1. Introduction
More than 80% of wastewater around the world is today released to the environment without appropriate treatment [
1]. Phenolic compounds are among the possible pollutants that impact natural aquatic systems. They are used in agriculture and are present in many industrial processes, such as pulp and paper, synthesis of pharmaceuticals, oil refining, production of polymers and resins, and food processing [
2,
3,
4,
5]. As a result, phenols are now often found in wastewater and in natural water. The US Environmental Protection Agency (USEPA), the National Pollutant Release Inventory (NPRI) of Canada and the European Union (EU) consider phenols and their derivatives as priority pollutants, due to their serious impact on humans, animals and the aquatic environment [
2,
4]. Therefore, wastewater treatment plants are requested to decrease the concentration of those compounds to the safety level, namely below 0.1–1.0 ppm [
3,
4]. Since phenols and phenolic compounds are chemically stable and highly soluble in water [
3], phenols abatement is a challenge for the traditional wastewater treatment plants. In addition, advance tertiary wastewater treatment technologies are still costly and often require consumption of additional chemicals and energy [
2,
3].
In this context, solar photocatalysis has the potential to offer feasible solutions for the abatement of phenols and other emerging pollutants [
6]. Titanium dioxide (TiO
2) is the most common material for the photocatalytic depollution of water, because it is chemically stable, nontoxic, relatively inexpensive, and it shows high degradation activity under UV light [
6,
7,
8]. However, the main drawbacks of TiO
2 photocatalysts are wide band bap energy (3.2 eV), which allows exploiting only about 5% of sunlight, and the fast recombination of electron-hole (e
−-h
+) pairs [
3,
6]. Recently, the use of graphene in combination with semiconductor materials, such as TiO
2 [
5,
6], has shown large potential for the photocatalytic depollution of both water and air. Indeed, the combination of graphene-based structure with TiO
2 can narrow the band gap energy and decrease of the rate of e
−-h
+ pair recombination [
6,
9], resulting in a wide light absorption range: from UV to visible light. Therefore, the synergy of GO with TiO
2 and enhanced efficiency in the photodegradation of organic pollutants can be achieved by using the GO-TiO
2 composites.
As reported in our previous work [
10] and by other authors [
6,
9,
11], in-situ nucleation and growth of TiO
2 nanoparticles on GO sheets allows achieving strong Ti-O-C chemical linkage between the two materials, and thus enhances photocatalytic activity. The synthesis conditions have a strong impact on the structure of the photocatalysts, and therefore on their ability to degrade water pollutants [
12]. For instance, the pH of the reaction mixture can allow a strong electrostatic interaction between TiO
2 and graphene oxide [
3,
10,
13]. In addition, graphene oxide is partially reduced during synthesis, due to the reaction temperature and to the interaction of its functional groups with the surface of TiO
2 particles [
5,
9,
14,
15,
16], thus photocatalytic activity is improved by the surface bonding, which facilitates electron transfer from TiO
2 to the graphene-based electron acceptor [
17].
The photodegradation activity is not only affected by the interface bonding between GO sheets and TiO
2 nanoparticles, but also by the GO loading. Indeed, a higher amount of GO can lower the photodegradation rate, because the excess of GO can prevent light to reach the TiO
2 photocatalytic centers [
17,
18,
19]. Conversely, enough GO should be added to establish a wide interface with TiO
2 nanoparticles [
20]. In this work, the TiO
2 photocatalysts was loaded with GO in different weight ratios (0–1.0 wt %) to study the impact of different GO loading over the TiO
2 photocatalyst. The structural features and the photocatalytic activity of the new materials were investigated. Over the past years, GO-TiO
2 photocatalysts have been mostly tested by degradation of organic dyes. However, most of the emerging organic pollutants are often less prone to mineralization by photocatalysis than the common organic dyes, having a different electron structure and a less extended conjugation [
21,
22,
23]. Hence, in this study, we used phenol as model pollutant and we performed photocatalytic tests under simulated sunlight, as this is the most convenient way to use photocatalytic oxidation in real wastewater plants. Furthermore, since there are concerns about synthesis reproducibility when different reactors are used, two fabrication methods were used: (a) the reaction mixture was stirred in a closed Pyrex beaker; and (b) GO-TiO
2 suspension was kept in a static Teflon vessel. Thus, it was possible to compare the morphology and the photocatalytic performances of the materials prepared under stirring and in static conditions.
