Fe3O4@P(DVB/MAA)/Pd composite microspheres: preparation and catalytic degradation performance

Baoliang Zhang*, Jiqi Wang, Junjie Chen, Hengyang Li, Hai Wang and Hepeng Zhang
Key Laboratory of Applied Physics and Chemistry in Space, Ministry of Education, Department of Applied Chemistry, School of Science, Northwestern Polytechnical University, Youyi Road 127#, Xi’an, 710072, China. E-mail: blzhang@nwpu.edu.cn; Fax: +86-029-88431653; Tel: +86-029-88431675

Received 23rd September 2016 , Accepted 12th October 2016

First published on 12th October 2016


Abstract

Fe3O4@P(DVB/MAA)/Pd composite microspheres were synthesized with a combination of coating and loading processes using Fe3O4 nanoparticles as a core. A series of characterizations revealed that a combination of Fe3O4 coated with a thin polymer shell and deposited Pd nanoparticles was successful. The saturation magnetization of Fe3O4@P(DVB/MAA)/Pd was 55.2 emu g−1 and the Pd content was 21.3%. Degradation activity studies confirmed that the as-obtained microspheres showed excellent degradation behavior towards RhB. The degradation efficiency of the Fe3O4@P(DVB/MAA)/Pd microspheres for rhodamine B (RhB) can reach 99.6% within 90 s. The regenerated catalyst still showed a catalytic degradation percentage of 98% after being used fifteen times. Meanwhile, the obtained catalyst also displayed degradation ability for other organic dyes. Using Fe3O4@P(DVB/MAA)/Pd microspheres is a very promising approach for the remediation of wastewater containing organic dyes due to the fast degradation rate, high degradation efficiency and excellent reusability.


1. Introduction

Dyes have been widely used in the leather, food and apparel industries and some other areas. Their industrial mass production and application generate a large amount of sewage, which creates a serious burden on the environment. During the past few decades, various methods have been used for treatment of dyes in wastewater. They can be divided into two categories: adsorption and degradation. Porous materials with high specific surface area or high selectivity are often used as adsorbents, including mesoporous SiO2,1,2 activated carbon,3,4 polymeric microspheres,5–7 etc. Semiconductor materials exhibit high degradation activity and materials such as independent or load-type TiO2,8,9 ZnO,10,11 cobalt oxide12,13 and quantum dots14,15 have been reported to decolorize wastewater.

In order to recycle treatment agents easily, magnetic functional materials have received great attention.16–19 Compared with conventional separation techniques such as centrifugation, precipitation and filtration, magnetic separation is a promising technique because of its easy operation and fast separation. A large number of load-type magnetic adsorbents and degradation agents have been used for dye treatment in liquids, and they have achieved satisfactory effects. These include magnetic carbon nanotubes,20 magnetic mesoporous silica,1,2 molecularly imprinted magnetic particles,21,22 Fe3O4@TiO2,23,24 Fe3O4@SiO2@TiO2,25–27 etc. Magnetic degradation agents display obvious application advantages because of the complete treatment and high recycling rate.23–27 In addition to photocatalytic degradation, in recent years, precious metal catalytic oxidation reduction degradation has become a research hotspot due to its fast degradation speed. This was demonstrated by Yang et al.,28 who loaded Pd nanoparticles onto Fe3O4 nanochains for the degradation of methylene blue (MB). The results showed that the hydrogenation of MB occurred in microdroplets and was catalyzed by Pd. The blue microdroplets became colorless in 75 s. This study demonstrates an effective method for the rapid removal of dyes in microsystems. However, it is not suitable for the treatment of large-scale industrial wastewater containing dyes.

