Zhiying Duan*,
Zhichao Wang,
Chufeng Sun,
Lianbiao Zhao and
Yanbin Wang
Chemical Engineering Institute, Northwest University for Nationalities, Lanzhou 730030, P. R. China. E-mail: zhiyingduan@163.com
First published on 16th June 2015
A photocatalyst (AC@TiO2-S) based on active carbon (AC) as a support and TiO2 as active sites has been successfully prepared through a facile, controlled sol–gel approach and characterized by Fourier transform infrared (FT-IR) spectroscopy, X-ray photoelectron spectroscopy (XPS), X-ray powder diffraction (XRD), nitrogen adsorption analysis, transmission electron microscopy (TEM) and scanning electron microscopy (SEM). Importantly, the as prepared AC@TiO2-S exhibits much higher photocatalytic activity than the catalyst AC@TiO2-G (prepared by sol–gel approach) for the degradation of methyl orange (MO) under visible light irradiation (λ > 420 nm). Additionally, this supported catalyst can be easily separated from the reaction system and reused for up to five cycles without significant loss in activity, indicating its excellent recyclability. On the basis of the results, AC@TiO2-S is promising for application in the degradation of other dyes, and the controllable sol–gel method can be applied in other fields.
Photocatalysis is an ambient-temperature process that can result in the decomposition of organic pollutants and the conversion of solar energy, and presents itself as a green chemistry technology.6 Among the various semiconductors, titanium dioxide (TiO2) has been proven to be one of the most suitable photocatalysts, largely due to its optoelectronic and physiochemical properties. Based on the advantages of high photocatalytic activity, excellent stability and low cost, TiO2 has been widely studied and applied as a photocatalyst in environmental cleaning and energy conversion.7–12 On the other hand, as reported,13 the rapid recombination rate of photogenerated electron–hole pairs within TiO2 may result in its low quantum efficiency. Therefore, if the recombination of charge carriers can be suppressed, the photocatalytic activity of TiO2 will be further enhanced. In the past decades, a large amount of effort has been devoted to modification of the photocatalytic process and improvement of photocatalytic performance.13–18 In particular, carbon–titania hybrid materials have attracted considerable interest because they can potentially offer desirable efficiency for separating electron–hole pairs.19–25 C60 can efficiently generate rapid photoinduced charge separation and relatively slow charge recombination.26 Meng et al.27 prepared a TiO2-type photocatalyst using C60, which had excellent photocatalytic activity for the degradation of Rhodamine B (RhB). Mesoporous TiO2–graphene nanocomposites were synthesized by Liu et al.19 and had good photocatalytic reactivity and tunable photocatalytic selectivity for the decomposition of methyl orange (MO) and methylene blue (MB) in aqueous solution.
Although C60 and graphene as support materials for TiO2 exhibit excellent performances, their high prices make them not ideal for mass production. In our work another carbon material, active carbon (AC), beneficial for enhancing the photocatalytic activity of TiO2 but much cheaper, was used as a support for TiO2. Its large surface area will also be helpful for the photodegradation, because photocatalytic reactions occur on the catalytic surface, which consequently necessitates the prerequisite adsorption of the targeted substrate molecule, and selective photocatalysis on the TiO2 surface is largely dependent on the adsorption selectivity.13
Initially, the TiO2 nanoparticles (NPs) were immobilized by a facile, controllable sol–gel approach. Then the structure of the synthesized catalyst (AC@TiO2-S) was confirmed by corresponding characterization means, and its catalytic activity and reusability were evaluated through the degradation of MO under visible light irradiation (λ > 420 nm), which has become one of the model reactions for testing the photocatalytic activities of various photocatalysts.
