At high oxidant/substrate ratios, the reaction yields
mainly cyclohexanone (apparently via further oxidation
of the initially formed cyclohexanol), which requires two
molecules of H O per one substrate molecule.
Table 1. Cyclohexane Oxidation with H O in the Presence of
2
2
a
1ꢀ3
2
2
1
2
3
Adamantane oxidation occurs predominately at more
b
electron-rich tertiary CꢀH groups (3°/2° values of
conversion, %
84
68
72
1
1
c
A/K
5.0
144
4.9
116
5.1
124
40ꢀ49), despite a 3-fold statistical prevalence of second-
ary CꢀH groups, yielding 1-adamantanol as the main
product (2-adamantanol and 2-adamantanone are the
major and minor byproduct, respectively).
d
TN
a
Reaction conditions: solvent: 0.4 mL of CH
AcOH, [cyclohexane]/[H O ]/[catalyst] = 400:20:0.1 μmol; 0 °C, oxi-
2 2
dant added by syringe pump over 1 h, and reaction mixture stirred for
3
CN þ 0.08 mL of
To probe the electronic effects on the oxidation site
selectivity, in particular the influence of electron-with-
drawing groups, the oxidation of substrates 4ꢀ6 contain-
ing different substituents at the same position has been
performed (Table 3). While the oxidation of 2,6-dimethy-
loctane yields an equimolar mixture of ‘remote’ and ‘prox-
imal’ oxidation products, introduction of electron accep-
tors substantially deactivates the proximal tertiary CꢀH
group. In the case of 6, the observed remote/proximal ratio
varies from 34:1 up to 97:1; to the best of our knowledge,
these values are the highest reported for nonheme metal
b
additional 1 h. Based on the oxidant, calculated as 100% ꢁ (alcohol þ 2
c
d
2 2 0
ketone)/[H O ] . Alcohol/ketone ratio. Turnover number, mol of
products (A þ K) per mol of catalyst.
Table 2. Catalytic Oxidation of Cyclohexane and Adamantane
with H
a
2
O
2
in the Presence of 1ꢀ3
yield of products, %
conversion,
3°d/
2°
ketone/
alcohol
3
b,c
catalysts. The oxidation of tertiary CꢀH groups in the
substrate
catalyst
%
presence of catalysts 1ꢀ3 is highly sensitive to the steric
environment: (ꢀ)-acetoxy-p-menthane 7 yields predomi-
nately product 8 with all catalysts (Table 4). Complex 2
demonstrates an unprecedented selectivity for 8 over 9
cyclohexane
cyclohexane
cyclohexane
1
2
3
77.8 (778)
87.0 (870)
80.0 (800)
ꢀ
ꢀ
ꢀ
71.7:6.1
84.2:2.8
75.0:5.0
conversion,
3°d/
2°
1-ol/2-ol/
2-one
(
57:1 at 0 °C; at ꢀ10 °C, 8 is formed as the only detectable
b,c
substrate
catalyst
%
product).
To test the scalability of the CꢀH oxidations, larger-
adamantane
adamantane
adamantane
1
2
3
10.3 (103)
70.6 (706)
36.2 (362)
48
40
49
9.7:0.6:ꢀ
65.7:3.2:1.7
34.1:2.1:ꢀ
scale oxidation of substrates 5, 6, and 7 in the presence of
e
a
Reaction conditions: [Cyclohexane]/[H
CN þ 0.08 mL of AcOH, oxidant added
by syringe pump over 1 h, and reaction mixture stirred for additional 1 h.
Adamantane]/[H
]/[catalyst] = 100:130:0.1 μmol, 0 °C, solvent: 0.8 mL of
CH Cl þ 0.16 mL of AcOH, oxidant added by syringe
CN þ 0.6 mL of CH
2 2
O ]/[catalyst] = 100:250:0.1
μmol, 0 °C, solvent: 0.4 mL of CH
3
a
Table 3. Catalytic Oxidation of Substrates 4ꢀ6
[
2 2
O
yield of products, %
3
2
2
pump over 30 min, and reaction mixture stirred for additional 5.5 h.
b
c
Conversion based on the substrate. Turnover number given in parentheses,
remote/
b,c
d
substrate catalyst conversion, %
remote proximal proximal
in mol of products per mol of catalyst. 3°/2° = 3 ꢁ [1-adamantanol]/
e
(
[2-adamantanol] þ [2-adamantanone]). Oxidant added over 2 h.
4
4
4
1
2
3
63.5 (635)
68.8 (688)
57.8 (578)
31.8
34.4
28.9
31.8
34.4
28.9
1:1
1:1
1:1
Cyclohexane is one of the most widely used ‘test sub-
strates’ for catalyzed CꢀH oxidations, since it enables free-
radical-driven oxidation to be readily distinguished from
the metal-based one: in the former case, the observed cyclo-
hexanol/cyclohexanone ratio is expected to be close to 1.0,
while, in the latter one, it should be substantially higher than
5
5
5
1
2
3
49.1 (491)
53.4 (534)
44.0 (440)
43.1
46.6
37.6
6.0
6.9
6.4
7:1
7:1
6:1
6
6
6
1
2
3
67.7 (677)
74.1 (741)
44.5 (445)
56.2
67.6
43.5
1.5
37:1
34:1
97:1
10
2.0
1. The results of the cyclohexane oxidation (Scheme 1) are
0.45
presented in Table 1. For all catalysts, the A/K ≈ 5 (clearly
indicative of metal-based oxidant) values are the highest ever
reported for nonheme manganese catalyzed cyclohexane
a
Reaction conditions: solvent: 0.4 mL of CH
AcOH, oxidant added by syringe pump over 30 min, and reaction
mixture stirred for additional 2.5 h, [alkane]/[H O ]/[catalyst] =
100:130:0.1 μmol, 0 °C. Conversion based on the substrate. Turnover
number given in parentheses, in mol of products per mol of catalyst.
3
CN þ 0.08 mL of
3
k
2
2
oxidations with H O . Under these model conditions
2
2
b
c
(
catalytic turnovers, which is already higher than that for most
[H O ] , [substrate], Table 1), 1ꢀ3 performed 115ꢀ144
2
2
3
,9
of the related iron-based catalysts. Under practical condi-
tions ([H O ] g [substrate]), the catalytic efficiencies are even
more impressive, up to a TON of 870 (Table 2).
catalyst 2 were carried out (Supporting Information); after
column chromatography separation, the isolated yields of
major oxidation products were 49, 52, and 66%, which is
2
2
(
10) (a) Tanase, S.; Bowman, E. In Advances in Inorganic Chemistry,
Vol. 58; van Eldik, R., Reedijk, J., Eds.; Academic Press: 2006; p 29.
b) Costas, M.; Chen, K.; Que, L., Jr. Coord. Chem. Rev. 2000, 200ꢀ202, 517.
(11) These 3°/2° selectivities are among the highest reported for
nonheme Fe and Mn catalysts (up to 48); see refs 10a, 10b.
(
Org. Lett., Vol. XX, No. XX, XXXX
C