In our previous work, we reported three kinds of magnetic degradation agents composed of Fe3O4 and a metal oxide semiconductor for removing organic dyes.13,24,29 The degradation efficiencies of the above materials are satisfactory, but the degradation speed needs to be improved. In this work, we report a rapid reductive degradation method for organic dyes based on the design and successful preparation of Fe3O4@P(DVB/MAA)/Pd magnetic composite microspheres. The advantages of the obtained catalysts are as follows: (1) compared with carbon materials and pure polymer microsphere carriers, magnetic materials as Pd carriers show excellent separation and recovery performance; (2) the polymer shell provides carboxy groups for the combining of Pd as well as improving the stability of the magnetic core; (3) the catalysts display the property of rapid degradation. The degradation performance of the as-prepared catalyst was investigated. The influences of initial concentration, reaction time and type of dye on the degradation efficiency were also studied.

2. Experimental sections

2.1 Materials

Divinylbenzene (DVB, 80% mixture of isomers) and palladium chloride (PdCl2) were purchased from J&K Scientific Ltd. Methacrylic acid (MAA), ethylene glycol (EG), rhodamine B (RhB), methylene blue (MB), methyl orange (MO), bromocresol green (BG), sodium borohydride (NaBH4) and azobisisobutyronitrile (AIBN) were bought from Sinopharm Chemical Reagent Co. Ltd. Sodium citrate, ferric chloride hexahydrate (FeCl3·6H2O), ethanol, hexamethylenediamine (HMD) and acetonitrile were purchased from Xi’an Sanpu Fine Chemical Plant. All of the above chemicals were analytical reagents. The water used throughout the work was deionized water produced by apparatus for pharmaceutical purified water (Aquapro Co. Ltd.).

2.2 Preparation of Fe3O4@P(DVB/MAA) microspheres

Fe3O4 nanoparticles were prepared through a hydrothermal method. 2.70 g of FeCl3·6H2O and 10.43 g of HMD were dissolved in 60 mL of EG under ultrasonic irradiation. The solution was transferred to a 100 mL Teflon-lined stainless-steel autoclave and heated at 200 °C for 12 h. The autoclave was then carefully cooled at room temperature. The black products of Fe3O4 nanoparticles were washed with ethanol and water using magnetic separation, and then dried by vacuum freeze-drying. Fe3O4@P(DVB/MAA) microspheres were synthesized by distillation precipitation emulsion polymerization, as in our previous work.30 Typically, 0.10 g of Fe3O4 nanoparticles, 0.05 g of AIBN, 0.60 g of MAA and 1.40 g of DVB were dispersed and dissolved in 150 mL acetonitrile. The suspension liquid was treated with ultrasonic irradiation. The reaction was carried out under mechanical stirring at 80 °C. After 10 h, the products were separated and washed with ethanol and water using magnetic separation. The obtained materials were Fe3O4@P(DVB/MAA) microspheres.

2.3 Preparation of Fe3O4@P(DVB/MAA)/Pd composite microspheres

A typical experimental procedure for the fabrication of Fe3O4@P(DVB/MAA)/Pd composite microspheres was as follows.31 Typically, 0.20 g of Fe3O4@P(DVB/MAA) was dispersed into a mixture of ethanol and water under ultrasonic irradiation. The volume of the mixture was 60 mL and the volume ratio of ethanol and water was 2[thin space (1/6-em)]:[thin space (1/6-em)]1. 10 mg of PdCl2 was added into the mixture under mechanical stirring at 45 °C for 12 h. Then, the products were separated and washed with deionized water three times. After vacuum freeze-drying, the Fe3O4@P(DVB/MAA)/Pd(II) precursor particles were obtained. 0.15 g of the as-prepared precursor particles was dispersed into 50 mL of a mixed solution of ethanol and water (the volume ratio was 3[thin space (1/6-em)]:[thin space (1/6-em)]2) under ultrasonic irradiation. 0.10 g of NaBH4 was added into the system. The reaction was carried out at 45 °C for 24 h. The Fe3O4@P(DVB/MAA)/Pd composite microspheres were obtained after washing with water and vacuum freeze-drying.

