Full Papers
conditions. From these results, it can be concluded that the
rGO/Au ratio had a significant effect on the catalytic activity of
the nanocomposite (Table S4, in the Supporting Information).
for the reaction and gave unfruitful results. Au NPs synthesized
by using only pDA as a reducing and stabilizing agent in the
absence of GO (Au–pDA) showed much lower catalytic activity
compared with Au–pDA–rGO (Table 2, entry 20). TEM images
of the Au–pDA composite showed the formation of agglomer-
ated nanoparticles with an average particle size of approxi-
mately 20 nm (Figure S8, in the Supporting Information).
Hence, the deposition of pDA on GO was crucial for controlling
the size of the Au NPs in the composite. On the other hand,
the Au–rGO composite without pDA (synthesized by using
Optimization and scope of reaction
To optimize the reaction conditions to obtain high conversion
and selectivity for the CÀH oxidations, we performed several
controlled experiments by using diphenylmethane as a model
substrate (Table 2). The Au–pDA–rGO nanocomposite did not
afford high conversion in the presence of molecular oxygen as
the single oxidant, even at elevated temperature. Therefore, it
was necessary to look for a secondary oxidant to facilitate
higher conversion. Addition of commonly available oxidants
such as H O or tert-butylhydroperoxide (TBHP) to the reaction
NaBH as the reducing agent) afforded only 38% yield of the
4
desired product under the optimized reaction conditions. It is
well known that several other supports such as polyvinyl pyr-
rolidone (PVP), activated carbon, and metal oxides such as TiO2
and CeO are often used for anchoring nanoparticles. To gain
2
2
2
mixture afforded moderate yields of the desired product di-
phenylketone along with the formation of several byproducts.
However, in combination with NHPI, Au–pDA–rGO afforded
high conversion and selectivity under mild reaction conditions
a better insight into the catalytic efficacy of the Au–pDA–rGO
nanocomposites, we performed the catalytic studies with Au–
PVP, Au–C, Au–TiO , and Au–CeO nanocomposites in the pres-
2
2
ence of NHPI. When using Au–PVP as a catalyst under the stan-
dard reaction conditions, the conversion was moderate and
the selectivity was poor as several other byproducts, including
diphenylmethanol and benzoic acid, were observed. Further,
the nanoparticles were agglomerated after just one cycle of
the reaction. Au NPs stabilized with activated carbon (Au–C)
did not afford higher yields of the oxidized product. In the
case of Au–TiO or Au–CeO as the catalyst in the presence of
(
608C). Use of 10 mol% of NHPI was found to be optimum for
our catalytic reaction (Table 2, entries 9–11). Among the sol-
vents, CH CN was found to be most suitable for the reaction,
3
as other solvents such as water, acetone, and DMSO only af-
forded low yields. Further, increasing the reaction temperature
from 258C to 608C resulted in tremendous enhancement in
conversion (Table 2, entries 8 and 11). Further increases in tem-
perature, however, led to a decrease in conversion and selec-
tivity (Table 2, entry 12). To evaluate the role of the individual
constituents in the ternary composite, several controlled ex-
periments were performed under the standard reaction condi-
tions. NHPI, GO, pDA or combinations of them were inefficient
2
2
NHPI, the oxidized products were obtained with moderate
yields at 608C (Table 2, entries 18 and 19), however, better con-
version was observed at elevated temperature (Table S5, in the
Supporting Information). From these studies, it was apparent
that Au–pDA–rGO exhibited the best catalytic activity when
coupled with NHPI, resulting in successful oxidation
[
a]
of diphenylmethane with 92% conversion and 97%
Table 2. Optimization of reaction conditions.
selectivity to diphenylketone in 12 h under mild con-
Entry Catalyst
Additive
mol%]
Reaction
conditions
Conversion
[%]
Selectivity
[%]
ditions.
