1806
R. J. Kell et al. / Bioorg. Med. Chem. Lett. 12 (2002) 1803–1807
readily accessible. Such a low percentage may arise
because there are interactions between the ‘active sites’
which the amount of diethylzinc present can not com-
pletely break up (see mechanistic discussion in ref 17).
That is, there is a further type of crosslinking.
9% higher. The explanation may in part be due to site–
site interactions producing crosslinks that limit swelling
and hence limit access to the ‘active sites’,4 but there are
other possible explanations. Thus, the reactions that
give racemates can take place both in the beads and in
the surrounding solvent, whereas the PS catalyst can
only influence the course of the reaction when the solu-
ble reactants (i.e., the aldehydes and dialkylzincs) are
within the beads. As a consequence the relative rates of
the catalysed and uncatalysed reactions depend crucially
on the distribution of the soluble reactants between the
bead phase and the solution phase. The present results
suggest a substantial fraction of the soluble reactants
are outside the beads.
Using 30mol% of PS catalyst, benzaldehyde, 4-chloro-
benzaldehyde and 4-carbomethoxy-benzaldehyde were
treated with dimethylzinc. As has been found in other
studies,10,13,27 these reactions were generally less satis-
factory than those with diethylzinc. It is not clear why
this should be. Thus, the % ees of the alcohol products
were significantly lower and the reactions were less
clean: see Table 1 entries 2, 4 and 6 and footnotes f and
g. Whilst, by GC–MS, the reaction with diethylzinc
gave <1% each of benzyl alcohol and propiophenone,
the reactions with dimethylzinc gave substantial
amounts of benzyl alcohol and acetophenone. How
such large amounts of benzyl alcohol are formed is not
clear, but the acetophenone presumably arises from by
hydride transfer from the initial product of addition of
dimethylzinc to benzaldehyde. We have suggested
before that reactions of this type cause PS catalysts such
as 1 to lose activity on repeated use.18 Such a side reac-
tion would not be possible with the PS N-methyl-a,a-
diaryl-l-prolinols used here.
In summary, using the approach summarised in Reac-
tion 2, PS catalysts containing N-methyl-a,a-diphenyl-
l-prolinol residues were easily prepared. The catalyst
moieties were bound through one or both phenyl resi-
dues. When PS catalyst A was used at 30mol% in tol-
uene at 20 ꢀC for examples of Reaction 1 involving
diethylzinc, the expected alcohols were obtained in 78–
94% ees. The PS catalysts recycle well and PS Catalyst
A was used successfully nine times. Where comparisons
can be made with the results obtained with the soluble
analogue 2, the PS catalysts usually afford somewhat
lower % ees. In part, this is due to the PS catalysts
having to compete with the background reactions
that give racemic alcohol products. Given the success
of the present study, in future work we propose to
prepare PS catalysts using the pure isomers of com-
pounds 4 and to use them for extended periods in flow
systems.18
Attention was next turned to PS Catalyst B. A series of
reactions was carried out between various aldehydes
and diethylzinc using one charge of 30mol% of PS
Catalyst B. It is evident from the results in Table 1 that
with this catalyst the % ees were 9% less on average
than those obtained with PS Catalyst A. This is
undoubtedly due to the fact that many of the catalyst
moieties are ‘double bound’. Apart from increasing the
extent of crosslinking, ‘double binding’ also means the
catalytic sites are on crosslinks and so are generally less
accessible than those on simple side chains.
Acknowledgements
We thank the EPSRC for Ph.D. (R.J.K.) and M.Sc.
(M.N.) Studentships.
It was hoped that the PS catalysts would recycle well.
The most extensively recycled sample was the charge of
PS Catalyst A which was used for all the eight reactions
carried out using 30mol% of the catalyst: see Table 1
and footnote e. After the eighth reaction, the reaction
summarised in entry 1 was repeated. It gave an ee of
87% compared with an ee of 88% for the first reaction.
This is encouraging and suggests that the present cata-
lyst moieties are more robust than those used in the PS
catalyst 1 studied previously.17,18
References and Notes
1. Clapham, B.; Reger, T. S.; Janda, K. D. Tetrahedron 2001,
57, 4637.
2. Hodge, P. In Innovation and Perspectives in Solid Phase
Synthesis; Epton, R., Ed; SPCC, Birmingham, 1990; p. 273.
3. De Miguel, Y. R. J. Chem. Soc., Perkin Trans. 1 2000,
4213.
4. Hodge, P. Chem. Soc. Rev. 1997, 26, 417.
5. Hodge, P.; Khoshdel, E.; Waterhouse, J.; Frechet, J. M. J.
J. Chem. Soc., Perkin Trans. 1 1985, 2327.
6. Hodge, P.; Kell, R. J.; Ma, J.; Morris, H. Aust. J. Chem.
1999, 52, 1041.
7. Pu, L.; Yu, H.-B. Chem. Rev. 2001, 101, 757.
8. Soai, K.; Niwa, S. Chem. Rev. 1992, 92, 833.
9. Itsuno, S.; Frechet, J. M. J. J. Org. Chem. 1987, 52, 4140.
10. Soai, K.; Niwa, S.; Watanabe, M. J. Org. Chem. 1988, 53,
927.
For comparison purposes reactions were also carried out
with soluble catalyst 2: see reference 28. When diethyl-
zinc was used the chemical yields, like those with the PS
catalysts, were >90%. The % ees obtained with this
catalyst are given in Table 1 and are in excellent agree-
ment with those reported in the literature8,23 bearing
in mind that the present reactions were carried out in
toluene at 20 ꢀC whereas most of the literature reactions
were carried out in hexane at 0 ꢀC. The % ees obtained
with catalyst 2 should be compared with those obtained
using 30mol% of PS Catalyst A. It is evident that
whilst the reactions catalysed by compound 2 in some
cases afford the same % ees, in other cases they are upto
11. Soai, K.; Niwa, S.; Watanabe, M. J. Chem. Soc., Perkin
Trans. 1 1989, 109.
12. Soai, K.; Watanabe, M. J. Chem. Soc., Chem. Comm.
1990, 43.
13. Itsuno, S.; Sakurai, Y.; Ito, K.; Maruyama, T.; Naka-
hama, S.; Frechet, J. M. J. J. Org. Chem. 1990, 55, 304.