Communications
Table 1: Rhodium-catalyzed dehydrogenative silylation of EtOH.[a]
Although we have not been successful in direct quantification
of the density of P atoms in 1 and 2, the density of the Au(111)
single crystal surface modified with the phosphane sulfide
derivative of 4 was accurately determined by electrochemical
reductive desorption of the attached thiolate molecules.[10]
The analysis indicated that the surface density of the thiolates,
which should be identical to the density of P atoms, is
0.69 nmolcmÀ2 (4.2 moleculesnmÀ2; the corresponding den-
sity for the linear alkanethiolate SAM on Au(111) is
4.6 moleculesnmÀ2), which strongly suggests the formation
of a monolayer in the closest packing arrangement (see the
Supporting Information).
Surface modification of a decanethiol derivative bearing a
conventional Ph2P-type coordinating group to afford [Au]-
Ph2P-Rh was also conducted for comparison. ICP-MS analysis
showed a density of Rh atoms (per geometric surface area) of
(0.71 Æ 0.06) nmolcmÀ2, which is almost identical to the value
(0.63 nmolcmÀ2) for 2.
We first examined [Au]-SMAP-Rh (2) for its catalytic
activity towards the hydrosilylation of ketones. Upon reaction
with cyclohexanone and Me2PhSiH (1.1 equiv) in hexane
(ketone/Rh 75000:1), 2 showed exceptionally high catalytic
activity, with a turnover number (TON) of 9800 over 30 h at
258C.[11] In contrast, the corresponding homogeneous con-
ditions, consisting of a mixture of [{RhCl(C2H4)2}2] and Ph-
SMAP (5) (Rh/P 1:1) in CH2Cl2 (ketone/Rh 100:1), afforded a
TON of 51 under otherwise identical condi-
Entry
Catalyst
t [h] Yield [%] TON[b] Total TON
1
2
3
4
[Au]-SMAP-Rh (2)[c]
2nd run
3rd run
16
16
16
16
16
30
16
80
81
78
73
36
37
9
60000
61000
59000
55000
15000
16000
3900
121000
180000
235000
4th run
5[d]
6[d]
7[d]
[{RhCl(C2H4)2}2]
[{RhCl(C2H4)2}2]
5/[{RhCl(C2H4)2}2]
(P/Rh 1:1)
8[d]
5/[{RhCl(C2H4)2}2]
(P/Rh 1:1)
30
9
3900
9[e]
[Au]-Ph2P-Rh[c]
2nd run
16
16
45
7
30000
4700
10[e]
34700
[a] The reaction was carried out with Me2PhSiH (12 mmol), EtOH
(1.2 equiv), and catalyst (Me2PhSiH/Rh 75000:1) in hexane (0.12 mL) at
258C. [b] Catalyst turnover number. [c] A gold surface with dimensions of
55 mm2 was used. [d] The reaction was carried out in CH2Cl2.
Me2PhSiH/Rh 43000:1. [e] Me2PhSiH/Rh 67000:1.
To obtain further information on the Rh species after the
catalytic reaction we analyzed 2 by XPS. The binding energy
of Rh 3d was 308.0 eV, which is much higher than that of
metallic Rh (typically, at 306.0–307.5 eV). The binding energy
of P 2p after the reaction was similar to that before the
reaction and much higher than free, noncoordinating phos-
phane (at 130.1 eV). The P/Rh elemental ratio was calculated
to be 1:0.8. On the basis of these XPS results, it is unlikely that
the major component of the Rh species consists of nano-
tions. Moreover, 2 showed good reusability
(TON of 25000 over three successive runs).
However, its applicability to other ketones was
very limited. This result was in sharp contrast
with that of the related silica-supported SMAP
ligand [silica]-SMAP,[12] which was applicable
particles.[9,15] It is probable that the P Rh bond is maintained
in [Au]-SMAP-Rh (2) during the catalysis.
À
to a broad range of sterically hindered ketones. The narrow
substrate scope of the hydrosilylation catalyzed by 2 suggests
a severely crowded catalytic environment.
The use of [{RhCl(C2H4)2}2] in the solution phase (a
homogeneous control) showed a TON of 15000, which was
only a quarter of that obtained with 2 (Table 1, entry 5). The
addition of SMAP 5 to the Rh complex (P/Rh 1:1) caused a
further decrease in the activity (Table 1, entry 7). In addition
to the moderate effect of the immobilization on activity
enhancement, a more pronounced effect was observed in
terms of the catalyst lifetime and reusability. In fact, the
homogeneous catalyst systems completely lost their activities
within 16 h, and afforded no further conversion after pro-
longed reaction times (Table 1, entries 6 and 8).
The same reaction was also catalyzed by [Au]-Ph2P-Rh,
which resulted in a yield of 45% and a TON of 30000 for the
first use. Interestingly, the yield for the second use of [Au]-
Ph2P-Rh dropped to 7%, which indicates that the SMAP
structure was critically important for the robustness and
reusability of the catalytically active surfaces. Furthermore,
[Au]-Ph2P-Rh was found to be unstable under the reaction
conditions. XPS analysis of the [Au]-Ph2P-Rh after a catalytic
reaction showed significant decomposition of the catalyst
monolayer. Although the signal intensity of the S atom
remained unchanged, only a trace amount of P atoms was
detected.
Thus, we turned our attention to the dehydrogenative
silylation of alcohols with a hydrosilane,[13,14] with the expect-
ation that this reaction would be less sterically demanding
(Table 1). Accordingly, a single chip of [Au]-SMAP-Rh (2; 5
5 mm2) was placed at the bottom of a glass screw-capped test
tube containing a solution of Me2PhSiH (12 mmol) and EtOH
(1.2 equiv) in hexane (0.12 mL). The substrate/catalyst ratio
(S/C) under these conditions was 75000:1, based on the
surface density of Rh atoms. The reaction was conducted at
258C without stirring. After 16 h, 80% of the Me2PhSiH was
converted into the silyl ether. This conversion corresponds to
a TON of 60000 (Table 1, entry 1).
The platelike shape of the catalyst means that recycling
can be readily achieved by physically transferring the used
catalyst chip into the reaction vessel for the next run. The
TON over four successive runs reached a total of 235000
(Table 1, entries 1–4). The activity of 2 was maintained during
repeated uses, thus indicating that the active species was not
released into the solution phase, but remained on the catalyst
surface without significant loss of activity. ICP-MS analysis of
the solution phase after a catalytic reaction indicated that
only less than 0.5% of the Rh atoms had leached out from the
Au surface.
The range of substrates compatible with the dehydrogen-
ative silylation catalyzed by 2 (5 5 mm2, S/C 75000:1, 258C,
5628
ꢀ 2008 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Angew. Chem. Int. Ed. 2008, 47, 5627 –5630