2.4 Determination of degradation performance

300 μL of an aqueous solution of NaBH4 (0.25 mol L−1) was poured into a 1.5 mL EP tube containing 5 mg of the Fe3O4@P(DVB/MAA)/Pd composite microspheres. After dispersing well, 700 μL of the dye solution was added to the above mentioned mixture and the initial concentration was 15 mg L−1. Then, the EP tube was put on a vertical mixer for the reaction. After a defined time, the Fe3O4@P(DVB/MAA)/Pd composite microspheres were magnetically separated from the suspension liquid. The supernatant was investigated by UV-vis for the calculation of the degradation efficiency. RhB, MO, MB and BG were chosen as model substrates. 5, 15, 20, 25, 30 and 35 mg L−1 were selected for the investigation of the initial concentration. The reaction variables at 10, 15, 20, 25, 30, 35, 40, 50, 60 and 90 s were also detected.

2.5 Characterization

Fourier transform infrared (FTIR) spectra were acquired on a TENSOR27 FTIR spectrometer (Bruker). The morphology of the nanoflowers was observed using a Scanning Electron Microscope (SEM, JEOL JSM-6700F) and a Transmission Electron Microscope (TEM, JEOL JEM-3010). Specific surface areas and pore size distribution were computed from the results of N2 physisorption (Tristar3020, Micromeritics) using the BET (Brunauer–Emmet–Teller) method. Powder X-ray diffraction (XRD) patterns were recorded on a Shimadzu XRD-6000 diffractometer using Cu Kα radiation. The concentration of the dye was analyzed using a UV-vis spectrophotometer (BlueStar, LabTech). The magnetic properties of the magnetic particles were assessed using a vibrating sample magnetometer (VSM, Lake Shore 7307). The magnetic content was measured according to the weight percentage of the residue after thermal analysis from room temperature to 550 °C with a heating rate of 10 °C min−1 under an air atmosphere. The content of palladium was recorded on an inductive coupled plasma emission spectrometer (ICP, 6300).

3. Results and discussion

3.1 Morphology of the composite microspheres

The synthesis procedure, illustrated in Fig. 1, begins with the synthesis of Fe3O4 nanoparticles through a solvothermal method. Then, the Fe3O4 nanoparticles were initially coated with a thin polymer shell, using DVB and MAA as monomers, by precipitation polymerization, to protect the magnetic cores and introduce carboxy groups to the surface of the magnetic core. The product is denoted Fe3O4@P(DVB/MAA). Subsequently, Pd nanoparticles were deposited onto the surface of the as-prepared Fe3O4@P(DVB/MAA) using PdCl2 as the precursor and NaBH4 as the reducing agent. Then, the Fe3O4@P(DVB/MAA)/Pd composite microspheres were obtained.
image file: c6ra23634k-f1.tif
Fig. 1 Schematic illustration of the preparation procedure of Fe3O4@P(DVB/MAA)/Pd composite microspheres.

Fe3O4 nanoparticles modified with amino groups were prepared using a solvothermal method. TEM and SEM images are shown in Fig. 2A and B. The average diameter of the Fe3O4 nanoparticles was estimated to be about 100 nm. It can be seen from the TEM image (Fig. 2A) that the mass thickness contrast of the particles was different. The SEM image in Fig. 2B confirms that the particles were constructed by Fe3O4 nanocrystals and many pores were observed between the nanocrystals. Therefore, the light gray spots on the nanoparticles in the TEM image were attributed to the above mentioned pores. In comparison with the pure Fe3O4 nanoparticles, a thin polymer layer, which was coated on the surface of the Fe3O4 nanoparticle, was clearly observed in Fig. 2C, and the surface roughness of the Fe3O4@P(DVB/MAA) composite microspheres (see Fig. 2D) was decreased. This suggested that the P(DVB/MAA) shell successfully covered the outer surface of the as-obtained Fe3O4 nanoparticles. Fig. 2E and F are TEM and SEM images of the Fe3O4@P(DVB/MAA)/Pd composite microspheres. As shown in Fig. 2D, small Pd nanoparticles are attached to the surface of the Fe3O4@P(DVB/MAA) microspheres. The increase in surface roughness seen in Fig. 2F further confirmed the existence of Pd nanoparticles. The diameter of the Pd nanoparticles was about 15 nm.


image file: c6ra23634k-f2.tif
Fig. 2 TEM and SEM images of the as-prepared particles: Fe3O4 nanoparticles (A and B); Fe3O4@P(DVB/MAA) composite microspheres (C and D); Fe3O4@P(DVB/MAA)/Pd composite microspheres (E and F) (the scale bar is 100 nm).

