5
654
K. Shimizu et al. / Tetrahedron Letters 43 (2002) 5653–5655
followed by centrifuging and washing with deionized
water, and subsequently drying in vacuo at 298 K. The
metal content of the catalyst (0.18 wt%) was determined
using ICP. XRD patterns of the catalysts were essen-
tially the same as that of sepiolite. The surface area of
ing step in the Suzuki reaction of aryl bromides on
2+
Pd -sepiolite is not the oxidative addition of aryl
halides to the palladium catalyst.
We performed the leaching test for the reaction of
4-bromoanisole at 100°C; when the solid catalyst was
removed before a completion of the reaction (reaction
time=1 h), the reaction did not proceed any further.
2
+
2
−1
Pd -sepiolite (240 m g by BET method) was very
2
−1
close to that of the original sepiolite (248 m g ). These
results suggest that the palladium complex is immobi-
lized on the surface of sepiolite, without changing tun-
nel structure of sepiolite.
2
+
This proves heterogeneous catalytic activity of Pd -
sepiolite and no contribution from homogenous cataly-
sis. The catalyst could be easily separated from the
reaction mixture by simple filtration and recycled with-
out loosing its activity in the reaction of 4-bromoan-
isole (entry 4). For a comparison, commercially
available palladium catalyst (Pd/C) was also tested for
The catalyst was tested for the cross-coupling between
aryl halide and phenylboronic acid (Scheme 1). Typi-
cally, the reaction was carried out by stirring the reac-
tion mixture containing aryl halide (2.5 mmol),
phenylboronic acid (3.7 mmol), potassium carbonate (5
2
+
this reaction. Compared to Pd -sepiolite (entry 4),
Pd/C showed lower yield and significantly lower TOF
(entry 12). Palladium acetate in bulk solution (entry
13), i.e. homogeneous catalysis, gave higher initial rate
mmol) and the catalyst (0.5 mmol of Pd) in DMF (5
3
cm ) at 100°C under N . As shown in Table 1, the
2
2
+
Pd -sepiolite catalyzed the Suzuki cross-coupling reac-
tion of an aryl iodide or aryl bromides with various
substituents and provided the corresponding coupling
products in excellent yields using a small amount of the
catalyst (0.02 mol%). As expected, aryl chloride was
most inactive (entry 8). Variation of the substituents in
the aryl bromides was also tested. Electron-donating
and electron-withdrawing substituents were both well
tolerated by the catalytic system and the coupling prod-
ucts were obtained in excellent yields. However, the
initial rate of the reaction depended on the substituents;
the ‘non-activated’ substrate (entry 2) and ‘deactivated’
2+
(TOF) than Pd -sepiolite, but resulted in a lower yield
2+
after 24 h than that of Pd -sepiolite.
2+
To evaluate the durability of the Pd -sepiolite catalyst,
we have examined the Suzuki reaction of several aryl
bromides with low catalysts concentration (entries 9–
11). In the cross-coupling of bromobenzene at 130°C, a
yield of 39% was obtained after 1 h with 0.001 mol% of
−
1
palladium, corresponding to TOF value of 39000 h .
After 24 h, the reaction proceeded in 65% yield
(TON=65000). As for 4-bromoanisole and 4-bro-
moacetophenone, under the same reaction conditions,
the products were obtained after 24 h in yields of 56
and 94%, respectively, corresponding to TONs of 56000
and 94000, respectively. To the best of our knowledge,
these are the highest activities for the heterogeneously
catalyzed Suzuki cross-coupling of aryl bromides.
(
4
electron-rich) substrates, such as 4-bromoaniline and
-bromoanisole (entries 3–5) gave better initial rates
than the ‘activated’ (electron-poor) substrates (entries 6
and 7). This reactivity tendency is in contrast to that
generally observed for palladium-catalyzed cross-cou-
9
pling reactions, which suggests that the rate-determin-
2+
a
Table 1. Reactions of aryl halides with phenylboronic acid over Pd -sepiolite catalyst
Entry
Substrate
C H I
T (°C)
Yield (%)b
TONc
TOFd (h−1
)
1
2
3
4
5
6
7
100
100
100
100
100
100
100
100
130
130
130
100
100
80
81
77
4000
4050
3850
4250
4550
4150
4550
230
65000
56000
94000
2000
2200
1595
2098
2380
1633
1532
819
1033
63
39000
9292
7163
74
6
5
C H Br
6
5
4-NH C H Br
2
6
4
e
4-MeOC H Br
85 (84)
6
4
3-ClC H Br
91
83
91
23
65
56
94
40
44
6
4
4-CH COC H Br
3
6
4
4-NO C H Br
2
6
4
f
8
4-CH COC H Cl
3
6
4
g
9
C H Br
6
5
g
1
1
1
1
0
4-MeOC H Br
6 4
g
1
4-CH COC H Br
3
6
4
h
2 (Pd/C)
3 (Pd(OAc)2)
4-MeOC H Br
6 4
i
4-MeOC H Br
1987
6
4
a
b
c
d
e
f
3
Reaction conditions: aryl halide (2.5 mmol), phenylboronic acid (3.7 mmol), K CO (5 mmol), catalyst (0.5 mmol of Pd), DMF (5 cm ).
2
3
GC yield using benzonitrile as internal standard after 20–24 h.
TON=(mol of product/mol of catalyst).
Turnover-frequency calculated at reaction time of 1 h.
Cycle 2.
Amount of the catalyst was 2.5 mmol of Pd.
g
h
i
3
Reaction conditions: aryl halide (25 mmol), phenylboronic acid (37 mmol), K CO (50 mmol), catalyst (0.25 mmol of Pd), DMF (25 cm ).
2
3
Pd/C catalyst (Pd=0.5 wt%) was used.
Palladium(II) acetate was used as homogeneous catalyst.