The scope of the oxidation reactions was surveyed
[
b[b]
1
2
3
4
5
6
7
8
9
1
Au–rGO
NHPI (10) CH
3
CN, 608C, 12 h
CN, 608C, 24 h
38.1
22.8
24.4
38.2
41.2
61.3
52.5
49.4
74.2
92.5
96.6
98.5
100
82.8
81
79.3
80.9
98
98.9
97.8
97.4
89.6
87.8
96.7
99
by using Au–pDA–rGO as the catalyst in the pres-
ence of NHPI to catalyze oxygenations of various hy-
drocarbons under the same conditions except for
the reaction time (Table 3). In general, the CÀH bond
oxidation of benzylic compounds occurred smoothly
under mild conditions to give ketone products. For
example, tetralin was oxygenated with high conver-
sion and selectivity to tetralone with 85% yield.
Indan, fluorene, and xanthene were oxidized with
good conversions (80–90%, Table 3, entries 2, 4, and
Au–pDA–rGO
Au–pDA–rGO
Au–pDA–rGO
Au–pDA–rGO
Au–pDA–rGO TBHP (10) CH
Au–pDA–rGO TBHP (5) CH
Au–pDA–rGO NHPI (10) CH
–
K
CH
3
2
3
CO (10) water, 708C, 24 h
H
H
2
O
O
2
(10) CH
(15) CH
3
CN, 608C, 12 h
3
CN, 608C, 12 h
3
CN, 608C, 12 h
3
CN, 608C, 12 h
3
CN, 258C, 12 h
3
CN, 608C, 12 h
3
CN, 608C, 12 h
3
CN, 608C, 12 h
3
CN, 808C, 12 h
2
2
Au–pDA–rGO NHPI (5)
CH
0
Au–pDA–rGO NHPI (15) CH
Au–pDA–rGO NHPI (10) CH
Au–pDA–rGO NHPI (10) CH
Au–pDA–rGO NHPI (10) water, 808C, 12 h
Au–pDA–rGO NHPI (10) acetone, 608C, 12 h 45.6
Au–pDA–rGO NHPI (10) DMSO, 608C, 24 h
Au–PVP
Au–C
[
c]
[d]
[e]
1
1
92, 52 , 65 , 93
1
1
1
1
1
1
1
1
2
2
3
4
5
6
7
8
9
0
90.7
25.1
9
). An exception was the case of 9,10-dihydroanthra-
<1.0
34.0
22.1
48.8
43.6
12
cene, where the dehydrogenation product was fa-
vored over the oxidation product (Table 3, entry 8).
In the case of toluene, the major oxidation product
was benzoic acid, probably because aldehydes are
known to be a radical initiator for NHPI-based oxy-
genations and are not stable in such radical reactions
NHPI (10) CH
NHPI (10) CH
NHPI (10) CH
NHPI (10) CH
NHPI (10) CH
3
CN, 608C, 12 h
3
CN, 608C, 12 h
3
CN, 608C, 15 h
3
CN, 608C, 14 h
3
CN, 608C, 12 h
87.5
100
97
95
Au–TiO
2
Au–CeO
Au–pDA
2
96.8
[
a] Reaction conditions: Unless otherwise specified, all the reactions were carried out
[
19]
(
Table 3, entry 10).
The oxidation of cyclohexane
with diphenylmethane (1.0 mmol); Au nanoparticle composite 0.02 g (Au loading
2
1
wt%); additive (5–15 mol%); under magnetic stirring; solvent 5 mL; O
2
pressure
was found to be sluggish, resulting in very low con-
version under similar reaction conditions (Table 3,
entry 11).
b
3+
0 bar; stirring rate 1000 rpm. [b] Au–rGO =GO and Au
reduced by NaBH .
4
[
c,d,e] Au–pDA–rGO catalyst amount was 0.01, 0.015, and 0.03 g, respectively.
ChemCatChem 2016, 8, 1825 – 1835
1829
ꢀ 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim