Songfang Zhaoa,
Yongju Gaoab,
Jinhui Lia,
Guoping Zhang*a,
Rong Sun*a and
Ching-Ping Wongcd
aShenzhen Institutes of Advanced Technology, Chinese Academy of Sciences, Shenzhen 518055, China. E-mail: gp.zhang@siat.ac.cn; rong.sun@siat.ac.cn
bNano Science and Technology Institute, University of Science and Technology of China (USTC), Suzhou 215123, China
cSchool of Materials Science and Engineering, Georgia Institute of Technology, 771 Ferst Drive, Atlanta, Georgia 30332, USA
dDepartment of Electronic Engineering, Faculty of Engineering, The Chinese University of Hong Kong, Hong Kong, China
First published on 23rd June 2015
A novel protocol to prepare multifunctional magnetic organic–inorganic nanostructured catalysts of Fe3O4@organosilicon/Ag with tailored properties is developed. Such nanostructure design endows the catalysts with superparamagnetism (11.6 emu g−1), excellent oxidation resistance, and catalytic activity. Fe3O4 nanoparticles (NPs) are encapsulated with porous organosilicon via improved self-assembly of a flexible-bridged organosilicon precursor without templates. Subsequently, dispersed Ag NPs are in situ grown on the porous microparticles via a silver mirror reaction. The as-prepared multifunctional catalysts are characterized by scanning electron microscopy, X-ray photoelectron spectroscopy, a vibration sample magnetometer, X-ray diffraction, thermal gravimetric analysis, and nitrogen adsorption and desorption, respectively. The resultant hybrid microparticles possess micro- and nano-pores, and exhibit a small hysteresis loop and low coercivity. Meaningfully, they exhibit exceptional catalytic performance for the reduction of 4-nitrophenol in the presence of sodium borohydride and could be reused at least 9 times with excellent stability by means of convenient magnetic separation. The catalysts could be employed to reduce other dyes such as methylene blue, orange G and rhodamine B, and their corresponding reductions follow pseudo-first-order reactions. Therefore, the proposed structure design and scalable route for the synthesis of hierarchical catalysts can pave the way for synthesizing other catalyst systems to address the diverse reaction demands.
To overcome these mentioned issues, many methods have been developed to synthesize magnetically retrievable Ag-based catalyst. Fe3O4 magnetic nanoparticles (MNPs), which possess high saturation magnetization, low coercivity and good biocompatibility, could be employed as perfect platforms for loading various nanocatalysts.12–14 Lin15 developed dumbbell-like Au–Fe3O4 nanostructures as recyclable nanocatalysts for reduction of 4-nitrophenol (4-NP) to 4-aminophenol (4-AP) in the presence of NaBH4. Li16 reported the preparation of recyclable catalysts Ag/Au-decorated Fe3O4/SiO2 nanoparticles through Au seeds attached onto NH2-SSCNs, followed by the deposition of Ag for catalytic reduction of methylene blue. However, Fe3O4 MNPs are prone to be easily aggregated, oxidized or dissolved in acid medium during the treatment procedure, and the traditional silica layer is non-porous and needs to be modified to loading metal NPs.16–19 Therefore, a suitable approach to design multifunctional composites consisting of Fe3O4 MNPs and other functional components is essential to avoid such limitations. Organosilicon is regarded as one of the efficient coating layer for Fe3O4 MNPs due to its high chemical and thermal stabilities, adjustable reactive sites, and good bio-compatibilities.20–22 On the other hand, organosilicon is also regarded as promising candidate for immobilizing Ag NPs and avoiding the aggregation of Ag NPs.23 The integrated microspheres of magnetic oxides and noble metals could endow the porous organosilicon with excellent catalytic activity and convenient magnetic separation. In return, the porous organosilicon could immobilize the Ag NPs and enhance the stability of Fe3O4 core. In general, it remains a challenge to how to conveniently synthesize these desirable multifunctional structures for extended applications.
In the present work, we propose a facile and scalable approach to deposit Ag NPs on Fe3O4 encapsulated with organosilicon (Fe3O4@Si/Ag), which is applied to catalytic reduction of diverse dyes. Initially, magnetically responsive Fe3O4@Si (core@shell) microparticles are fabricated via solvothermal and improved sol–gel method. Then, Ag NPs are in situ grown on the surface of Fe3O4@Si microparticles via the silver mirror reaction. The as-prepared Fe3O4@Si/Ag catalyst could successfully realize a combination of functions and features from single component. Furthermore, as a magnetically recoverable catalyst, its catalytic performance, reusability along with the corresponding kinetics behaviours are also investigated in the reduction of 4-NP, orange G, methylene blue, and rhodamine B in the presence of NaBH4. More important, the unique Fe3O4@Si hierarchical structure makes the microparticles promising candidates for immobilizing metal catalyst.
The organosilicon coated Fe3O4 microparticles are prepared under multi-step acid–alkali condition without templates. All glassware is dried completely prior to use. Typically, 6.5 g DHBP/CHCl3 solution (34 wt%) and 6.44 g Fe3O4/ethanol solution (5 wt%) are charged into a round bottomed flask equipped with a mechanical stirrer, and the mixture is stirred vigorously for 5 min. Then 0.65 g diluted HCl (0.1 M) is added into the above solution and stirred for another 3 min to obtain uniform solution. Subsequently, 0.07 g HCl (10 M) is then dropwise added to the mixture under ultrasonication condition for 2 min, and a solution of ethanol (10 mL) and CHCl3 (5 mL) is poured to the mixture. After another 5 min 1.5 mL ammonium hydroxide (25 wt%) is added. The reaction is stirred for another 20 min, and then aged for 0.5 h at room temperature. The products are washed with CHCl3, ethanol and water sequentially, and dried in an oven overnight at 60 °C. It should be noted that the concentration and amount of HCl and NH4OH should be well controlled.
To study the recyclability of the magnetic catalysts, the used Fe3O4@Si/Ag catalyst is separated from the solution by magnet after the completion of reduction process. Similar to the above catalytic reduction process, the cuvette is then placed in a UV-vis spectrophotometer to monitor the time-dependent absorption at λmax = 400 nm at room temperature. The recycle tests are repeated at least 9 times.
To characterize the structure variations during the whole synthesis procedure, FTIR spectra are recorded in Fig. 1a. Absorption bands at 2930 and 2850 cm−1 are attributed to the asymmetric and symmetric stretching vibration of C–H in aliphatic CH2 groups, while the peaks at 1580 cm−1 result from the bending vibrations of N–H. In the curve of DHBP, the disappearance of peaks at 2275 and 1360 cm−1 attributed to stretching vibrations of –NCO, and emergence of a new carboxylic band at 1700–1750 cm−1 and a strong peak of the C–O stretching at 1080 cm−1 indicate that the reaction between the amine group of APTS and isocyanate group of HDI occurs successfully.27,28 The broad absorption peaks at 3333 cm−1 corresponding to –OH group indicate the existence of the hydroxyl group. The characteristic peaks at 560 cm−1 are assigned the Fe–O stretching vibration of Fe3O4, confirming the existence of Fe3O4.29 Moreover, the spectrum of Fe3O4@Si/Ag is almost the same as that of the Fe3O4@Si but a weak intensity, resulting from the non-absorption of Ag NPs in the infrared regions.30 More detailed information regarding the chemical and bonding environment of Fe3O4 and Fe3O4@Si/Ag is ascertained using X-ray photoelectron spectroscopy (XPS). The binding energies at 710.5 and 724.1 eV are contributed to the peaks of Fe 2p3/2 and Fe 2p1/2 in Fe3O4, respectively (Fig. 1b). There are no obvious shakeup satellite structures at the higher binding energy side of both main peaks (about 718.8 and 729.5 eV), which is the characteristic of Fe3O4. The relative areas ratio of the deconvoluted peak assigned to Fe2+ and Fe3+ are calculated to be 0.31:
0.69, which is clearly that of the stoichiometric of Fe3O4 within the uncertainty of calculations.31 In the case of Fe3O4@Si/Ag, the doublet peaks at 367.8 and 373.8 eV, corresponding to Ag 3d5/2 and Ag 3d3/2, and the gap between the two states (6.0 eV), demonstrate that Ag in the composite is zero-valent and further testify that Ag(NH3)2OH has been reduced to Ag NPs by silver mirror reaction.32 Fig. 1c shows the representative XRD patterns of all the samples. The diffraction peaks of Fe3O4 NPs can be indexed to the face-centered cubic structures of magnetite. The characteristic peaks at 2θ = 18.3°, 30.1°, 35.8°, 43.1°, 53.4°, 57.2°, 62.5° and 74.5°, corresponding to (111), (220), (311), (400), (422), (511), (440) and (533) crystal planes of Fe3O4,8 are observed in all samples, revealing that its crystalline structure is well maintained after a series of functionalization. Besides, the apparent broad peak at around 2θ = 23° corresponding to the amorphous peak of organosilicon, indicates that organosilicon has successfully encapsulated the Fe3O4 NPs. In the case of Fe3O4@Si/Ag catalysts, with the exception of characteristic peaks of Fe3O4, five new peaks appearing at 2θ = 38.1°, 44.1°, 64.4°, 77.3° and 81.3°, are corresponding to the (111), (200), (220), (311) and (222) crystal planes of the face centered cubic of Ag,10 which prove the formation of Ag NPs and its good crystal structure. These aforementioned results confirm the formation of multifunctional hierarchical catalyst. The thermal behaviors of Fe3O4, Fe3O4@Si and Fe3O4@Si/Ag are assessed by TGA under nitrogen atmosphere in Fig. 1d. It could be seen that the significant weight loss in the range of 200–600 °C is mostly attributed to the degradation of polymer chains of organosilicon and the residual weight increases after the deposition of Ag NPs, which implies that the successful encapsulation of Fe3O4 with organosilicon and the immobilization of Ag NPs.
