Chemistry Letters Vol.34, No.12 (2005)
1627
Table 2. Epoxidation of various alkenes by V-mont in the
a
This work was supported by a Grant-in-Aid for Scientific
Research from JSPS. We thank the Center of Excellence
(21COE) program ‘‘Creation of Integrated Ecochemistry’’ of
Osaka University.
presence of O2
Yield of epoxide/%b
Entry
1
Substrate
Selectivity/%
Cyclooctene
Cyclooctene
Cyclooctene
Cyclododecene
Cyclopentene
2-Octene
80
79
78
40
35
21
11
>99
98
c
2
References and Notes
d
3
98
93
1
a) ‘‘Modern Oxidation Methods,’’ ed. by J.-E. B a¨ ckvall, Wiley-VCH,
Weinheim (2004). b) ‘‘The Activation of Dioxygen and Homogeneous
Catalytic Oxidation,’’ ed. by D. H. R. Barton, A. E. Martell, and D. T.
Sawyer, Plenum, New York (1993). c) R. A. Sheldon and J. K. Kochi,
4
5
e
54
80f
85g
6
‘‘Metal-Catalyzed Oxidation of Organic Compounds,’’ Academic Press,
New York (1981).
7
1-Octene
a
2
There is only one heterogeneous catalyst for liquid-phase epoxidation,
which has been applied only to styrene, see: a) Q. Tang, Y. Wang,
J. Liang, P. Wang, Q. Zhang, and H. Wan, Chem. Commun., 2004,
440. Homogeneous catalysts, see: b) Y. Nishiyama, Y. Nakagawa, and
N. Mizuno, Angew. Chem., Int. Ed., 40, 3639 (2001). c) R. Neumann
and M. Dahan, J. Am. Chem. Soc., 120, 11969 (1998). d) R. Neumann
and M. Dahan, Nature, 388, 353 (1997). e) A. S. Goldstein, R. H. Beer,
and R. S. Drago, J. Am. Chem. Soc., 116, 2424 (1994). f) M. M. T. Khan
and A. P. Rao, J. Mol. Catal., 39, 331 (1987). g) J. T. Groves and
R. Quinn, J. Am. Chem. Soc., 107, 5790 (1985).
Substrate (3 mmol), V-mont (0.1 g, V: 0.019 mmol), ꢀ,ꢀ,ꢀ-tri-
fluorotoluene (1 mL), 90 C, 72 h, O2 atmosphere. Determined
ꢁ
b
c
by GC analysis using an internal standard technique. Reuse-1.
f
d
e
Reuse-2. 2-Cyclopentene-1-ol was formed. Small amounts of
g
octanal was formed. Small amounts of decanal was formed.
OH
OH
O
V-mont (0.6 mol%)
+
+
tert-butyl acetate (10 mL),
OH
3
4
a) Y. Izumi and M. Onaka, Adv. Catal., 38, 245 (1992). b) P. Laszlo,
Acc. Chem. Res., 19, 121 (1986). c) T. J. Pinnavaia, Science, 220, 365
(
1)
(2)
(3)
9
6 h, 1 atm of O2, 100 °C
Total Yield 93%
(1983).
Selectivity; (1) : (2) : (3) = 41 : 44 : 15
a) T. Kawabata, M. Kato, T. Mizugaki, K. Ebitani, and K. Kaneda,
Chem.—Eur. J., 11, 288 (2005). b) T. Kawabata, T. Mizugaki, K.
Ebitani, and K. Kaneda, J. Am. Chem. Soc., 125, 10486 (2003). c) T.
Kawabata, T. Mizugaki, K. Ebitani, and K. Kaneda, Tetrahedron Lett.,
Scheme 1.
tive liquid-phase epoxidation of cyclooctene using a heterogene-
ous catalyst with an atmospheric pressure of O2 as the sole oxi-
dant.2
44, 9205 (2003). d) T. Kawabata, M. Kato, T. Mizugaki, K. Ebitani,
and K. Kaneda, Chem. Lett., 32, 648 (2003). e) K. Ebitani, M. Ide, T.
Mitsudome, T. Mizugaki, and K. Kaneda, Chem. Commun., 2002,
The scope for epoxidation using the V-mont catalyst is sum-
marized in Table 2. This V-mont selectively catalyzed the epox-
idation of various kinds of cyclic and linear alkenes with 1 atm of
O2, affording the corresponding epoxides as major products.
Upon completion of the epoxidation of cyclooctene, the V-mont
was separated from the reaction mixture by simple filtration, and
could be reused without any appreciable loss of its high catalytic
activity and selectivity (Entries 2 and 3).
