Moreover, we noticed that the dihydrogen pressure remained
constant throughout the reaction, giving evidence that dihydrogen
is not consumed. This data is in accordance with the fact that the
rhodium complex [(o-dppbe)Rh(COD)]OTf does not catalyse the
hydrogenation of acetophenone under these conditions. Finally, it
is worth mentioning that a constant dihydrogen pressure was
required to maintain the high catalytic activity of the rhodium
complex. Indeed, a run partially conducted under dihydrogen
pressure for 15 min (20 bar H2), depressurized to 1 bar and finally
stopped after 1 h afforded phenylethanol in a moderate yield
(50%). Nevertheless, depressurization did not ‘‘shut down’’
definitively the catalytic activity of the rhodium centre. Thus, a
run conducted successively at 20 bar (15 min), 1 bar (30 min) and
20 bar (15 min) led to phenylethanol in good yield (90%). One
might claim that the rate enhancement was due to the pressure and
not to dihydrogen itself. However, this possibility is excluded by
the fact that the catalytic hydrosilylation of acetophenone under
20 bar N2 led to a very poor yield.
generally accepted Rh(III) intermediates can undergo a second
oxidative addition of another molecule of silane, facilitating the
final reductive elimination step of the product. Based on these
previously reported mechanistic studies, we propose that dihydro-
gen replaces here the second molecule of silane in the generation of
the oxidative Rh(V) adducts. These complexes would then exist in
solution, but only if the local concentration of dihydrogen was
sufficient. This hypothesis explains all of the experimental results
1
described above. Further experiments, notably H NMR spectro-
scopy under dihydrogen pressure, are in progress aiming to
provide support for this hypothesis.
Using our experimental protocol (i.e. under 20 bar H2), we
hydrosilylated a range of aromatic and aliphatic ketones, the
results of which are presented in Table 1. For comparative
purposes, hydrosilylation reactions under an inert atmosphere
were carried out in parallel and quenched after the same reaction
1
time. Yields were determined by H NMR spectroscopy of the
crude products after desilylation. The hydrosilylation of propio-
phenone, a-tetralone and pinacolone provided the corresponding
alcohols in almost quantitative yields after only 1 h. In contrast,
the same catalyst under N2 gave the products in much lower yields
(5, 7 and 4% yields, respectively). Although the hydrosilylation of
cyclohexanone and acetone led to moderate yields (46 and 32%,
respectively), these reactions were still, respectively, 11 and 16 times
faster compared to those performed under an inert atmosphere.
When the rhodium complex [(dppe)Rh(COD)]OTf was used as the
catalyst precursor, a significant rate enhancement under dihydro-
gen pressure was also observed (Table 1, results in brackets).14 It is
noteworthy that this structurally comparable complex shows
different efficiencies depending on the ketone used. While results
were comparable with acetophenone, a-tetralone and pinacolone,
a lower yield was obtained with propiophenone as the substrate.
On the other hand, the rhodium complex with dppe as the ligand
was found to be more efficient for the hydrosilylation of
cyclohexanone and acetone.
According to the literature, hydrosilylation is often accompanied
by the undesired dehydrogenative silylation of the enol of
acetophenone (silyl enol ether).1,9 In the subsequent hydrolysis
step, the silyl enol ether reverts to the original acetophenone.
However, this side reaction, which represents a major drawback,
would have no impact on the yield of the reaction if a subsequent
catalytic hydrogenation of the silyl enol ether occurred. This would
also rationalize why dihydrogen is, overall, not consumed, since
silylation of the enol is accompanied by the evolution of molecular
1
hydrogen. To check this hypothesis, we measured the H NMR
spectrum of the crude product before hydrolytic work-up. The
spectrum of the product obtained after a hydrosilylation reaction
run under ‘‘normal’’ conditions (i.e. under an inert atmosphere)
showed signals corresponding to the hydrosilylated product (silyl
ether) together with those of residual acetophenone. No trace of
silyl enol ether was detected. According to the NMR spectrum, the
hydrosilylation of acetophenone under 20 bar H2 also led
exclusively to the hydrosilylated product. Moreover, attempts to
hydrogenate the trimethylsilyl enol ether derived from acetophe-
none in the presence of a catalytic amount of [(o-dppbe)Rh-
(COD)]OTf remained unsuccessful. These results, combined with
those discussed above, strongly suggest that dihydrogen is not the
stoichiometric reducing agent.
Since the hydrosilylation of ketones can be highly accelerated by
using different ligands, we envisioned taking advantage of this
phenomenon for an asymmetric version of this reaction.
Preliminary experiments were performed with [((R,R)-
Deguphos)Rh(COD)]OTf as the chiral catalyst and acetophenone
as the substrate. A significant rate enhancement associated with
dihydrogen pressure was again observed. While only a 27% yield
was obtained after 5 h under an inert atmosphere, the reaction
went to completion after 1 h if run under 20 bar H2. Interestingly,
the reaction product (phenylethanol) was obtained with a higher ee
To elucidate the positive role of dihydrogen on the kinetics, we
examined the hydrosilylation of acetophenone at 20 bar H2 with
Ph2SiD2. Surprisingly, under these conditions, the silyl ether was
obtained with only 40% deuterium incorporation. Moreover, the
addition of H2 (20 bar) to a THF solution of Ph2SiD2 in the
presence of a catalytic amount of the rhodium complex resulted in
the partial conversion of Ph2SiD2 to Ph2SiD22nHn (n = 1 or 2,
product containing only 33% of deuterium after 1 h). These results
of H/D exchange strongly suggest that both H2 and Ph2SiD2
undergo an oxidative addition to the same metal centre to give a
cationic rhodium(V) adduct.10–12 Subsequent repeated sequences of
reductive elimination–oxidative addition would allow the conver-
sion of Ph2SiD2 to Ph2SiH2. Since this kind of isotopic exchange
occurs in the presence of the ketone, we suspect that Rh(V) species
would also be involved in the hydrosilylation process. This
hypothesis is supported by previous studies, suggesting that
mechanisms of hydrosilylation involving Rh(V) species are
reasonable.13 An important suggestion in these reports is that
Table 1 Catalytic hydrosilylation of various ketonesa
Yield (%)b
Entry
Substrate
Under 20 bar H2
Under N2
1
2
3
4
5
Acetophenone
Propiophenone
a-Tetralone
Pinacolone
Cyclohexanone
Acetone
98 (94)
95 (57)
92 (90)
99 (99)
46 (96)
32 (62)
4 (5)
5 (2)
2 (3)
4 (6)
4 (5)
2 (6)
6
a
Conditions:
[(o-dppbe)Rh(COD)]OTf
(0.1
mol%),
ketone
b
(2.2 mmol), Ph2SiH2 (2.4 mmol), THF (2 mL), rt, 1 h. The yields
in brackets correspond to reactions performed with [(dppe)Rh-
(COD)]OTf as the catalyst.
714 | Chem. Commun., 2007, 713–715
This journal is ß The Royal Society of Chemistry 2007