the presence of aqueous KOH (1.5 M, 0.20 mL, 0.30 mmol)
in dioxane (1.8 mL) at 30 °C for 1 h. The phenylboronic
acid (3m) used for the present experiments is the com-
mercially available sample received from Tokyo Kasei
Kogyo. While the reaction in the presence of 1.0 or 0.10
mol % of the catalyst 1 gave a quantitative yield of the 1,4-
addition product 4am, further decrease of the catalyst caused
lower yields of 4am. Thus, the yield was 79% in the presence
of 0.05 mol % of catalyst 1 and no 4am was produced with
the catalyst loading of 0.01 mol %. The enantiomeric purity
of 4am was kept high (96% ee (S)) whenever it was obtained.
In the second set of experiments (entries 5-7), the loading
of catalyst 1 was kept constant (0.05 mol %) and the effects
of the amount of boronic acid 3m were studied. To our
surprise, the use of a larger amount of the boronic acid
resulted in a lower yield of the product. The reaction with
3.0 and 5.0 equiv of the boronic acid gave 4am in 37% and
0% yield, respectively. Consistent with this tendency, the
yield was higher (95%) with a smaller amount of boronic
acid (1.2 equiv). In the case of low yields, the starting enone
The catalytic activity of the rhodium complex [RhCl((S,S)-
9
Bn-bod*)]
dibenzylbicyclo[2.2.2]octa-2,5-diene,
the asymmetric 1,4-addition of phenylboronic acid (3m) to
2
(1), where (S,S)-Bn-bod* stands for (S,S)-2,5-
1c,d
was examined for
2
1
-cyclohexenone (2a). In the first set of experiments (entries
-4 in Table 1), the loading of catalyst 1 was decreased
Table 1. Rhodium-Catalyzed Asymmetric 1,4-Addition of
a
b
Phenylboronic Acid (3m) or Phenylboroxine (5m) to
(1)c
2a was recovered in the corresponding amounts. These rather
unusual results may suggest that the phenylboronic acid used
here contains a small amount of a contaminant which
deactivates the catalyst.
Attempts to remove the impurity by recrystallization of
the boronic acid were not successful, no 1,4-addition product
being obtained with the catalyst loading of 0.01 mol %. It
3
m or 5m
catalyst 1
(mol % Rh)
yield (%)
entry
(equiv B to 2a)
of 4amd
% eee
1
2
3
4
5
6
7
PhB(OH)2 (2.0)
PhB(OH)2 (2.0)
PhB(OH)2 (2.0)
PhB(OH)2 (2.0)
PhB(OH)2 (3.0)
PhB(OH)2 (5.0)
PhB(OH)2 (1.2)
(PhBO)3 (1.2)
(PhBO)3 (2.0)
(PhBO)3 (1.2)
1.0
100
100
[79]
[0]
[37]
[0]
95
96
100
71
96 (S)
96 (S)
96 (S)
0.10
0.05
0.01
0.05
0.05
0.05
0.01
0.01
0.005
3
was found that the use of phenylboroxine ((PhBO) , 5m) in
place of phenylboronic acid (3m) greatly improved the
present catalytic reaction. The boroxine 5m, which was
obtained by dehydration of the commercially available
boronic acid 3m by azeotropic removal of water from its
benzene solution and purified by washing the crude boroxine
96 (S)
96 (S)
96 (S)
96 (S)
96 (S)
f
8
9
0
f
g
10
1
repeatedly with hexane, gave high yields of the 1,4-addition
a
Commercially available boronic acid was used as received. b Prepared
product 4am (96% ee) in the presence of 0.01 mol % of the
catalyst 1 (entries 8 and 9). Under the same conditions (0.01
mol % of Rh catalyst), the 1,4-addition did not proceed at
all with phosphorus ligands such as binap or phosphorami-
dites, demonstrating the high catalytic activity of the diene
rhodium catalyst. A larger scale reaction is possible with
0.005 mol % of the catalyst, which gave 71% yield of 4am
in the reaction period of 1 h (entry 10), the turnover
frequency (TOF) of the catalyst being calculated to be 1.4
c
and purified by us (see text). The reaction was carried out with enone 2a
0.60 mmol) and aqueous KOH (1.5 M, 0.20 mL, 0.30 mmol) in dioxane
1.8 mL) at 30 °C for 1 h. Isolated yield of 4am by silica gel
chromatography. The yields in brackets are those obtained by H NMR
with nitromethane as an internal standard. Determined by HPLC analysis
with a chiral stationary-phase column (Chiralcel OD-H). Enone 2a (3.0
mmol) and aqueous KOH (5 M, 0.30 mL, 1.5 mmol) in dioxane (3.0 mL).