2. Experimental Section
After preparing graphene oxide (GO) via a modified Hummers method from a natural graphite powder (UF2 99,5 Graphit Kropfmühl GmbH, Hauzenberg, Germany) as described elsewhere, [
10], the graphene-titanium dioxide (GT) composites were synthesized by two methods, namely in static conditions (GTS) and in a stirred tank (GTD), and their properties were compared. All chemicals used for the synthesis of the nanocomposites were purchased from Sigma-Aldrich (St. Louis, MO, USA), unless otherwise specified.
2.1. Synthesis of the GT Composites
The ratios of TiCl4/GO/H2O in the synthetic mixtures were calculated to obtain a final GO + TiO2 concentration of 1.0 g/L. In short, a freeze-dried GO powder was dispersed at 0.01 wt % in ultrapure water (resistivity ≥ 18 MΩ cm) by high power ultrasonication in a cold bath for 3 h. The concentration of the GO suspension was adjusted with ultrapure water according to the above calculation to total volume of 100 mL. The mixture was sonicated for 30 min and then stirred in an ice bath for 30 min. TiCl4 (98% purity) was added under vigorous stirring for 1 h in the ice bath. After allowing the mixture to reach room temperature, the pH was adjusted to 6.0 with NH4OH (25% in water), and maintained at this value for 2 h. For the static (S) process, the mixture was transferred to Teflon-lined autoclave, maintained at 100 °C for 4 h in an oven and let cool overnight. In the dynamic (D) method, the suspension was heated at 100 °C for 4 h and cooled down to room temperature with continuous stirring for 18 h. After this, GT nanocomposites were collected by centrifugation and cleaned with ultrapure water until no chloride ions were detected by the silver nitrate test (0.1 M AgNO3 solution) on supernatant. Finally, the precipitation was washed with ethanol and dried in vacuum at 40 °C.
GT photocatalysts with theoretical GO loading of 0.05, 0.1, 0.2, 0.5 and 1.0 wt %, named 0.05GTS, 0.1GTS, 0.2GTS, 0.5GTS and 1.0GTS, respectively, were prepared by the static process Samples 0.05GTD and 1.0GTD (0.05 and 1.0 wt % GO loading, respectively) were synthesized with under stirring conditions. A pure TiO2 reference, TS, was prepared by the statistic method, in the same conditions used for the GTS composites with no GO in the starting mixture.
2.2. Characterization of the GT Composites
The morphology of the samples was characterized by high-resolution transmission electron microscopy (HRTEM) over a JEOL 3010-UHR instrument (Tokyo, Japan). The crystalline phase and the TiO
2 crystallites size were investigated by a PANAnalytical Empyrean diffractometer (Almelo, The Netherlands), operating at 45 kV and 40 mA, with Cu Kα radiation (λ = 1.5418 Å). Both reflection spinner and SAXS (small angle X-ray scattering) stage were used. SAXS measurements were performed over 5.3 × 10
−3 Å
−1 and 3.5 × 10
−1 Å
−1 for studying the size distribution of the titania particles. The X-rays diffraction (XRD) patterns of the powdered samples were acquired in a 2
θ range from 5° to 70°. Reference cards, PDF 01-021-1272 of anatase and 01-029-1360 of brookite, were chosen for peak analysis [
24]. The fraction of the anatase phase,
, over the total crystalline material (anatase and brookite) was calculated by Equation (1) [
25,
26].
where
is the integrated intensity of anatase phase highest peak (101),
is the integrated intensity of brookite phase highest peak (121), and the coefficients
and
are 0.886 and 2.721, respectively [
10]. The deconvolution technique was used for anatase and brookite peak separation due to their overlapping. After baseline subtraction, the XRD pattern was fitted by Lorentzian function over the Fityk 0.9.8 (freeware software developed by Marcin Wojdyr). By doing that, it was assumed that the broadening of the three main peaks of brookite is the same [
24].
XPS spectra were obtained by an ESCALAB 250Xi X-ray photoelectron spectrometer (Thermo Fisher Scientific, Waltham, MA, USA) using Al Kα radiation. The diffuse reflectance spectra in the range 200–800 nm were measured by UV-visible Spectrophotometer, PerkinElmer Lambda 1050 (Waltham, MA, USA), with an integrating sphere using BaSO
4 as a reference material. The band gap energy was obtained from the Tauc plot of the Kubelka-Munk (K-M) function [
27,
28,
29]:
where
is the absorption coefficient of the solid at a certain value of wavelength (
),
h is Planck’s constant,
is the proportionality constant,
is the frequency of light and
is the band-gap energy.