3.2 Composition and performance of the composite microspheres

In order to validate the composition of the products, the samples were examined by powder X-ray diffraction. As demonstrated in the XRD pattern in Fig. 3A, in the 2θ range of 20–80°, a series of characteristic peaks of Fe3O4 at around 2θ = 30.2°, 35.6°, 43.3°, 53.7°, 57.3° and 62.8°, which were related to the reflections of the (220), (311), (400), (422), (511) and (440) planes, respectively, were observed for all samples and are well indexed to the typical cubic inverse spinel structure (JCPDS card no. 19-0629).32 These peaks are sharp and intense, indicating the well crystallized structure. As deduced from Debye–Scherrer’s formula, the average size of the Fe3O4 was about 24.6 nm. There were no additional peaks in the pattern of the Fe3O4@P(DVB/MAA) microspheres. The reason for this was that the polymer shell was amorphous. In addition, the deposition of the Pd nanoparticles onto the microspheres can be confirmed from the corresponding XRD data. In the blue curve in Fig. 3A, besides the obvious peaks of Fe3O4, there also exist three other diffraction peaks (labeled with the symbol ■). The three peaks positioned at 2θ values of 40.1°, 46.6° and 68.1°, can be attributed to the reflections of the (111), (200) and (220) crystalline planes of Pd (JCPDS card no. 65-2867), respectively. This result demonstrated the occurrence of the combination of Fe3O4@P(DVB/MAA) and Pd.
image file: c6ra23634k-f3.tif
Fig. 3 X-ray diffraction patterns (A) and FTIR spectra (B) of Fe3O4 nanoparticles, Fe3O4@P(DVB/MAA) microspheres and Fe3O4@P(DVB/MAA)/Pd microspheres.

Fig. 3B shows the FTIR spectra of the as-prepared particles. The strong characteristic absorption peaks at 580 cm−1, which were observed in the spectra of all the products, were attributed to the Fe–O vibration. Compared with Fe3O4 nanoparticles, the increased peaks at 846, 1448, 1552, 1602, 1701 and 2800–3000 cm−1, which belong to absorption bands of benzene rings, carbonyl groups and saturated carbon–hydrogen bonds, were detected in the spectrum of Fe3O4@P(DVB/MAA). This indicated that the shell coated on the surface of the Fe3O4 nanoparticles was polymerized by DVB and MAA. The main absorption peaks of Fe3O4@P(DVB/MAA)/Pd were similar to those of the Fe3O4@P(DVB/MAA) composite microspheres.

The weight percentages of each component in the Fe3O4 nanoparticles, Fe3O4@P(DVB/MAA) and Fe3O4@P(DVB/MAA)/Pd composite microspheres were estimated based on mass data from TGA curves. As shown in Fig. 4A, it can be clearly observed that the weight loss of the Fe3O4 nanoparticles was 5.6%, which can be attributed to the thermal decomposition of small organic molecules and functional groups. The magnetic content of the Fe3O4@P(DVB/MAA) microspheres was 87.3%. It can be calculated that the ratio of the thin polymer shell was 7.8%. The weight loss of the Fe3O4@P(DVB/MAA)/Pd composite microspheres was 9.4%. The solid residues were Fe3O4 and Pd. Meanwhile, the content of Pd nanoparticles was measured by ICP, and the value was 21.3%.


image file: c6ra23634k-f4.tif
Fig. 4 The thermal gravimetric curves (A) and magnetization curves (B) of the Fe3O4 nanoparticles, Fe3O4@P(DVB/MAA) microspheres and Fe3O4@P(DVB/MAA)/Pd microspheres.

