Full Paper
troarenes. The chemoselective reduction of nitro to amino
groups is a key process in organic synthesis. For instance,
amino groups can serve as reactive sites for further derivatiza-
tion to produce pharmaceuticals, agrochemicals, and bioactive
compounds.[22] Initially, we optimized the catalytic conditions
by studying the reduction of 4-nitroaniline (1) with different re-
ducing agents and solvents (Supporting Information, Table S1,
entries 1–9). Among the examined conditions, g-Fe2O3-MNAs
catalyst (10 mol% based on 1) with four equivalents of methyl
hydrazine (MeNHNH2) in ethanol afforded 53% conversion of
1 to 4-aminoaniline (1a) in 1 h (Supporting Information,
Table S1, entry 5).[23] No byproducts such as azoxy-, azo-, or 1,2-
diarylhydrazine were detected during the reaction progress by
The present catalyst system could efficiently promote the
synthesis of aryl amines from various substituted nitroarenes. It
was found that the mesoporous g-Fe2O3-MNAs catalyze the re-
duction of nitroarenes 2–13 almost quantitatively to their cor-
responding aryl amines 2a–13a (>94% yields; see Scheme 2).
1
means of H NMR spectroscopy. In stark contrast, no reduction
of 1 was observed under mild hydrogenation with H2 (1 atm)
or other transfer hydrogenation reagents such as hydrosilanes
(1,1,3,3-tetramethyldisiloxane and dimethylphenylsilane) and
boranes (NaBH4 and NH3BH3) (Supporting Information,
Table S1, entries 6–9). In the absence of catalyst no appreciable
reduction of 1 takes place; that is, the reduction process is cat-
alytic in nature. For comparison, use of commercially obtained
iron compounds and bulk g-Fe2O3 solid as catalysts led to neg-
ligible conversions to 1a (Supporting Information, Table S1, en-
tries 10–14), even over a four-hour reaction period. Also,
random g-Fe2O3 aggregates (g-Fe2O3-RNAs) and mesoporous
assemblies from a-Fe2O3 (a-Fe2O3-MNAs) and Fe3O4 (Fe3O4-
MNAs) NPs resulted in lower conversions of 1 (Supporting In-
formation, Table S1, entries 15–17). These results clearly sug-
gest that the high catalytic activity of g-Fe2O3-MNAs is related
not only to the large pore volume being accessible to reac-
tants but also to the crystal phase of the iron oxide NPs, which
provide active facets and edge sites for the reaction.[7b] We fur-
ther found that a small addition of water significantly im-
proved the reactivity of g-Fe2O3-MNAs (see Supporting Infor-
mation, Figure S5 and Table S1, entries 18–20). Presumably,
under these reaction conditions, the nitro groups are protonat-
ed to give more electrophilic substrates[24] that bind in the H
sites of the catalysts (see below), although further studies are
needed to ascertain this effect.
Scheme 2. Reduction of various aryl and alkyl nitro compounds by g-Fe2O3-
MNAs catalyst. The percentages correspond to the yields of isolated prod-
ucts. In parentheses: the corresponding yields of isolated products with hy-
drazine as reducing agent.
Notably, nitroarenes containing additional reducible groups,
such as halo [chloro (5) and bromo (6)], methyl carboxylate (7),
cyano (8), and carbonyl (12), were selectively reduced to the
target amines. Similarly, the reaction process was found to be
inactive towards other easily reducible groups such as lactone
(11) and vinyl (13) substituents under the present catalytic
conditions. In addition, the same reductions were also per-
formed by using hydrazine as reducing agent, which gave sim-
ilar product yields at certain reaction times (Scheme 2, values
in parentheses). These results clearly support the high propen-
sity of the g-Fe2O3-MNAs catalyst to selectively reduce nitroar-
enes to aryl amines. Remarkably, the g-Fe2O3-MNAs could also
catalyze reduction of nitroalkanes 14–17, which do not readily
react,[25] to give the corresponding oximes 14b–17b as the
only products, albeit in lower yields (73–89%), and with an
eightfold excess of MeNHNH2 (Scheme 2). Currently, NPs of
precious metals such as Rh, Ni, Pd, and Au[24b,26] are regarded
as the state-of-the-art catalysts for reduction of aromatic nitro
compounds with hydrazine. However, the high cost and poor
durability (they are moisture-sensitive) of these nanomaterials
pose significant limitations to large-scale application. The iron
oxide assemblies described herein can be considered to be
highly effective, stable (even in water), and inexpensive alter-
native catalysts for widespread use in amine production. To
the best of our knowledge, only one example of an g-Fe2O3-
based catalyst exhibits similarly high catalytic activity to our
material, but it requires an excess of hydrazine and harsh con-
ditions (858C).[7b]
Owing to the 3D structure and magnetic susceptibility of
the g-Fe2O3-MNAs, this catalyst could be readily recycled by
simple filtration or by using an external magnetic field. As
shown in Figure S6 of the Supporting Information, the catalyst
reaches an almost constant activity, giving as high as 99% con-
version to 1a in 2 h even after seven consecutive runs. N2
sorption isotherms of the reused sample show no obvious
changes in the surface area and pore volume (162 m2 gÀ1 and
0.19 cm3 gÀ1; Figure S7, Supporting Information), reflecting ex-
cellent durability and recyclability. Given these encouraging re-
sults, the g-Fe2O3-MNAs catalyst was also tested for possible
large-scale production of anilines from nitroarenes. In particu-
lar, 3.6 mmol of 1 was reduced in the presence of g-Fe2O3-
MNAs (4 mol%) with MeNHNH2 (6 equiv) in MeOH (10 mL).
After completion of the reaction (ꢀ9 h based on TLC analysis),
the catalyst was magnetically separated from the mixture and
the corresponding aniline 1a was purified by column chroma-
tography and isolated in 91% yield.
Chem. Eur. J. 2016, 22, 4600 – 4607
4604
ꢀ 2016 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim