catalyzed by RANEYs Ni catalyst. The byproduct was
ascribed to the product of benzene ring hydrogenation, which
was caused by the micropores of RANEYs Ni.8,35 The results
showed that the nickel nanoparticles had higher catalytic
activity and selectivity than RANEYs Ni catalyst in the
hydrogenation of p-nitrophenol to p-aminophenol.
Conclusions
In summary, nickel nanoparticles with different sizes and
different structures were prepared by reducing nickel oxalate
with hydrazine hydrate in the presence of organic modifiers,
such as PEG 200, PEG 6000, Tween 40, Tween 80, and sodium
dodecyl sulfonate, respectively. The ability of the organic
modifiers on decreasing particle size of nickel nanoparticles
is in an order of sodium dodecyl sulfonate (60 nm) 4 Tween
80 (178 nm) 4 PEG 6000 (184 nm) 4 PEG 200 (284 nm) 4
Tween 40 (297 nm). PEG 6000 caused the formation of nickel
nanoparticles with a twin crystal structure and point defects
while PEG 200 resulted in the formation of nickel nanoparticles
with point defects. When Tween 80 was used as an organic
modifier, the nickel nanoparticles with dislocations were formed.
The nickel nanoparticles with a relatively perfect internal struc-
ture were prepared in the presence of Tween 40 as an organic
modifier. When sodium dodecyl sulfonate was used as an
organic modifier, nickel nanoparticles with dislocations were
formed. The catalytic activity of the nickel nanoparticles in the
hydrogenation of p-nitrophenol to p-aminophenol generally
increased with decreasing their sizes. However, the catalytic
activity of nickel nanoparticles depended not only on the size
but also on the crystal structure. All the resultant nickel
nanoparticles showed higher catalytic activity and selectivity
than the RANEYs Ni catalyst.
Fig. 5 Catalytic activities of the nickel nanoparticles prepared by
reducing nickel oxalate with hydrazine hydrate in the presence of (’)
PEG 200, (K) PEG 6000, (m) Tween 40, (.) Tween 80, and (E)
sodium dodecyl sulfonate as organic modifiers, respectively, and the
(&) RANEYs Ni catalyst in the hydrogenation of p-nitrophenol to
p-aminophenol.
nanoparticles were 5.63, 4.40, 3.72, 3.20, and 1.01 molnitrophenol
/
molcatÁh, and the p-nitrophenol conversions were 80.1%,
62.6%, 52.9%, 45.5%, and 14.4% (Table 1) while the nickel
nanoparticles were prepared by using sodium dodecyl sulfonate,
Tween 80, PEG 6000, PEG 200, and Tween 40 as organic
modifiers, respectively. After reaction for 8 h, the conversions
of p-nitrophenol were up to 97%, 97%, 98%, 97%, and 80%,
respectively. By comparing the initial p-nitrophenol hydro-
genation rates at the first 2 h, it was found that the catalytic
activities of the nickel nanoparticles were in an order of
sodium dodecyl sulfonate (60 nm) 4 Tween 80 (178 nm) 4
PEG 6000 (184 nm) 4 PEG 200 (284 nm) c Tween 40
(297 nm). The catalytic activity of the nickel nanoparticles
generally increased with decreasing their sizes.
Acknowledgements
The authors would like to thank Professor K. Chen (Jiangsu
University) for supporting TEM and HRTEM measurements
of nickel samples. This work was financially supported by
research funds from Jiangsu Province Education Bureau
(1221310008) and Zhenjiang Science and Technology Bureau
(GJ2006006) and Jiangsu University (1281310001).
Interestingly, although the nickel nanoparticles prepared by
using PEG 200 and Tween 40 as organic modifiers had
comparable average particle sizes, the catalytic activity of
the former was ca. 3.2 times higher than that of the later. As
certified by HRTEM analysis, the nickel nanoparticles prepared
by using PEG 200 as an organic modifier had point defects.
However, when Tween 40 was used as an organic modifier, the
as-prepared nickel nanoparticles had a comparatively perfect
internal structure. It can be concluded that the catalytic
activity of the nickel nanoparticles depends on the synergistic
effect of the crystal structure and the size.
References
1 M. Pinza, M. Brufani and C. Milanese, US Pat., 6 043 285, 2000.
2 L. Chassot and H. J. Braun, US Pat., 6 592 631 B2, 2003.
3 F. Faranda, US Pat., 5 998 110, 1999.
4 C. V. Rode, M. J. Vaidya and R. V. Chaudhari, Org. Process Res.
Dev., 1999, 3, 465–470.
5 C. V. Rode, M. J. Vaidya, R. Jaganathan and R. V. Chaudhari,
Chem. Eng. Sci., 2001, 56, 1299–1304.
6 M. J. Vaidya, S. M. Kulkarni and R. V. Chaudhari, Org. Process
Res. Dev., 2003, 7, 202–208.
7 H. Lu, H. Yin, Y. Liu, T. Jiang and L. Yu, Catal. Commun., 2008,
10, 313–316.
8 Y. Du, H. Chen, R. Chen and N. Xu, Appl. Catal., A, 2004, 277,
259–264.
9 R. Chen, Q. Wang, Y. Du, W. Xing and N. Xu, Chem. Eng. J.,
2009, 145, 371–376.
10 R. Chen, Y. Du, Q. Wang, W. Xing, W. Jin and N. Xu, Ind. Eng.
Chem. Res., 2009, 48, 6600–6607.
To compare the catalytic activities of the as-prepared nickel
nanoparticles with that of RANEYs Ni catalyst, the catalytic
activity of RANEYs Ni catalyst was also investigated. The
initial p-nitrophenol hydrogenation rate of RANEYs Ni
catalyst was 0.64 molnitrophenol/molcatÁh after the first 2 h. After
reaction for 8 h, the conversion of p-nitrophenol was only 49%
(Fig. 5). The initial p-nitrophenol hydrogenation rate of the
nickel nanoparticles was 1.6–8.8 times higher than that of
RANEYs Ni catalyst. On the other hand, there was a
byproduct produced and the selectivity of p-aminophenol
was less than 95% while p-nitrophenol hydrogenation was
ꢀc
This journal is The Royal Society of Chemistry and the Centre National de la Recherche Scientifique 2010
712 | New J. Chem., 2010, 34, 708–713