The reaction of 1.73 g (18 mmol) of enone 2a.
(
(
d
1
e
f
g
from 1.0 to 0.01 mol % for the reaction of enone 2a (0.60
mmol) with boronic acid 3m (1.2 mmol, 2 equiv to 2a) in
4
-1
×
10 h . To the best of our knowledge, this TOF number
is highest for the catalytic asymmetric carbon-carbon bond-
8
forming reactions including asymmetric 1,4-addition reac-
tions.
(
7) (a) ComprehensiVe Asymmetric Catalysis; Jacobsen, E. N., Pfaltz,
A., Yamamoto, H., Eds.; Springer-Verlag: Heidelberg, Germany, 1999.
b) Catalytic Asymmetric Synthesis, 2nd ed.; Ojima, I., Ed.; Wiley-VCH:
New York, 2000.
8) For reports describing high TOF: (a) Long, J.; Hu, J.; Shen, X.; Ji,
11,12
(
Arylboroxine and water are known to be in a fast
13
equilibrium with arylboronic acid, and hence, the reaction
(
2
-1
B.; Ding, K. J. Am. Chem. Soc. 2002, 124, 10 (TOF ) 1.0 × 10 h ). (b)
Yoshida, T.; Morimoto, H.; Kumagai, N.; Matsunaga, S.; Shibasaki, M.
(10) Washing the solid boroxine with hexane is essential for the required
high purity.
(11) Examples of low catalyst loadings in rhodium-catalyzed asymmetric
1,4-addition: (a) Amengual, R.; Michelet, V.; Gen eˆ t, J.-P. Synlett. 2002,
1791. (b) Takaya, Y.; Ogasawara, M.; Hayashi, T. Tetrahedron Lett. 1999,
40, 6957. (c) Reetz, M. T.; Moulin, D.; Gosberg, A. Org. Lett. 2001, 3,
4083.
2
-1
Angew. Chem., Int. Ed. 2005, 44, 3470 (TOF ) 2.4 × 10 h ). (c) Kina,
A.; Shimada, T.; Hayashi, T. AdV. Synth. Catal. 2004, 346, 1169 (TOF )
2
-1
3
.5 × 10 h ). (d) Matsunaga, S.; Kinoshita, T.; Okada, S.; Harada, S.;
3 -1
Shibasaki, M. J. Am. Chem. Soc. 2004, 126, 7559 (TOF ) 3.1 × 10 h ).
(
3
e) Davies, H. M. L.; Venkataramani, C. Org. Lett. 2003, 5, 1403 (TOF )
3
-1
.8 × 10 h
)
(9) The rhodium complex was obtained by treatment of (S, S)-Bn-bod*
(12) In the nonasymmetric 1,4-addition of an arylboronic acid, high TOF
1
4
-1
with [RhCl(C2H4)2]2 in chloroform. H NMR (CDCl3): δ 0.24 (m, 4H),
.52 (m, 4H), 2.76 (d, J ) 14.1 Hz, 4H), 3.52 (br, 4H), 3.54 (d, J ) 14.0
Hz, 4H), 4.03 (d, J ) 5.4 Hz, 4H), 7.21 (t, J ) 7.3 Hz, 4H), 7.29 (t, J )
.4 Hz, 8H), 7.35 (d, J ) 7.4 Hz, 8H).
(up to 1.0 × 10 h ) of [Rh(OH)(cod)]2 as a catalyst has been reported:
Itooka, R.; Iguchi, Y.; Miyaura, N. J. Org. Chem. 2003, 68, 6000.
(13) Tokunaga, Y.; Ueno, H.; Shimomura, Y.; Seo, T. Heterocycles 2002,
57, 787.
0
7
342
Org. Lett., Vol. 8, No. 2, 2006