The morphologies and structure of Fe3O4, Fe3O4@Si and Fe3O4@Si/Ag are further investigated by SEM (Fig. 2). As revealed in Fig. 2a and b, the Fe3O4 microparticles have well-defined spherical morphology with average diameter of 700 nm. Through an improved sol–gel process, the Fe3O4 MNPs encapsulated with organosilicon possess rough surface and porous structure, which are not only good platforms for the immobilization of Ag NPs and the multiple accessible channels for diffusion and transport of the reactant molecules, but also improves the oxidation resistance of Fe3O4 core. Furthermore, it can be seen that there is no essential structure change after the growth of Ag NPs in the Fe3O4@Si/Ag compared with that of Fe3O4@Si in Fig. 2d. Therefore, desirable multifunctional structures are successfully developed via a series of processes, including solvothermal method, improved sol–gel method and silver mirror reaction.
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Fig. 2 (a and b) SEM images of Fe3O4 NPs, (c) SEM image of Fe3O4@Si microparticles, and (d) SEM image of Fe3O4@Si/Ag particles, and Ag NPs are marked with ellipses. |
To investigate the detailed information of the porous structure in the resultant microparticles, the surface area and pore size distribution are determined by the multipoint BET method using N2 adsorption/desorption analysis. Fig. 3 shows the N2 adsorption/desorption isotherms and BJH pore size distribution of Fe3O4, Fe3O4@Si and Fe3O4@Si/Ag. All isotherms can be classified to a type-IV isotherm with H3 hysteresis loop according to the IUPAC and BDDT classification.33 The BET surface area, pore volume and pore size are summarized in Table S1.† These results reveal that there are nano-sized pores, and the primary and secondary pore diameters are centred at 2 and 90 nm (Fig. 3b), respectively, implying that the Fe3O4@Si maintains its initial porous structure after the immobilization of the Ag NPs. The decrease in pore size indicates that the Ag NPs occupies the pores of the Fe3O4@Si microparticles, and the increase in surface area results from the accumulation of Ag NPs.
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Fig. 3 (a) N2 adsorption/desorption isotherms and (b) pore size distribution of samples Fe3O4, Fe3O4@Si and Fe3O4@Si/Ag. |
The magnetic behaviours of these materials are critical to ensure magnetic separation. Fig. 4 shows the room-temperature magnetic hysteresis loops of Fe3O4, Fe3O4@Si and Fe3O4@Si/Ag. They exhibit a small hysteresis loop and low coercivity, suggesting superparamagnetic behaviour. The main magnetic parameters of the three samples are listed in Table S2.† The magnetic saturation (Ms) values are 81.1, 15.3, and 11.6 emu g−1, respectively, depending on the effective mass of the Fe3O4 microspheres. Whereas the coercivity values are 34.9, 43.8, and 47.9 Oe, respectively. The slight changes of coercivity might be attributed to the influence of the surrounding environment.24,34 To investigate the magnetic response of the catalyst visually, a magnet is placed beside the cuvette, Fe3O4@Si/Ag microparticles in aqueous solution are attracted to the side of the cuvette leaving the solution transparent within 10 s. Therefore, the catalysts could be separated from water quickly under the magnetic field, leading to easy recycling and reuse.
