional treatments to the
SWNT or activated carbons to decrease the population of
sites playing a negative role would be necessary to test this
hypothesis. It is interesting to note that the TOF for
the reaction of benzaldehyde in the presence of both
VOsalenfSWNT and VOsalenfAC is also high with
3. Conclusions
In the present work, we have developed a library of chiral
vanadyl salen complexes that are covalently attached to
solid supports or with a high ionophilicity that makes the
catalyst soluble in ionic liquids and not extractable by
conventional organic solvents. The preparation of this
library illustrates a simple methodology to obtain hetero-
geneous catalysts based on the addition of mercapto groups to
terminal C]C double bonds. From this series, we have
prepared a chiral vanadyl salen complex anchored to silica
t
comparable values to those observed for the tetra BuVO-
(
activity and asymmetric induction ability is very similar to
VOsalenfsilica) through a 14 membered chain whose
salen complex in homogeneous phase and higher than
observed for catalyst anchored to silica and, therefore, it
may be worth while to try to optimise the asymmetric
induction of these two catalysts.
t
that of chiral tetra BuVOsalen complex in ionic liquid. The
activity of the latter complex in solution can be considered
as the maximum intrinsic activity achievable for the vanadyl
salen complexes and, therefore, VOsalenfsilica is con-
sidered as an optimum recoverable catalyst since it exhibits
the activity of the homogeneous complex plus the
advantages of heterogeneous catalysts in terms of recovery
and reusability. No vanadium leaching has been observed
for this system.
One of the most important issues when studying a
heterogeneous catalyst is its performance upon reuse. In
t
the case of homogeneous phase tetra BuVOsalen
complex in [beim]PF ionic liquid, upon extraction of
6
the product with hexane, the extracted solution becomes
green indicating that some fraction of the vanadyl
catalyst present in the ionic liquid was also extracted
together with the reaction products. Although, a second
t
4. Experimental
use of the ionic liquid containing chiral tetra BuVO-
salen complex gave essentially the same conversion and
ee values as in the first use, it is clear that over the long
term a depletion of the vanadyl salen chiral complex
would eventually lead to a reduction of this activity.
Also, separation of the vanadium traces from the
reaction mixture would be problematic. In the case of
the VOsalenfsilica as catalyst, reuse of the solid after
one run was simply achieved by filtration of the solid
and subsequent washings with fresh aliquots of chloro-
form. Upon removal of the solid catalyst VOsalenfsilica,
the reaction mixture was surveyed for the presence of
catalytic active species. In no case was it observed that
the reaction progresses in a solution that has been
reacted up to 40% conversion in the presence of
VOsalenfsilica when the solid has subsequently been
removed and the supernatant allowed to react further
under normal conditions.
Silica (Aldrich), SWNT (Carbolex, HiPCO, O80% purity),
activated carbon (Norit), and [bmim]PF (Aldrich) were
commercial samples.
6
t
Chiral tetra BuVOsalen complex was prepared by dissol-
0
t
ving in methanol tetra tert-butyl ligand 4 (RZR Z Bu)
1 mmol) and VOacac (1.1 mmol) and stirring the solution
(
overnight at room temperature. The complex was purified
by a short chromatographic column using silica as stationary
phase and eluting initially with hexane to remove the ligand
followed by diethyl ether. Tetra tert-butyl salen ligand (4,
0
t
RZR Z Bu) was prepared by condensation at room
temperature of 2 equiv of 3,5-di-tert-butylsalicylaldehyde
0
and following the reported procedure.
and 1 equiv of (C)-R,R -1,2-cyclohexanediamine in ethanol
16
Precursor 5 was obtained as a mixture starting from 3-tert-
butyl-5-chloromethylsalicylaldehyde, 3,5-di-tert-butylsali-
Based on the results achieved with benzaldehyde, we
t
selected two systems, namely chiral tetra BuVOsalen
0
cylaldehyde and (C)-R,R -1,2-cyclohexanediamine in
ethanol in the proportions indicated in Scheme 1, and
adding vanadyl sulphate before reacting the complex with
undecen-1-ol in xylene at reflux temperature, following the
complex in [beim]PF and VOsalenfsilica in CHCl as
6
3
the systems with the highest asymmetric induction ability
and studied the transformation of two more aldehydes into
the corresponding chiral silylated cyanohydrins in order to
expand the scope of the heterogeneous catalysts and to show
the generality of our system. The results achieved are listed
in Table 3.
9
detailed experimental procedure previously reported by us.
Functionalised silica containing 3-mercaptopropylsilyl
groups was obtained by reacting silica (ALDRICH) with
3
-mercaptopropyl trimethoxysilane in toluene at reflux
temperature under an inert atmosphere, and subsequently
submitting the resulting solid to exhaustive silylation using
excess of ethoxytrimethylsilane under the same conditions
as for 3-mercaptopropylsilylation. The anchoring of pre-
cursor 5 to the functionalised silica was accomplished using
AIBN as radical initiator in the absence of oxygen following
As can be seen in Table 3, although as in the case of
benzaldehyde the activity and TOF for the cyanosilylation
of a substituted benzaldehyde (4-methoxybenzaldehyde)
and an aliphatic aldehyde (hexanal) using VOsalenfsilica
as solid catalyst is somewhat lower than that of the chiral
t
tetra BuVOsalen complex in [beim]PF , the ee values of
9
6
a procedure described elsewhere.
both catalytic systems were very similar with the additional
advantage that the solid catalyst can be easily separated and
reused.
Precursor 8 was synthesized starting from 5-bromo-3-
methylsalicylaldehyde that was submitted to Suzuki