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Journal of Nanomaterials
Volume 2015, Article ID 538275, 5 pages
http://dx.doi.org/10.1155/2015/538275
Research Article

Preparation and Photocatalytic Activity of TiO2/Fine Char for Removal of Rhodamine B

School of Materials Science and Engineering, Henan Polytechnic University, Jiaozuo 454000, China

Received 21 January 2015; Revised 27 March 2015; Accepted 27 March 2015

Academic Editor: William W. Yu

Copyright © 2015 Mingjie Ma et al. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

Abstract

TiO2/fine char (FC) photocatalyst was prepared via sol-gel method with tetrabutyl titanate as the precursor and FC as the carrier. The structural property of TiO2/FC photocatalyst was investigated by X-ray diffraction (XRD) and scanning electron microscopy (SEM), and the photocatalytic activity of TiO2/FC was evaluated by photocatalytic degradation of rhodamine B (RhB) aqueous solution under UV light irradiation. The results showed that TiO2 was successfully coated on the surface of FC, and the TiO2/FC photocatalyst had better photocatalytic efficiency and stability for degradation of RhB under UV light illumination as compared to that of the pure TiO2 and FC. The study provided a novel way for the application of FC to the photocatalytic degradation of organic wastes.

1. Introduction

With the development of the industrialization process, more and more industrial waste water has been discharged and waste water treatment has become an urgent problem to be solved [1, 2]. In recent years, photocatalytic oxidation technology for environmental pollution control is becoming a hot spot of environmental science research. , a photocatalytic semiconductor, has been widely applied in the field of photocatalysis due to its many advantages such as low cost, relatively high efficiency, nontoxicity, and good chemical stability. Although possesses high photocatalytic efficiency, it is always powder or particle, which may easily aggregate. In addition, the efficient recovery of from treated water is still a challenge [37]. Immobilizing on a porous solid surface, such as zeolites or activated carbon, can increase the efficiency of and solve the problem of hard recovery [810].

FC is an industrial by-product derived from U-GAS gasifier; if not disposed properly, it may cause environmental pollution. Although it is a solid waste, it has many merits such as porosity, high surface area, and lightweight property, making it a potential application in wastewater and air treatment [11, 12]. In view of the merits of FC, it might be used as a carrier to immobilize onto its surface to prepare photocatalyst, which can show a strong adsorption and photocatalytic degradation towards target pollutants. To the best of our knowledge, it was rarely reported that FC was employed as a photocatalyst.

In this work, /FC photocatalyst was prepared via sol-gel method with tetrabutyl titanate as the precursor and FC as the carrier. The as-prepared photocatalyst was characterized and its photodegradation efficiency was evaluated by photocatalytic degradation of RhB aqueous solution under UV light irradiation. The photocatalyst shows a high photodegradation efficiency. This work not only provided a novel way for the application of FC but also developed a low cost material for the degradation of organic wastes.

2. Experimental

2.1. Preparation of FC Carrier

FC was obtained from the U-GAS gasifier. 20 g of the FC was mixed with 200 mL distilled water under magnetic stirring for 6 hours to remove the soluble compounds. The disposed FC was dried at 105°C for 12 hours and then calcined in muffle furnace at 500°C for 3 hours in air.

2.2. Preparation of TiO2/FC Photocatalyst

Sol-gel method was utilized to prepare the /FC composite photocatalyst with tetrabutyl titanate as the precursor and FC as the carrier. Firstly, the tetrabutyl titanate (10 mL) was added into the solution containing glacial acetic acid (5 mL) and absolute ethyl alcohol (30 mL) drop by drop under the vigorous stirring. After stirring for 30 min, FC (10 g) was introduced with continuous stirring for 30 min. Subsequently, the mixing solution of distilled water (4 mL) and absolute ethyl alcohol (6 mL) was slowly dripped into the aforementioned mixture under rapid stirring. Thus, the /FC gel was obtained. The gel was aged at room temperature for 24 h, followed by drying at 70°C for 24 h. After calcination in air at 500°C for 2 h, the /FC photocatalyst was obtained, and the amount of in /FC catalyst was 19%. In contrast, pure nanoparticles were also prepared by the same procedure without the addition of FC.

2.3. Characterization

XRD was performed on a Rigaku X-ray diffractometer with Cu-Ka radiation (Bruker D8 ADVANCE diffractometer,  Å), over the scanning angle range 10 to 80°. The crystallite size of was calculated by using the Scherrer formula, [13], where is the crystallite size, is the shape factor (0.9), is the X-ray wavelength (1.5406 Å), is the line broadening at half of the maximum intensity, and is the diffraction angle. SEM (JSM 6700F, Japan) was used to investigate the surface morphology at an accelerating voltage of 5 kv. The surface area () was calculated from the nitrogen adsorption isotherms obtained at 77 K using a NOVA 2000e apparatus.

2.4. Photocatalytic Experiment

The photocatalytic experiments were carried out in a water-jacket reactor at a constant temperature of 10°C and initiated by irradiating with a 175 W high-pressure mercury lamp, the distance between the water-jacket reactor and lamp was kept at 10 cm. In every experiment, 50 mg of test sample and 100 mL of 2 × 10−5 mol/L RhB aqueous solution were introduced in the reactor with magnetic stirring. 5 mL of the irradiated solution was extracted from the reactor at certain intervals. After centrifugal separation, the concentration of RhB was analyzed by a UV-vis spectrophotometer at  nm. The photodegradation efficiency was calculated by the equation:where represents the initial absorbance of the RhB solution and is the absorbance at time .