Additionally, the above V-mont exhibited high catalytic ac-
tivity for the oxygenation of adamantane in tert-butyl acetate
solvent under an atmospheric O2 pressure, affording 1-adaman-
tanol (1), 1,3-adamantanediol (2), and 2-adamantanone (3); the
6
90. f) T. Kawabata, T. Mizugaki, K. Ebitani, and K. Kaneda, Tetra-
hedron Lett., 42, 8329 (2001). g) K. Ebitani, T. Kawabata, K.
Nagashima, T. Mizugaki, and K. Kaneda, Green Chem., 2, 157 (2000).
After calcination of the V-mont, the diminishing intensity of the (001)
diffraction and maintaining of the clay phase are indicative of the trans-
formation into a card-house structure.
The V ions in Na3VO4 and VOSO4 are known to exist in a tetrahedral
coordination and square-pyramidal coordination, respectively, see:
J. Wong, F. W. Lytle, R. P. Messmer, and D. H. Haylotte, Phys. Rev.
B, 30, 5596 (1984).
5
6
7
8
H. G. Bachmann, F. R. Ahmed, and W. H. Barnes, Z. Kristallogr.
Mineral., 115, 110 (1961).
Various metal cation-exchanged monts (M-monts) were prepared in a
similar way by treatment of Na-mont with aqueous solution of the cor-
responding metal chlorides. A general procedure for V-mont-catalyzed
epoxidation of cyclooctene is as follows: Into a reaction vessel equipped
with a reflux condenser and balloon were placed the V-mont (0.1 g, V:
total yield of oxygenated products reached 93% at 96 h, as
shown in Scheme 1.10 Oxidation did not proceed in the absence
of the V-mont under identical reaction conditions. This yield is
higher than those reported for other methods of adamantane
0.019 mmol), cyclooctene (3 mmol), and ꢀ,ꢀ,ꢀ-trifluorotoluene (1
mL). After vigorous stirring of the heterogeneous reaction mixture at
ꢁ
1
1
oxidation with O2 as a sole oxidant.
The above two oxidation reactions were inhibited by the
90 C for 72 h, the catalyst was separated by centrifugation. GC analysis
of the supernatant showed an 80% yield of epoxide.
9
With respect to solvents, the use of ꢀ,ꢀ,ꢀ-trifluorotoluene and tert-
butyl acetate afforded high yields of cyclooctene oxide (80%). The reac-
tion carried out in CH3CN gave a moderate yield (30%), while toluene,
and 1,2-dichloroethane were significantly less effective (<1%).
addition of radical scavengers such as p-tert-butylcatechol and
2,6-di-tert-butylphenol. Furthermore, the ratio of oxidation at
tertiary vs secondary positions in the oxygenation of adamantane
was 8.6:1, which is similar to the ratio observed for radical
oxidations.12 These facts suggest that the above oxidations by
10 1-Adamantanol was a major product at 48 h. The selectivities of (1), (2),
and (3) were 78:4:18, respectively.
1
1a,12
11 Product yields for oxygenation of adamantane: a) S. Shinachi, M.
Matsushita, K. Yamaguchi, and N. Mizuno, J. Catal., 233, 81 (2005),
vanadium-substituted phosphomolybdates catalyst (84%). b) K.
Yamaguchi and N. Mizuno, New J. Chem., 26, 972 (2002), Ru-substitut-
ed silicotungstate catalyst (42%). c) N. Mizuno, M. Tateishi, T. Hirose,
and M. Iwamoto, Chem. Lett., 1993, 2137, Ni and Fe-substituted hetero-
polyanion catalyst (29%). d) M. M. T. Khan, D. Chatterjee, S. Kumar,
and A. P. Rao, J. Mol. Catal., 75, L49 (1987), Ru-saloph complex
catalyst (13%). See: 2C) Ru-substituted polyoxometalate catalyst (57%).
the V-mont involve a radical oxidation mechanism.
In conclusion, we have developed a highly efficient hetero-
geneous catalyst system based on monts for the epoxidation with
molecular oxygen. This system has the following advantages: (a)
the use of 1 atm of molecular oxygen as an oxidant without the
need for reducing reagents or radical initiators, (b) high catalytic
activity and selectivity, (c) recyclable catalysts, and (d) applica-
tion to aerobic oxygenation of adamantane via C–H activation.
Further studies on mechanistic details and possible extension
to other organic syntheses are currently underway.
12
a) Y. Ishii, J. Mol. Catal. A: Chem., 117, 123 (1997). b) Y. Ishii, T.
Iwasawa, S. Sakaguchi, K. Nakayama, and Y. Nishiyama, J. Org.
Chem., 61, 4520 (1996).
Published on the web (Advance View) November 8, 2005; DOI 10.1246/cl.2005.1626