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dard mild conditions, no reduction of the aromatic ring was
observed (entry 3).
Table 1. Hydrogenation of olefinic compounds with Pd0@g-Fe2O3 nano-
catalyst in n-hexane or water.[a]
Secondly, the Pd0@g-Fe2O3 nanocatalyst was also studied in
the dehalogenation reactions of halogenoarenes under the
same conditions (100 kPa H2, RT). The results are reported in
Table 2. In a first set of experiments (Table 2, entries 1–4), the
influence of the solvent was studied. Whatever the solvent
was, good activities were achieved with the Pd0@g-Fe2O3 cata-
lyst for the transformation of chlorobenzene into benzene (en-
tries 1, 2), particularly with a TOF in n-hexane of approximately
400 hÀ1. However, the dehalogenation of 2-chloroanisole in n-
hexane (entry 3) led to poor conversion (13%) and destabiliza-
tion of the Pd0@g-Fe2O3 suspension. This result was attributed
to the production of chlorine species in the reaction mixture,
which acts as a poison towards the catalytic system, as already
reported.[48–49] The addition of chlorohydric acid hydrochloric
acid in the hydrogenation of 1-tetradecene in n-hexane after
5 min led to deactivation of the catalyst, with a 40% conver-
sion after 2 h, instead of a complete transformation under clas-
sical conditions (Table 1, entry 2). Moreover, the maghemite (g-
Fe2O3) support was totally inactive towards the dechlorination
reaction of 2-chloroanisole in water (Table 2, entry 5), with no
production of anisole after 24 h. In a second set of experi-
ments, the scope of the reaction was extended to other halo-
genoarenes in neat water (Table 2, entries 7–9). The reactivity
of bromobenzene is lower than of the chloroarenes (Table 2,
entry 7 vs. 2), as already reported.[49–51] This result could be ex-
plained by the lower electron affinity of Br (3.364 eV) than that
of Cl (3.615 eV), which results in a less effective activation of
the bromo reactant through surface s-complex formation. The
additional presence of a second chloro group (Cl or Br) on the
ring leads to a deactivating effect, lowering the halogenoarene
reactivity because the halogen substitution reduces the elec-
tron density associated with the ring carbons (entries 8–9).[51]
Thirdly, the reduction of nitroarenes into aniline was investi-
gated by using the Pd0@g-Fe2O3 nanocomposite under stan-
dard conditions (100 kPa H2, RT) in neat water (Table 3). As al-
ready observed in previous experiments, no reduction of the
nitro groups was observed with the g-Fe2O3 support (Table 3,
entry 2). However, the Pd0@g-Fe2O3 nanocomposite was active
towards the hydrogenation of nitrobenzene in neat water with
a TOF up to 150 hÀ1 (entry 1). Moreover, the tandem hydroge-
nation–dehalogenation reaction of 4-chloronitrobenzene was
Entry
Substrate
Product
TOF[b] [hÀ1
]
in n-hexane
in water
1
2
3
cyclohexene
1-tetradecene
styrene
cyclohexane
tetradecane
ethylbenzene
200
50
600
150
n.c.[c] (82%)
100
[a] Reaction conditions: catalyst Pd0@g-Fe2O3 (50 mg, 1% wt Pd, 4.6ꢂ
10À6 mol Pd), substrate (0.47 mmol), 100 kPa H2, 10 mL solvent, RT. [b] De-
termined by GC analysis and defined as the number of consumed H2 per
mole of introduced Pd per hour. [c] Not calculated; conversion deter-
mined by GC analysis shown in parentheses.
sults not only from the exposed surface metal atoms because
the surface can restructure, atoms can shift positions during
the heterogeneous processes and partial aggregation could
occur during catalysis, modifying the fraction of surface atoms.
These changes in the surface render the determination of the
number of surface atoms difficult. The results are gathered in
Table 1.
Notably, the bare g-Fe2O3 particles are not active towards
the reduction of unsaturated compounds. In contrast, the
Pd0@g-Fe2O3 nanocomposite presents remarkable activities to-
wards the hydrogenation of linear and cyclic olefins (Table 1,
entries 1–3) in both solvents. However, the catalytic system
was more active in n-hexane, with TOFs up to 600 hÀ1 for sty-
rene (entry 3). These results could be attributed to a better sol-
ubilization of the substrate and product in organic solvents,
and also to a better diffusion of the substrate towards the met-
allic surface, as already reported.[47] Concerning the 1-tetrade-
cene (entry 2), the kinetics are slower owing to the hydropho-
bic nature of the substrate and to the isomerization of the ter-
minal olefin, leading to the formation of more hindered olefins,
which are more difficult to reduce. Finally, under these stan-
Table 2. Dehalogenation of halogenoarenes with Pd0@g-Fe2O3 nano-
catalyst in n-hexane or water.[a]
Entry Substrate
Solvent
Product[b] [%] t [h] TOF[c] [hÀ1
]
1
2
3
4
5[e]
6
7
8
chlorobenzene
n-hexane benzene (98)
water
n-hexane anisole (13)
0.25 392
benzene (100) 1.5 67
Table 3. Hydrogenation of nitroarene derivatives into aniline with Pd0@g-
chlorobenzene
2-chloroanisole
2-chloroanisole
2-chloroanisole
4-chloroaniline
bromobenzene
Fe2O3 in water.[a]
0.5
2.2
24
n.c.[d]
water
water
water
water
anisole (100)
anisole (0)
aniline (100)
benzene (100)
45
–
Entry Substrate
Time [h] TOF[b] [hÀ1
]
3.1
2
32
50
18
22
1
nitrobenzene
nitrobenzene
4-chloronitrobenzene
nitrobenzene/4-chloronitrobenzene (1:1)
2
–
5
5
150
–
80
70
2[c]
3
1,2-dichlorobenzene water
2,4-dichloroanisole water
benzene (100) 5.7
anisole (100) 4.5
9
4
[a] Reaction conditions: catalyst Pd0@g-Fe2O3 (50 mg, 1% wt Pd, 4.6ꢂ
10À6 mol Pd), substrate (0.47 mmol), 100 kPa H2, 10 mL solvent, RT.
[b] Percentage of conversion determined by GC analysis. [c] Number of
consumed H2 per mole of introduced Pd per hour. [d] Not calculated.
[e] g-Fe2O3.
[a] Reaction conditions: catalyst Pd0@g-Fe2O3 (50 mg, 1% wt Pd, 4.6ꢂ
10À6 mol Pd), substrate (0.47 mmol), 100 kPa H2, 10 mL solvent, RT.
[b] TOF determined by GC analysis and defined as the number of con-
sumed H2 per mole of introduced Pd per hour. [c] Reaction performed
with g-Fe2O3 support.
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