hand, many useful catalytic oxidation methods have been
elaborated,10-17 among which aerobic oxidation procedures
with transition metal catalysts have an advantage from
economic and environmental viewpoints.12-17 However, these
systems require relatively expensive metal catalysts, a large
quantity of additives, and a higher reaction temperature to
obtain satisfactory results.
Oppenauer (OPP) oxidation,18-20 the reverse process of
the Meerwein-Ponndorf-Verley (MPV) reduction (Scheme
1),19b,21 is a classical yet useful method and is widely
is still room for improvement in terms of catalytic efficiency
and substrate generality.22-26 Further, only a few examples
of aluminum-based OPP catalyst have appeared in the
literature.27 Recently, we disclosed new aluminum alkoxide
3 as a highly effective MPV reduction catalyst,28 and this
discovery prompted us to pursue the application of the
organoaluminum precatalyst 2 to OPP oxidation (Scheme
2). In this letter, we wish to report preliminary results of
Scheme 2. Application of Catalyst 2 to OPP Oxidation
Scheme 1. Opp Oxidation and MPV Reduction
employed for the synthesis of steroids and terpenoids. Despite
its operational simplicity with inexpensive and nontoxic
reagents such as Al(OBut)3 and Al(OPri)3 as well as eminent
functional group compatibility, the full synthetic potential
of this oxidation has yet to be realized mainly because of
the low reactivity of the metal alkoxides. Actually, use of 1
equiv of reagent or more with a large excess of hydride
acceptor under relatively drastic conditions is a usual recipe
but causes undesirable side reactions, i.e., dehydration of
alcohols and aldol condensations. Although some beautiful
modifications of OPP oxidation have been introduced, there
this study, providing a practical catalytic OPP oxidation
procedure.
First, we examined the reactivity of aluminum catalyst 2,
prepared in situ by mixing Me3Al and ligand 1 in CH2Cl2,28
in the OPP oxidation of carveol as a representative substrate
with 1.2 equiv of t-BuCHO as a hydride acceptor at 21 °C
for 1 h (Table 1).29 The reaction proceeded smoothly with 5
mol % of 2 to afford carvone in 90% isolated yield (entry
1). Notably, the loading of 2 can be reduced to 1 mol %
without losing the catalytic activity (entry 2).30 Needless to
(10) For recent heterogeneous catalysts, see: (a) Nishimura, T.; Kakiuchi,
N.; Inoue, M.; Uemura, S. Chem. Commun. 2000, 1245. (b) Dijksman, A.;
Arends, I. W. C. E.; Sheldon, R. A. Synlett 2001, 102. (c) Choudary, B.
M.; Kantam, M. L.; Rahman, A.; Reddy, C. V.; Rao, K. K. Angew. Chem.,
Int. Ed. 2001, 40, 763. (d) Itoh, A.; Kodama, T.; Inagaki, S.; Masaki, Y.
Org. Lett. 2001, 3, 2653. (e) Son, Y.-C.; Makwana, V. D.; Howell, A. R.;
Suib, S. L. Angew. Chem., Int. Ed. 2001, 40, 4280.
Table 1. Catalytic OPP Oxidation of Carveola with 2 in
Various Solventsb
(11) For unaerobic catalytic oxidations, see: (a) Ley, S. V.; Norman, J.;
Griffith, W. P.; Marsden, S. P. Synthesis 1994, 639. (b) Mukaiyama, T.;
Matsuo, J.; Iida, D.; Kitagawa, H. Chem. Lett. 2001, 846. (c) Hashimoto,
K.; Kitaichi, Y.; Tanaka, H.; Ikeno, T.; Yamada, T. Chem. Lett. 2001, 922.
(12) Pd catalysts: (a) ten Brink, G.-J.; Arends, I. W. C. E.; Sheldon, R.
A. Science 2000, 287, 1636. (b) Hallman, K.; Moberg, C. AdV. Synth. Catal.
2001, 343, 260. (c) Ferreira, E. M.; Stoltz, B. M. J. Am. Chem. Soc. 2001,
123, 7725.
(13) Cu catalysts: (a) Marko, I. E.; Giles, P. R.; Tsukazaki, M.; Brown,
S. M.; Urch, C. J. Science 1996, 274, 2044. (b) Marko, I. E.; Gautier, A.;
Mutonkole, J.-L.; Dumeunier, R.; Ates, A.; Urch, C. J.; Brown, S. M. J.
Organomet. Chem. 2001, 624, 344.
(14) Ru catalysts: (a) Marko, I. E.; Giles, P. R.; Tsukazaki, M.; Chelle-
Regnaut, I.; Urch, C. J.; Brown, S. M. J. Am. Chem. Soc. 1997, 119, 12661.
(b) Dijksman, A.; Marino-Gonzalez, A.; Mairata i Payeras, A.; Arends, I.
W. C. E.; Sheldon, R. A. J. Am. Chem. Soc. 2001, 123, 6826.
(15) Mo catalyst: Lorber, C. Y.; Smidt, S. P.; Osborn, J. A. Eur. J. Inorg.
Chem. 2000, 655.
entry
2 (mol %)
solvent
CH2Cl2
% yieldc
1
2
3
4
5
6
5
1
1
1
1
1
90
94
94
92
80d
83d
toluene
cyclohexane
THF
AcOEt
a Cis/trans ) 42:58. b Unless otherwise specified, the oxidation of carveol
was conducted with 2 as a catalyst (prepared in each solvent) and t-BuCHO
(1.2 equiv) as a hydride acceptor in various solvents (1 M substrate
concentration) at 21 °C for 1 h, and the reaction solution was directly
subjected to purification by column chromatography on silica gel without
aqueous workup. c Isolated yield. d Stirred for 5 h.
(16) V catalyst: Maeda, Y.; Kakiuchi, N.; Matsumura, S.; Nishimura,
T.; Uemura, S. Tetrahedron Lett. 2001, 42, 8877.
(17) Co catalyst: Iwahama, T.; Yoshino, Y.; Keitoku, T.; Sakaguchi,
S.; Ishii, Y. J. Org. Chem. 2000, 65, 6502.
(18) Oppenauer, R. V. Rec. TraV. Chim. 1937, 56, 137.
2670
Org. Lett., Vol. 4, No. 16, 2002