The magnetic properties of the samples were determined by VSM at room temperature as illustrated in Fig. 4B. The values of saturation magnetization (Ms) of the Fe3O4 nanoparticles, Fe3O4@P(DVB/MAA) and Fe3O4@P(DVB/MAA)/Pd composite microspheres were 83.6, 74.7 and 55.2 emu g−1, respectively. The results showed that the polymer shell and the deposited Pd nanoparticles weakened the saturation magnetization of the Fe3O4 core to some extent. However, the final catalyst still showed good magnetic properties. In addition, no pronounced hysteresis loop was found and the remanence of the particles was about zero. This indicated that the as-obtained magnetic materials were superparamagnetic.

Fig. 5 shows the N2 adsorption–desorption isotherms and pore size distributions of the particles. The adsorption–desorption isotherms (Fig. 5A) of all samples belonged to the type IV isotherm (isotherms with a hysteresis loop) according to IUPAC, and the hysteresis loops were H3 type. Such a hysteresis loop type indicated that the samples contained stack-type pores. The specific surface areas of the Fe3O4 nanoparticles, Fe3O4@P(DVB/MAA) and Fe3O4@P(DVB/MAA)/Pd composite microspheres were 55.25, 13.05 and 23.84 m2 g−1, respectively, and the average pore sizes were 8.03, 21.24 and 18.23 nm, respectively.


image file: c6ra23634k-f5.tif
Fig. 5 BET (A) and pore size distribution (B) curves of the Fe3O4 nanoparticles, Fe3O4@P(DVB/MAA) microspheres and Fe3O4@P(DVB/MAA)/Pd microspheres.

3.3 Degradation of dyes

RhB was chosen as the pollutant model to investigate the degradation properties of the Fe3O4@P(DVB/MAA)/Pd composite microspheres. To examine the influence of time on dye degradation, kinetics experiments were carried out at room temperature. The initial concentration of RhB was 15 mg L−1. As shown in Fig. 6A, the degradation efficiency of the Fe3O4@P(DVB/MAA)/Pd microspheres was up to 98.9% within 60 s, whereas the removal efficiencies of Fe3O4, Fe3O4@P(DVB/MAA) and NaBH4 were 13.1%, 7.5% and 1.9%, respectively, under the same conditions. When the reaction time was prolonged to 90 s, the degradation efficiency of the Fe3O4@P(DVB/MAA)/Pd microspheres reached 99.6%. Investigations into the effect of the initial concentration of RhB on the catalytic degradation efficiency were carried out by adjusting the initial concentration of RhB from 5 mg L−1 to 35 mg L−1 with a reaction time of 60 s, and the results are depicted in Fig. 6B. As the initial concentration of RhB changed from 5 mg L−1 to 15 mg L−1, the degradation efficiency showed no obvious change. At a higher initial concentration, the degradation efficiency decreased with the increase of the initial concentration. It is well known that the reaction is reactant-limited and that the high initial concentration and the long reaction time is needed.
image file: c6ra23634k-f6.tif
Fig. 6 The time dependence of the removal efficiency (A); effect of initial concentration of RhB on the removal efficiency (B).

The reusability of the Fe3O4@P(DVB/MAA)/Pd microspheres was investigated in this study. The reuse process is schematically illustrated in Fig. 7. Deionized water was used as a cleaning agent for the regeneration of the Fe3O4@P(DVB/MAA)/Pd microspheres. The magnetic catalyst materials were collected by a permanent magnet each time and they can be re-dispersed again simply by shaking after removing the magnet. Consequently, the treatment is a green process with low energy consumption, which normally does not lead to any waste disposal problems. From the TEM images (inset of Fig. 7), it can be seen that a good morphology of Fe3O4@P(DVB/MAA)/Pd remained after being used fifteen times, indicating that the obtained catalysts had excellent stability. Repeated experiments were carried out to check the reusability of the Fe3O4@P(DVB/MAA)/Pd microspheres according to the above described process. As shown in Fig. 8, the degradation capacity of the as-prepared catalyst for RhB did not show any significant decrease even after fifteen cycles of successive reuse. After being used fifteen times, it still showed a catalytic degradation percentage of 98% under the same conditions (Fig. 9).


