Chelation-Controlled Rhodium-Catalyzed Hydroacylation
FULL PAPER
Table 4. Traceless chelation-controlled hydroacylation.[a]
could also be prepared in good yield, showing the compati-
bility of this reaction with heterocyclic scaffolds. However,
substrate 3h with a benzylic amine was unreactive. Substrate
3i, featuring a para-disposed acyl group, was also unreactive,
thus confirming the requirement for ortho-coordination.
We have previously reported that complex C is a highly
active catalyst for the sulfide-directed hydroacylation of al-
kenes and alkynes.[15] This raised the exciting possibility of
performing hydroacylation reactions, in which the SMe
À
group would act as a directing group for aldehyde C H acti-
À
vation, followed by reductive cleavage of the C S bond with
the same catalyst. This reaction would give ketone products,
in which the thiomethyl group acts as a traceless directing
group. Based on the ease with which the thiomethyl sub-
stituent can be introduced, by using simple SNAr chemistry,
this combination would provide an attractive route to
ketone products. We tested this concept by subjecting the al-
dehyde 5a to hydroacylation conditions, employing
10 mol% of catalyst C and 1-octene (Table 4). After two
hours at 808C, the mixture was cooled to room temperature,
and (EtO)3SiH was added. After stirring overnight, we were
pleased to find that the ketone 6a could be isolated in 87%
yield. The alkene component of this reaction could be easily
varied, and very good functional group tolerance was ob-
served. For example, products featuring ester (6b), acetal
(6c) and sulfonamide (6d) groups were all delivered in good
yields. This reaction is also highly compatible with both
alkyl- (6e) and aryl-halides (6 f), allowing for the possibility
of further functionalization of the products. Variation of the
aldehyde component of the reaction was also possible. The
dimethoxy aldehyde 5g gave the ketone product in 84%
yield, and an aldehyde with both ortho- and para-SMe
groups gave the ortho-reduced product in good yield. Pleas-
ingly, the aldehyde scope was not limited to aromatic sub-
strates, as the cycloalkenyl aldehyde 5i delivered the corre-
sponding a,b-unsaturated ketone. The stability of the enone
product 6i suggested that the products of traceless alkyne
hydroacylation could also be accessed. By using the iPr-sub-
stituted catalyst E, recently reported as a highly active cata-
lyst for alkyne hydroacylation,[17] bulky terminal alkynes, as
well as an internal alkyne could be employed, delivering
enones 6j and 6k in excellent yields. Bis-enones were also
accessible (6l). Catalyst E was also used for the hydroacyla-
tion of butyl vinyl ether, which proceeds with high branched
selectivity to give the a-substituted ketone 6m. Finally, the
hydroacylation of an allene could be achieved with catalyst
C, which gave the b,g-unsaturated ketone 6n following
silane reduction.
[a] Conditions
5 (1.0 equiv), alkene/alkyne (1.5 equiv), complex C
(10 mol%), (EtO)3SiH (2.0 equiv), Isolated yields. [b] Complex E was
used as catalyst.
complex
D
(featuring the small bite-angle di-
AHCTUNGTREG(NNUN tBu)phosphine) can catalyse the hydroacylation of unacti-
vated alkenes at as low as 0.1% catalyst loading.[15] The
most efficient catalyst for the aryl sulfide reduction step is
complex E,[17] which can efficiently deliver the reduced com-
pound by using only 0.5 mol% loading (Scheme 2). By com-
bining these two catalysts into a one-pot tandem reaction,
the traceless hydroacylation product 2 could be isolated in
82% yield, although employing only 0.8 mol% Rh in total
(Scheme 2). This represents an efficient method for the syn-
thesis of these valuable ketone products. These two proce-
dures, involving either a single catalyst at higher loading, or
two separate catalysts at low loading, are complementary,
and allow the choice of either catalyst loading, or the con-
venience of a simplified reaction procedure, to be the para-
mount consideration.
The use of catalyst C represents a convenient method for
tandem hydroacylation/sulfide reduction, because this cata-
lyst is active in both steps, bench stable and easily prepared
from commercially available materials. However, the use of
the relatively high catalyst loading of 10 mol% for this
tandem reaction is not ideal. The amount of catalyst needed
can be dramatically reduced if two separate catalysts are
employed, each of which have been optimised for the indi-
vidual steps of the process. We have previously shown that
We have probed the mechanism of the sulfide reduction
process employing precatalyst C,[18] with a combination of
Chem. Eur. J. 2013, 19, 3125 – 3130
ꢀ 2013 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
3127