G. Xiao et al.
Table 3 Comparison oꢀ the Fe O @GO with some reported catalysts ꢀor Baeyer–Villiger oxidation oꢀ ketones
3
4
Entry
Catalyst
Oxidant
Solvent
Temp. (°C)
Time (h)
Yield (%)
1
2
3
4
Mg–Al mixed oxide [29]
Sn exchanged hydrotalcites [24]
Sn-supported on clay [39]
Fe O @GO
H O
1,4-Dioxane
Acetonitrile
1,2-Dichloroethane
Solvent ꢀree
70
70
12
4
2
89
58
93
84
2
2
2
2
2
H O
2
H O
Reꢃuxing temperature
Room temperature
2
H O
5
3
4
2
When the ortho-position was electron donating group, the
selectivity oꢀ product was higher than the one with electron-
withdrawing group (entry 1, 3, 4). Particularly, adamantane
ketone had a perꢀect conversion with an excellent yield
4 Conclusions
A novel catalyst oꢀ magnetic nanocomposite Fe O @GO
3
4
was prepared which showed high catalytic activity ꢀor
Baeyer–Villiger oxidation in hydrogen peroxide. Yield
oꢀ 2-methyl cyclohexanone being 84% with selectivity oꢀ
94% was obtained in a small-scale experiment (2 mmol oꢀ
2-methyl cyclohexanone). The optimum reaction condi-
tions were ꢀound to be as ꢀollows: molar ratio oꢀ hydrogen
peroxide and 2-methyl cyclohexanone was 6:1, dosage oꢀ
Fe O @GO was 0.02 g, room temperature, solvent ꢀree,
(
entry 5). On the contrary, the product oꢀ chain ketone was
obtained hardly (entry 6).
The recyclability oꢀ the catalyst was investigated in the
oxidation oꢀ cyclohexanone. The catalyst was separated ꢀrom
the reaction mixture simply because oꢀ its magnetic property,
and the recovered catalyst was washed with acetone, dried
in a desiccator and reused directly ꢀor another run without
3
4
ꢀ
urther puriꢁcation. The recyclability results clearly indicate
reaction time oꢀ 5 h. The catalyst was magnetically reused
and recycled ꢀor several runs with a little loss oꢀ efciency
and selectivity.
that the catalyst remained active without any signiꢁcant loss
in efciency (entry 3, 5). A ꢁltration test was carried out
in order to check whether any loss oꢀ nanoparticles Fe O
3
4
during the reaction. The reaction was allowed to run ꢀor 2 h,
then the catalyst was separated ꢀrom the reaction mixture,
then it was allowed to run without the catalyst ꢀor next 3 h.
It was ꢀound that the conversion aꢀter the ꢁrst 2 h, the con-
version oꢀ 2-methyl cyclohexanone is 63%. Until the end oꢀ
the reaction aꢀter separation oꢀ the catalyst, the conversion
remained unchanged. This conꢁrms that no leaching oꢀ any
active species oꢀ the catalyst in the reaction process.
Compliance with Ethical Standards
Conflict of interest There are no conꢃicts to declare.
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