Fig. 2 Depiction of the catalytically active centre attached to a soluble silsesquioxane moiety and bound in a constrained manner inside mesoporous
silica.
ide.9 The spectrum showed two broad peaks centred at d 135
and 75 which may be attributed to the phenyl and cyclopenta-
dienyl rings, respectively. There is a peak at d 12 which may be
assigned to the methyl group bound to the chiral carbon and the
carbon bound to the silicon. The central carbon in the propyl
tether may be assigned to the peak at d 22, whilst the final
carbon of the tether, that bound to the nitrogen, can be attributed
to the peak at d 52. The final peaks in the spectrum are at d 41
and 58 and may be assigned to the methyl group of the amine
and the chiral carbon, respectively. The 31P MAS NMR
spectrum revealed a broad, split signal centred around d 30,
which is comparable to that observed with the ferrocenyl
precursor 2.
The ferrocenyl precursor 2 was also reacted with an
incompletely condensed silsesquioxane cube,10 to form a
homogeneous model of the anchored heterogeneous catalyst.
Solution 1H NMR spectroscopy in C4D8O was used to
characterise the model compound (ESI†), and the absence of the
peaks for the hydroxy protons of the box at d 6.97 and the
methoxy protons of 2 at d 3.47, are diagnostic in this regard. The
MCM-41 bound catalyst and the silsesquioxane catalyst are
illustrated in Fig 2.
The two catalysts were tested in the one-step hydrogenation
of ethyl nicotinate to ethyl nipecotinate.‡ The catalysis was
performed under mild conditions (20 bar H2, 40 °C) and in both
cases proceeded with the formation of the desired nipecotinate.
However, analysis of the products revealed that the MCM-41
anchored species catalysed the reaction with a 17% ee whilst the
use of the homogeneous silsesquioxane complex resulted in a
racemic product. This remarkable change in stereoselectivity
demonstrates the profound importance of confinement in the
catalysis. The free catalyst shows no enantioselectivity whilst
chiral confinement results in a catalyst that shows greater
selectivity by almost a threefold margin than any other
reported.1 The confined catalyst also displayed a higher degree
of activity (TON = 291) compared to the homogeneous form
(TON = 98), after a reaction time of 72 h, and is remarkably
stable. The reaction mixture of the anchored catalyst contained
less than 3 ppb of metal (by ICP analysis), thereby ruling out the
possibility of any leaching.
We thank EPSRC for a rolling grant to J. M. T. and an award
to B. F. G. J. We also wish to thank ICI for a case studentship
to S. A. R. M.S.I. Inc. is gratefully acknowledged for the
molecular modelling software. We are also grateful for
assistance from Professor L. F. Gladden.
Notes and references
‡ The catalytic testing was performed in a high-pressure stainless steel
reactor (Cambridge Reactor Design) lined with PEEK (polyether ether
ketone). The catalyst (250 mg MCM-anchored, 100 mg box) was added to
5 g of ethyl nicotinate in 100 ml solvent (90 ml THF, 10 ml methanol). The
vessel was pressurised to 20 bar with hydrogen and heated to 40 °C, whilst
stirring was maintained at 400 rpm. During the reaction small aliquots were
removed, using a mini-robot autosampler, to enable the kinetics to be
studied. The products of the reaction were analysed by gas chromatograpy
(GC, Varian, Model 3400 CX) employing a BPX5 capillary column (25 m
3 0.32 mm) and flame ionisation detector. The ee was determined on the
same machine via the conversion of the nipecotinate to a diastereomeric
amide using (R)-(2)-Mosher’s acid chloride.2
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These results show the considerable potential that this type of
catalyst offers, and how, by careful design of an active centre, a
heterogeneous catalyst may be engineered, the performance of
which is far superior than its free, homogeneous analogue.
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