3. Results and Discussions

3.1. Material Characterization

The composition and crystal structure of /FC photocatalyst were identified by XRD, and for a comparison, the XRD patterns of FC and were also analyzed. As seen in Figure 1, the diffraction peaks at = 25.4°, 37.8°, 48°, 55°, and 62.6° can be perfectly indexed to those XRD patterns of anatase nanoparticles [14]. Compared with diffraction peaks of pure FC, the peak intensity of FC in /FC was obviously weakened and only two relatively narrow diffraction peaks can be observed at = 20.8° and 26.5°. XRD analysis strongly confirmed the existence of anatase on FC. The crystallite size of pure was calculated to be about 31 nm and the crystallite size of on the /FC was 12 nm, indicating that particle size was significantly decreased after its loading onto FC, which will be favorable for its improvement of photocatalytic activity and efficiency. The BET measurement indicated that the specific surface area of , FC, and /FC reached 3.235, 28.544, and 39.113 m2/g, respectively, which further suggested that the loading on FC was good for the enhanced photoactivity.

Figure 1: XRD patterns of (a) FC, (b) , and (c) /FC.

The morphology of FC, , and /FC was characterized by SEM. As seen in Figure 2(a), FC contained coarse, angular, and irregular particles. For the operational temperature range of U-GAS gasifier is 850~1000°C and FC cannot enter into the liquid state, giving rise to irregular particle shapes. The poor dispersion and obvious agglomeration were observed in the SEM image of (Figure 2(b)). It could be seen from Figure 2(c) that the porous coating was uniformly modified onto the surface of FC, indicating a successful immobilization of . Such results were consistent with the XRD analysis.

Figure 2: SEM images of (a) FC, (b) , and (c) /FC.
3.2. Photocatalytic Activity Test

The photocatalytic activity of /FC was evaluated by monitoring the degradation efficiency of RhB in aqueous solution, which was also compared with other photocatalysts, for example, and FC. As shown in Figure 3, the degradation efficiency of RhB was low in the dark and reached a ready value after 15 min, indicating that it was difficult for the degradation of RhB in the absence of light. Under UV irradiation, the degradation efficiency of RhB was significantly enhanced and increased with the increase of time. At a given time, the photodegradation efficiency of RhB on /FC was obviously higher than that on pure and FC. After UV irradiation for 90 min, the photodegradation efficiency of RhB on /FC, , and FC reached 90%, 80%, and 33%, respectively. The high photocatalytic activity of /FC may be understood from two aspects. On one hand, the modified onto FC possesses a better dispersibility and the number of photocatalytic activity sites will be increased, causing an enhanced photodegradation of RhB molecules. On the other hand, FC is strong adsorbent and can provide a high-density environment for the photocatalytic reaction, speeding up the efficiency of photocatalytic degradation [15].

Figure 3: Photodegradation efficiency curves of RhB.

Photocatalytic degradation of RhB depended on the amount of the catalyst used. Figure 4 shows the photodegradation efficiency of RhB when the concentration of /FC was varied from 0.3 to 0.7 g/L. The photodegradation efficiency of RhB increased with an increase in /FC concentration up to 0.5 g/L, and after that a further increase in catalyst concentration led to a slow decrease in the photodegradation efficiency of RhB. Such phenomena can be understood from two aspects. On one hand, the increase of /FC concentration will increase the number of photoactive sites and also the number of the RhB molecules absorbed. And a further increase of the catalyst concentration beyond 0.5 g/L may cause light scattering and screening effects, which will hinder the penetration of light and reduce the specific activity of the catalyst. On the other hand, at high catalyst concentration, it is difficult to maintain the homogeneous suspension due to particle agglomeration, which may also reduce the catalytic activity. So the photodegradation efficiency of RhB decreases gradually. In the present study, the optimum concentration of /FC is found to be 0.5 g/L for the degradation of RhB.

Figure 4: Effect of /FC amount on the photocatalytic degradation of RhB at irradiation time of 90 min. 2 × 10−5 mol/L RhB; average of three experiments (mean ± S.D.).

The reusability of the photocatalyst is of great importance in the photodegradation of organic contaminants. To evaluate the reusability of /FC, the photodegradation experiment of RhB was performed repeatedly for six times under the same experimental condition. As seen in Figure 5, the photodegradation efficiency of RhB showed a slight change and remained as high as 97.6% after 6 cycles. This indicates that /FC can be reusable with meager loss in activity during the photocatalytic oxidation of RhB molecules. The long-term storage stability was also investigated and the obtained results were shown in Figure 6. After storage for 50 days, the photodegradation efficiency of RhB on /FC decreased only 3.3% compared to the initial value. The results indicate the satisfactory reproducibility and stability of /FC towards RhB degradation.

Figure 5: Reusability of /FC. Experimental condition: 2 × 10−5 mol/L RhB; 0.5 g/L /FC, irradiation time of 90 min.
Figure 6: Long-term stability of /FC. Experimental condition: 2 × 10−5 mol/L RhB; 0.5 g/L /FC, irradiation time of 90 min.

4. Conclusions

The /FC photocatalyst was successfully obtained by the sol-gel method. The as-prepared photocatalyst had better photocatalytic efficiency and stability for degradation of RhB under UV light illumination as compared to that of the pure and FC. FC is believed to enhance the dispersibility of , improving the photocatalytic degradation performance of nanometer . The photocatalyst had a potential application to purify polluted water, and it also provided a new way for FC utilization.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

Acknowledgments

This work was supported by the National Natural Science Foundation of China (no. 51202059), the Research Foundation for Youth Scholars of Higher Education of Henan Province (no. 2013GGJS-047), the Key Foundation of Henan Educational Committee (no. 14A430014), and Foundation for Distinguished Young Scientists of Henan Polytechnic University (J2014-05) and the Opening Project of Henan Key Discipline Open Laboratory of Mining Engineering Materials (no. MEM13-4).

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