2.3. Photocatalytic Tests
Phenol was used as the model pollutant for studying the photodegradation activity of the GT composites under sun simulator. The set-up of photocatalytic experiment is shown in
Figure 1a: the photocatalytic double wall cell was made of borosilicate glass (capacity 30 mL) with a quartz window cap (
Figure 1b, diameter 30 mm) to exploit the simulated sunlight. A control cell with the same dimensions was used for tests in the dark and therefore was covered with a polypropylene blind cap. The solar light was generated at 1000 W/m
2 intensity by a 300 W xenon lamp (model LS0306, LOT QuantumDesign, San Diego, CA, USA) and the calibration was done before testing with a Si reference solar cell (Model LS0042, ReRa Solutions, Nijmegen, The Netherlands). The lamp was set up above the photocatalytic cell at a distance of 100 mm from the surface of the sample. The temperature for the photodegradation experiment was controlled by water circulation at 22 ± 1 °C.
The GT composites were dispersed in ultrapure water at concentration 1000 ppm with ultrasonication until well dispersed. After that, the sample suspension and 20 ppm phenol solution with ratio 1:1 were mixed in the photocatalyst cells without light for 30 min, because we observed that after this time adsorption-desorption equilibrium was reached. Then, the test suspension was exposed to the simulated solar light and the samples were collected at the specific time intervals throughout 180 min. The collected samples were filtrated through 0.45 μm cellulose filter. The sample solutions were analyzed via High Performance Liquid Chromatography (HPLC, Dionex with Chromeleon 6.80 software (Thermo Fisher Scientific, Waltham, MA, USA) with a Luna® 5μ C18(2) 100Å column (Phenomenex, Torrance, CA, USA), 250 × 4.60 mm2. KH2PO4 (0.025 M) solution and acetonitrile with ratio 40:60 were used as mobile phase.
The apparent rate constant for the photodegradation tests (
) [
29,
30] was obtained from the plot of −(
) against with time (minutes), i.e., according to a first-order kinetic:
where
is the apparent kinetic constant of pseudo-first order,
is the starting concentration and
is the concentration at the reaction time (
).
4. Conclusions
GT composites were synthesized by the sol-gel method with two different reactor configurations: (a) stirring mixture in Pyrex beaker; and (b) a static condition in autoclave vessel. GO loading was varied from 0 to 1.0 wt %. All materials were prepared at 100 °C and consisted of TiO
2 particles with polyhedral shape and 8–9 nm crystallite size, agglomerated on GO monolayers. XRD analysis revealed that all samples were mixtures of anatase and brookite phases, with a prevalence of anatase (around 75–80%). GT composites prepared with different methods but same GO loading showed similar morphology. XPS analysis suggested the formation of Ti-O-C interface bonding, because the peak corresponding to the oxidized carboxylic groups in the GT composites shifted towards higher binding energy, compared to the starting GO. Moreover, all GT composites showed a bathochromic shift of their absorption edge (from 376 nm to 388 nm), thus showing higher ability to exploit solar light (lower ban gap). Nevertheless, the photodegradation efficiency of the GT composites decreased with the GO loading. There are two possible reasons for that [
38]: Firstly, GO acted as a light absorber, thus competing with the TiO
2 photocatalytic centers [
39,
40]. Secondly, at high loading, GO acted as a charge carrier recombination center, thus facilitating the electron–hole pare recombination [
18,
41]. Therefore, our study stressed the importance TiO
2-GO interface for substrates such as phenol, which shows no significant adsorption on GO, a common feature of most water micropollutants. Moreover, our study showed that the different methods, i.e. dynamic and static mixing in the reactor, did not influence the morphology and chemistry of GT nanocomposites. The photocatalytic activity was ruled mainly by the GO loading.
In this work, we prepared GT composites economically, with low-energy and low-chemical consumption, nearly neutral pH, and environmentally friendly syntheses. Our materials can be produced with a constant structure, even by using different types of reactor for the synthesis. The synergy between GO and TiO2 appeared to depend on interface. Therefore, the materials with the highest phenol photodegradation activities were those with 0.05 wt % GO loading. On the contrary, materials with GO loading higher than 0.5 wt % had lower activity than the pure TiO2 reference.