As shown in Fig. 5a, upon the addition of NaBH4 aqueous solution, the UV-vis absorbance band immediately shifts from 317 to 400 nm, which is attributed to the formation of 4-nitrophenolate under the alkaline condition. Meanwhile, the corresponding colors change from yellow to yellow green.36 The reaction conversion can be calculated from C/C0, which is measured from the relative intensity of UV-vis absorbance (A/A0) at 400 nm. Herein, C is the concentration of 4-NP during the reaction and C0 is the initial concentration. It is noteworthy that the reduction of 4-NP with an excess amount of NaBH4 could not occur without suitable catalysts. As shown in Fig. 5b, once introducing a small amount of the Fe3O4@Si/Ag catalyst, the peak intensity at 400 nm successfully decreases with concomitant increase in peak at 300 nm as the reduction proceeds, which is the characteristic absorption peak of 4-aminophenol (4-AP), indicating the occurrence of reduction of 4-NP to 4-AP. Meanwhile, the reduction of 4-NP could also be visually witnessed through color change from yellow green to colorless within 12 min. Moreover, the addition of the alone Fe3O4@Si cannot promote the reduction of 4-NP even after 120 min and the Ag NPs alone could promote the occurrence of reduction of 4-NP (Fig. 5c), undoubtedly confirming that the reduction of 4-NP by NaBH4 is solely catalyzed by Ag NPs immobilized on Fe3O4@Si. That is to say, Ag NPs in the reaction system play an important role in electron transference between the BH4− ions and 4-nitrophenolate ions. It is worth noting that the reaction starts immediately without induction time after the addition of catalysts.
The concentration of NaBH4 is higher than that of 4-NP, and it could be considered as constant during the reaction process. Pseudo-first-order kinetics can be applied to evaluate the reaction rate constants. The reaction kinetics can be described as ln(C/C0) = −kt, where k is the apparent first-order rate constant (min−1) and t is the reaction time (min).37 Therefore, we plot ln(C/C0) vs. reaction time t in Fig. 5d and e, which show a good linear relationship for ln(C/C0) against reaction time t in the catalytic reduction catalyzed by the heterostructures following pseudo-first-order kinetics. The kinetic reaction rate constant (k) calculated from the slope of the straight line in Fig. 5d are 0.0001, 0.453 and 2.010 min−1, respectively. The increase of rate constant directly indicates the speeding up of the degradation of 4-NP, which is attributed to that more catalysts could offer larger surface area and active sites to enhance the contacting opportunity with 4-NP, resulting in the enhancement of catalytic activity. Moreover, the kinetic reaction rate constant (k) of the reduction catalyzed by Ag NPs alone is 3.676 min−1, which is higher than that of Fe3O4@Si/Ag catalyst due to the effective mass of Ag NPs.
On the other hand, the effect of concentration of NaHB4 aqueous solution on reaction rate constant k is also investigated in Fig. 5e. When the mole ratio between the 4-NP and NaBH4 is 100, 200, 400, the corresponding rate constant k are calculated to be 0.203, 0.453 and 0.864 min−1, respectively. The increase in rate constant k results from the more electrons offered by higher amounts of NaHB4.
In order to demonstrate the universality of Fe3O4@Si/Ag catalyst, the catalytic reductions of OG, RhB and MB with NaBH4 have been used as other model reactions. The whole reaction involves the following processes: NaBH4 is adsorbed onto the catalyst surface to form metal hydride, and then various dyes are also adsorbed onto the surface; dyes are reduced and desorbed to create a free space for the reaction to continue. Fig. S2a† shows the successive UV-vis spectra of the OG reduction in the presence of Fe3O4@Si/Ag. Obviously, the absorption intensity at λmax = 478 nm of OG decreases with the reaction time, indicating the occurrence of the reduction of OG. As expected, the catalytic reduction proceeds successfully, and no poisoning of catalyst occurs. Similar to the reduction of 4-NP, reduction of OG also follows pseudo first-order kinetics and exhibits a good linear relationship, as shown in Fig. S2b.† The catalyzed reaction rate is determined to be 0.091 min−1, which is ten times higher than that of reduction without catalyst (0.0094 min−1). As for the reduction of RhB and MB, the similar results are obtained, which certifies that the Fe3O4@Si/Ag has excellent performance towards the hydrogenation of diversiform dyes under aqueous reaction conditions.
Regeneration capacity of catalyst is of great importance in the view of practical application. Hence, the successive cycles of the catalytic reduction of 4-NP are performed with Fe3O4@Si/Ag. After each run of catalysts, the catalysts are separated from the reaction mixture by magnet, rinsed with deionized water, and then reused in the next cycle. As shown in Fig. 5f, in the first three cycles, the conversion is almost 100%; with the increase in cycling times, the conversion drops and still remains at 80% for the same reaction time (5 min), which implies that Fe3O4@Si/Ag could serve as a recyclable and reusable catalyst. The recyclability of the catalyst may result from the efficient stabilization of Fe3O4@Si/Ag.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c5ra08963h |
This journal is © The Royal Society of Chemistry 2015 |