Please do not adjust margins
RSC Advances
Page 3 of 5
DOI: 10.1039/C6RA19170C
Journal Name
COMMUNICATION
Fig. 3 Catalytic conversion of OPD to 2,3ꢀDPA over CysꢀFe3O4 MNPs, MILꢀ
101(Fe) and Fe3O4/MILꢀ101(Fe), respectively.
Fig. 4 The productivity of 2,3ꢀDPA using Fe3O4/MILꢀ101(Fe) as catalyst
after five consecutive reaction.
Similar to peroxidase, the catalytic activity of Fe3O4/MILꢀ
101(Fe) was found to be closely dependent on pH, temperature,
H2O2 concentration,and so on. Therefore, the reaction conditions,
such as the concentration of H2O2 and Fe3O4/MILꢀ101(Fe), pH,
temperature, and reaction time, have been optimized (Fig. S7).
Under the optimal reaction conditions, the Fe3O4/MILꢀ101(Fe)
displayed a higher catalytic activity than that of CysꢀFe3O4 MNPs
and MILꢀ101(Fe), achieving 97.79% yield of 2,3ꢀDPA(Fig. S8).
Compared with other existing catalyst (Table S1), the asꢀsynthesized
Fe3O4/MILꢀ101(Fe) shows highest catalytic efficiency among the
reported catalyst for the oxidation of OPD. For the product 2,3ꢀDPA
(structure displayed in Fig. S9), the characterization data of FTIR,
1H NMR, 13C NMR and ESIꢀTOFMS are showed in Fig. S10ꢀ13,
respectively.
From the results shown above, one can easily draw a conclusion
that the catalytic activity of Fe3O4/MILꢀ101(Fe) is higher than those
of CysꢀFe3O4MNPs and MILꢀ101(Fe) for the same reaction time.
This catalytic activity enhancement can be attributed to the
synergistic effect of CysꢀFe3O4MNPs and MILꢀ101(Fe).
Furthermore, the recyclability of the Fe3O4/MILꢀ101(Fe) catalyst
was also examined in the dimerization reaction of OPD. The catalyst
was isolated by magnetic separation from the reaction mixture and
washed with methanol, and reused for the next run under the same
conditions. The results indicated that no significant loss of activity
for the dimerization reaction of OPD was observed over Fe3O4/MILꢀ
101(Fe) in the five successive catalytic cycles, suggesting that the
Fe3O4/MILꢀ101(Fe) possesses longꢀterm stability (Fig. 4). The
atomic absorption spectrometry (AAS) has been used for monitoring
the leaching test. The total iron content which leached from the
composite would have a relatively high leaching quantity in the firstꢀ
time using. The highest leaching amount is 1.153 ng/mL. The
leaching amount dropped dramatically with the increase of cycling
times, and even no iron was detected after three cycles (Fig.S14).
However, the catalytic efficiency of the composite is still maintained
at a high level. It indicates that the catalytic activity is mainly
derived from the composite material rather than the leached iron ion.
After five recycling use, the PXRD pattern showed that the used
Fe3O4/MILꢀ101(Fe) keeps close to the originality (Fig. S15). As can
be seen from the Xꢀray photoelectron spectroscopy (XPS) spectrums
(Fig.S16), there were no changes between the fresh and recovered
Fe3O4/MILꢀ101(Fe). It indicates that the composite remains the
integrity without any valence state change before and after the
reaction. Besides, the morphology of Fe3O4/MILꢀ101(Fe) has no
serious changes and no great influence upon the catalytic activity
after five consecutive reaction cycles (Fig. S17).
In summary, we have developed a facile, general and effective
ultrasoundꢀassisted electrostatic selfꢀassembly strategy for
immobilizing Fe3O4 MNPs on the surface of MILꢀ101(Fe). The
catalytic property of Fe3O4/MILꢀ101(Fe) was evaluated by using the
dimerization reaction of OPD as a model reaction system. It is
noteworthy that the asꢀprepared Fe3O4/MILꢀ101(Fe) composite
synergistically improves the catalytic activity compared to the Cysꢀ
Fe3O4 and MILꢀ101(Fe). Furthermore, the high catalytic activity was
retained after a number of reaction cycles with a slightly change.
This study may bring light to new opportunities in the development
of high performance heterogeneous catalysts based on the
peroxidaseꢀlike activity of Feꢀbased MOFs or nanostructures.
The authors gratefully acknowledge thank the financial support
of the National Natural Science Foundation of China (NSFC, No.
21175109).
Notes and references
1. W. G. Lu, Z. W. Wei, Z. Y. Gu, T. F. Liu, J. Park, J. Park, J. Tian,
M. W. Zhang, Q. Zhang, T. Gentle Iii, M. Bosch and H. C. Zhou,
Chem. Soc. Rev., 2014, 43, 5561ꢀ5593.
2. (a) G. Férey, Chem.Soc.Rev., 2008, 37, 191ꢀ214; (b) Z. Y. Gu, C.
X. Yang, N. Chang and X. P. Yan, Accounts Chem Res, 2012, 45,
734ꢀ745; (c) N. Chang, Z.ꢀY. Gu and X.ꢀP. Yan, J. Am. Chem.
Soc., 2010, 132, 13645ꢀ13647; (d) J. J. GutiérrezꢀSevillano, A.
MartínꢀCalvo, D. Dubbeldam, S. Calero and S. Hamad, RSC Adv.,
2013, 3, 14737.
3. (a) D. Wang, L. Sun, C. Hao, Y. Yan and Z. Liang, RSC Adv.,
2016, 6, 57828ꢀ57834; (b) B. Ding, C. Guo, S. X. Liu, Y. Cheng,
X. X. Wu, X. M. Su, Y. Y. Liu and Y. Li, RSC Adv., 2016, 6,
33888ꢀ33900; (c) J. F. Guo, R. M. Fang, C. Z. Huang and Y. F.
Li, RSC Adv., 2015, 5, 46301ꢀ46306.
4. (a) P. Horcajada, T. Baati, J. F. Eubank, D. Heurtaux, P. Clayette,
C. Kreuz, J.ꢀS. Chang, Y. KyuHwang, V. Marsaud, P.ꢀN. Bories,
L. Cynober, S. Gil, G. Férey, P. C. a. R. Gref, T. Chalati, C. Serre,
B. Gillet and C. Sebrie, Nat.Mater., 2010, 9, 172ꢀ178; (b) J.
Zhuang, C.ꢀH. Kuo, L.ꢀY. Chou, D.ꢀY. Liu, E. Weerapana and C.ꢀ
K. Tsung, ACS Nano, 2014, 8, 2812ꢀ2819.
5. (a) H. T. H. Nguyen, O. T. K. Nguyen, T. Truong and N. T. S.
Phan, RSC Adv., 2016, 6, 36039ꢀ36049; (b) A. R. Oveisi, A.
Khorramabadiꢀzad and S. Daliran, RSC Adv., 2016, 6, 1136ꢀ1142;
(c) K. Huang, Y. Xu, L. Wang and D. Wu, RSC Adv., 2015, 5,
32795ꢀ32803; (d) S. Beheshti and A. Morsali, RSC Adv., 2014, 4,
41825ꢀ41830.
6. (a) D. Wang, R. Huang, W. Liu, D. Sun and Z. Li, ACS Catal.,
2014, 4, 4254ꢀ4260; (b) K. G. Laurier, F. Vermoortele, R.
Ameloot, D. E. De Vos, J. Hofkens and M. B. Roeffaers, J. Am.
This journal is © The Royal Society of Chemistry 20xx
J. Name., 2013, 00, 1-3 | 3
Please do not adjust margins