| Sample | Amount of TBT used (mL) | Phase | Gel time (min) | Calcination temperature (°C) | BET surface area (m2 g−1) | Ti content (wt%) | C content (wt%) | Ti : C (atomic ratio) |
|---|---|---|---|---|---|---|---|---|
| AC@TiO2-1 | 3.5 | Solution | 30 | 400 | 946.6 | 1.1 | 82.7 | 0.33 : 100 |
| AC@TiO2-S2 | 5 | Sol | 30 | 400 | 940.4 | 3.5 | 77.5 | 1.13 : 100 |
| AC@TiO2-S3 | 6.5 | Sol | 30 | 400 | 688.3 | 8.7 | 68.8 | 3.16 : 100 |
| AC@TiO2-S4 | 5 | Sol | 30 | 350 | 940.2 | 3.5 | 77.3 | 1.13 : 100 |
| AC@TiO2-S5 | 5 | Sol | 30 | 450 | 941.8 | 3.5 | 77.8 | 1.12 : 100 |
| AC@TiO2-S6 | 5 | Sol | 15 | 400 | 943.2 | 2.5 | 79.6 | 0.79 : 100 |
| AC@TiO2-S7 | 5 | Sol | 45 | 400 | 922.6 | 4.8 | 75.8 | 1.58 : 100 |
| AC@TiO2-G | 5 | Gel | 120 | 400 | 523.3 | 11.4 | 63.3 | 4.50 : 100 |
At the beginning of the experiment, the solution was uniform when the beam was passed through the molecular solution of the precursor of Ti. Invisible light scattering was observed due to mutual interference, and was completely offset. After formation of the colloid, the radius of the dispersed phase particles is generally between 1 and 100 nm, smaller than the wavelength of incident light. A bright red beam could be seen in a perpendicular direction to the incident light – the Tyndall phenomenon. The intensity of scattering light also increased with the increase of particle concentration. Thus during the experiment, colloid concentration could be controlled by the intensity of the scattering light. By controlling the sol, we prepared a series of catalysts (AC@TiO2-S) with well dispersed TiO2 NPs.
To determine the photocatalytic lifetime, the as-prepared catalyst AC@TiO2-S2 was recovered and reused five times for the decomposition of MO under the same conditions. After each photocatalytic reaction, the aqueous solution was filtered to recycle the AC@TiO2-S2 particles, which were washed and dried at 60 °C for next cycle.
XPS was used to further investigate the chemical elements on the surface. The full-scan XPS spectrum for the catalyst AC@TiO2-S2 is shown in Fig. 2A. Peaks corresponding to C, O and Ti are clearly observed, and the high-resolution XPS spectra of C1s, O1s and Ti2p are depicted in Fig. 2B–D. The C1s peak located at 284.6 eV mainly comes from the support material. The high-resolution XPS spectrum of O1s exhibits an asymmetric peak at 530.3 eV, which was attributed to the lattice oxygen of TiO2,31 and is consistent with previous studies of TiO2. The Ti2p XPS spectrum shows two peaks at 465.0 and 459.3 eV, corresponding to Ti2p1/2 and Ti2p3/2, respectively, which demonstrates the presence of Ti4+ in pure anatase titanium.8
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| Fig. 2 XPS spectra of AC@TiO2-S2: (A) the survey spectra of AC@TiO2-S2, (B) C1s XPS spectrum, (C) O1s XPS spectrum and (D) Ti2p XPS spectrum. | ||
The XRD patterns of the AC support material and the catalyst AC@TiO2-S are given in Fig. 3. Compared with the pattern of AC, there are five weak diffraction peaks at 25.2°, 38.4°, 47.7°, 55.1° and 63.7° corresponding to the (101), (004), (200), (211) and (204) crystal facets, which were attributed to the single phase, crystalline anatase TiO2.8 No obvious diffraction peak of rutile TiO2 was detected. The diffraction peaks were still observed with the increase of calcination temperature.
The nitrogen adsorption–desorption isotherms and pore size distributions of the AC support material and the synthesized catalysts are shown in Fig. 4. It can be seen that the AC, AC@TiO2-G and AC@TiO2-S2 exhibit type IV isotherm patterns, demonstrating that they all have a mesoporous structure (Fig. 4A). The BET surface area of AC@TiO2-S2 is 940.4 m2 g−1, which is a little higher than that of AC (931.6 m2 g−1). However, the specific surface area of the catalyst AC@TiO2-G is reduced to 523.3 m2 g−1 (Table 1). What’s more, narrow pore size distributions are observed, centered at 3.75 3.65 and 3.81 nm, respectively for AC, AC@TiO2-G and AC@TiO2-S2 (Fig. 4B). These results indicate that introducing TiO2 to the AC did not destroy the structure of the support material, which can be further confirmed by TEM and SEM analysis.
