Chemistry Letters Vol.36, No.6 (2007)
749
ly efficient NiII-catalyst for the alkane hydroxylation reaction
with m-CPBA using diphenol ligand L2H2. Optimization of
the reaction conditions as well as characterization of the active
oxygen species is now under investigation.
1000
2
800
1
600
400
200
0
This work was financially supported in part by Grants-
in-Aid for Scientific Research (Nos. 17350086, 18037062, and
18033045) from the Ministry of Education, Culture, Sports,
Science and Technology, Japan.
3
References and Notes
b) D. T. Sawyer, A. Sobkowiak, T. Matsushita, Acc. Chem.
1
0
30
60
90
120
Time / min.
´
Figure 2. Time courses for the oxidation of cyclohexane
(2.5 M) with m-CPBA (0.33 M) catalyzed by 1 ( ), 2 ( ), and
3 ( ) (0.33 mM) in CH2Cl2/CH3CN (v/v = 3/1, total 6 mL)
at room temperature.
f) P. Stavropoulos, R. Cꢀelenligil-Cꢀetin, A. E. Tapper, Acc.
J. Chem. Soc., Dalton Trans. 2002, 672. h) T. Punniyamurthy,
Oxo and Metal-Peroxo Species in Catalytic Oxidations, ed.
by B. Meunier, Springer, Berlin, 2000.
4047. b) T. Higuchi, K. Shimada, N. Maruyama, M. Hirobe,
d) J. B. Vincent, J. C. Huffman, G. Christou, Q. Li, M. A.
Nanny, D. N. Hendrickson, R. H. Fong, R. H. Fish, J. Am.
K. J. Oberhausen, R. H. Fong, W. M. Yu, G. Christou, J. B.
coordinate distorted square planer geometry with an N2O2 donor
set, in which two deprotonated phenolate oxygen atoms O(1) and
O(2), tertiary amine nitrogen N(1), and the imine nitrogen N(2)
of the TMG co-ligand are involved (Figure 1, right). Thus, one of
the phenol groups of the ligand is free from coordination.
Catalytic activity of the NiII-complexes was examined using
cyclohexane as the substrate and m-CPBA as the oxidant
(Scheme 1).9 Figure 2 shows the time courses of total turnover
number (TON) of the catalysts. In all the cases, cyclohexanol
was obtained as a major product together with a small amount
of cyclohexanone and a trace amount of over oxidation product
"-caprolactone. As reported previously, the monophenol com-
plex 1 acted as an efficient turnover catalyst to give total TON
as 719 and alcohol product selectivity (A/K; alcohol/ketone
ratio) as 7.2 after 2 h. When the diphenol complex 2 was
employed as the catalyst, the total TON and A/K values became
larger as 858 and 7.7, respectively, although the turnover rate at
the initial stage of the reaction (ca. 30 min) was little lower
(Figure 2).10 On the other hand, complex 3 exhibited relatively
low catalytic activity as compared to 1 and 2, whereas the
A/K value (65) of 3 was much higher than that of others.
Although the details of the catalytic mechanism have yet to
2
´
30, 3002. f) R. A. Leising, J. Kim, M. A. Perez, L. Que, Jr.,
Kaizer, E. J. Klinker, N. Y. Oh, J.-U. Rohde, W. J. Song, A.
a) W. Nam, I. Kim, Y. Kim, C. Kim, Chem. Commun. 2001,
1262. b) W. Nam, J. Y. Ryu, I. Kim, C. Kim, Tetrahedron
a) K. Jitsukawa, Y. Oka, S. Yamaguchi, H. Masuda, Inorg.
T. Nagataki, Y. Tachi, S. Itoh, Chem. Commun. 2006, 4016.
T. Nagataki, K. Ishii, Y. Tachi, S. Itoh, Dalton Trans. 2007,
1120.
Supporting Information (experimental procedures and X-ray
stractural determination) is available electronically on the
index.html. Crystallographic data of 2 and 3 have been depos-
ited with Cambridge Crystallographic Data Centre as supple-
mentary publication no. CCDC-640872 and -640873, respec-
tively.
¨
3
4
5
II
III
ꢀ
be clarified, we proposed that a nickel–oxo (Ni –O or Ni =O)
species is involved as a key reactive intermediate for the alkane-
hydroxylation.7,8 Introduction of the additional phenol group in-
to L1H to give L2H2 may enhance the durability of the catalyst.
Namely, self-degradation of the catalyst may be suppressed in 2,
allowing the high TON, even though the turnover rate became a
little lower (Figure 2). On the other hand, the triphenol ligand
L3H3 itself may not fit to the octahedral geometry, which is
required for the m-CPBA-binding to generate the nickel–oxo
species. Thus, 3 may exhibit the lower catalytic activity.
Nonetheless, significantly high alcohol selectivity (A/K = 65)
of 3 is noteworthy.
6
7
8
9
Another advantage of catalyst 2 is its high solubility to
non-polar organic solvent. Thus, the oxidation of cyclohexane
(15 mmol, 1.62 mL) with 2 (0.002 mmol) in the presence of
m-CPBA (0.4 mmol, suspended) can be carried out without
adding any other solvent to yield cyclohexanol in 93% together
with a small amount of cyclohexanone (7%) based on the
oxidant (the oxidant efficiency was 100%, A/K = 13.3).9
In summary, we have succeeded in developing a significant-
10 After a prolonged reaction time (24 h), the total TON reached
ca. 1000 and all the m-CPBA (0.33 M) was consumed. Thus,
the product yield based on the oxidant was ca. 100%, demon-
strating the high durability of the catalyst.