image file: c6ra23634k-f7.tif
Fig. 7 Schematic diagram of the reuse process of the Fe3O4@P(DVB/MAA)/Pd composite microspheres.

image file: c6ra23634k-f8.tif
Fig. 8 Reusability of the Fe3O4@P(DVB/MAA)/Pd composite microspheres for the degradation of RhB.

image file: c6ra23634k-f9.tif
Fig. 9 The removal efficiency of different dyes by the Fe3O4@P(DVB/MAA)/Pd composite microspheres.

The catalytic degradation properties of the Fe3O4@P(DVB/MAA)/Pd microspheres were also evaluated for other organic dyes including MB, MO and BG. It was obvious that the obtained catalyst displayed degradation ability for the above dyes. At a reaction time of 60 s, the degradation efficiency showed a trend of MB > BG > MO, and the values were 92.6%, 71.8% and 23.6%, respectively, which is lower than that of RhB. The major reason for the difference in catalytic conversion of different dyes under the same conditions is the structure of the dye. RhB is anionic and it tended to adsorb on the Pd nanoparticles. The other three kinds of cationic dyes were not inclined to adsorb on Pd nanoparticles.33 Therefore, the degradation efficiency of RhB was higher. During the degradation process, the reduction reaction happened on the surface of the Pd nanoparticles, which played the role of the catalysts. The reaction occurred between the dyes and NaBH4, which were adsorbed on the Pd nanoparticles.

A comparison of the performance of Pd-based materials is given in Table 1. Comparing the as-prepared Fe3O4@P(DVB/MAA)/Pd microspheres with previously reported catalysts, it could be seen that the designed catalysts exhibited excellent degradation efficiency and a rapid degradation rate.

Table 1 Removal ability of Pd-based materials
Pd-based materials Dyes Concentration (mg L−1) Removal ability References
Time Removal efficiency
a The data were read from the curves which are shown in the references.
Pd-activated carbon Bromophenol red 20 19 min 97% 34
Agar@Fe/Pd RhB 5 35 min 81% 35
Pd-activated carbon MB 7 9.5 min 95% 36
Pd nanocubes/multiwalled carbon nanotubes MO 20 60 min 99% 37
Pd/hydroxyapatite/Fe3O4 Methylene red 7 80 min >90%a 38
Pd-activated carbon Congo red 25 24 min >90%a 39
Pd nanoparticles(6.6 nm) RhB 3.2 2 min >95% 40
Pd-activated carbon Congo red 20 18 min 80% 41
Fe3O4@P(DVB/MAA)/Pd RhB 15 1.5 min 99.6% This work


4. Conclusion

In summary, Fe3O4@P(DVB/MAA)/Pd microspheres, with a high catalytic degradation activity and a size of about 100 nm, were prepared in this paper. The initial concentration of RhB affected the degradation efficiency. The degradation efficiencies reached up to 98.9% within 60 s when the initial concentration of RhB was 15 mg L−1. The as-prepared catalyst can be regenerated by washing with water and it exhibited excellent and stable reusability. The preliminary results suggest that this kind of magnetic catalyst has potential application value in the ultra-fast and highly efficient degradation of organic dyes. Because of its ease of recovery after liquid phase reaction, it will greatly facilitate the practical running of industrial pollutant cleanup.

Acknowledgements

The authors are grateful for the financial support provided by the State Key Program of National Natural Science of China (Grant No. 51433008), the Natural Science Foundation of Shaanxi Province (Grant No. 2015JQ2055, 2015JM2050), and the National Undergraduate Training Programs for Innovation.

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