The TEM and SEM images given in Fig. 5 provide more information about the morphology and structural features of the synthesized catalyst AC@TiO2-S2. It can be seen directly that the surface of the AC is covered with well-dispersed TiO2 nanoparticles. Obvious aggregation was not observed. The average size of the TiO2 NPs is about 12 nm. In addition, the TiO2 NPs in AC@TiO2-S2 have a perfect crystal structure (Fig. 5B).
It is well-known that the preparation conditions have an effect on the performances of catalysts, so the influences of different titanium
:
carbon ratios, gel times and calcination temperatures in the preparation of the catalysts for photocatalytic activity were investigated. From Fig. 7A, it can be seen that AC has no photocatalytic activity for the degradation of MO. The AC@TiO2-S2 showed the highest photocatalytic activity among the catalysts with different titanium
:
carbon ratios. In addition, it could be seen that the catalyst prepared at 400 °C (AC@TiO2-S2) exhibited the highest photocatalytic activity, and the conversion of MO was nearly 100% after being irradiated for 150 min (Fig. 7B). A comparison of the photocatalytic activities between the samples prepared at different gel times is given in Fig. 7C. When the gel time was chosen as 30 min, the best conversion of MO was obtained. The relatively close values of degradation rate of MO for AC@TiO2-S2, AC@TiO2-S6 and AC@TiO2-S7 showed that a uniform sol has been generated. When the gel time was about 120 min, the magnetic stirring bar didn’t move and the system turned into a solid gel gradually (AC@TiO2-G). However, the catalytic activity of AC@TiO2-G was greatly reduced compared to AC@TiO2-S2, AC@TiO2-S6 and AC@TiO2-S7. After 180 min, MO had mostly not been degraded.
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Fig. 7 Temporal changes in MO concentration in the presence of catalysts prepared (A) at different titanium : carbon ratios, (B) at different calcination temperatures and (C) at different gel times. | ||
Separation and stability are very important for supported photocatalysts. Therefore the reusability of the synthesized catalyst AC@TiO2-S2 was further evaluated and the results are shown in Fig. 8A. It can be seen that the photocatalyst AC@TiO2-S2 was reused in up to five runs without significant loss of activity for the photodegradation of MO, indicating that our catalyst has excellent recyclability. However, the AC had no photocatalytic activity for the degradation of MO and the adsorption of MO for recycled AC reduced. The UV-vis diffuse reflectance spectra (DRS) of the fresh AC@TiO2-S2, used AC@TiO2-S2 (5 times) and AC are thus shown in Fig. 8B. As known, the TiO2 displays a weak absorption intensity ranging from 400 to 800 nm. However, the addition of AC induced increased the light absorption intensity in the UV and visible light regions. Compared with AC, the fresh AC@TiO2-S2 showed significant enhancement of light absorption at a wavelength of 400–800 nm. Furthermore, the AC@TiO2-S2 that had been used 5 times for photodegradation also showed enhancement of light absorption. The results of DRS indicate that the AC@TiO2-S2 has visible light photocatalytic reactivity for organic degradation and has excellent recyclability. TEM was used to get more information about the morphology and structural features of the used AC@TiO2-S2 (5 times), and the TEM images are shown in Fig. 8C and D. Consistent with the fresh AC@TiO2-S2, the TiO2 NPs for used AC@TiO2-S2 were randomly attached on the AC with perfect crystal structures, which further reveals that the AC@TiO2-S2 catalyst has excellent recyclability.
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carbon ratios, gel times and calcination temperatures in the preparation of the catalyst for photocatalytic activity were investigated. The synthesized AC@TiO2-S2 had good reusability, evidenced by being extensively recycled for five runs without any substantial loss of activity. On the basis of these results, the photocatalyst AC@TiO2-S2 is promising for application in the degradation of other dyes, and the controllable sol–gel method provides an effective approach for future industrial applications in pollution control and solar energy conversion, owning to its low cost and easy scaling up.
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