R. Giovannetti*a,
E. Rommozzi
a,
M. Zannottia,
C. A. D'Amato
a,
S. Ferraroa,
M. Cespib,
G. Bonacucinab,
M. Minicuccic and
A. Di Ciccoc
aSchool of Science and Technology, Chemistry Division, University of Camerino, Via S. Agostino 1, 62032 Camerino, Italy. E-mail: rita.giovannetti@unicam.it
bSchool of Pharmacy, University of Camerino, Via S. Agostino 1, 62032 Camerino, Italy
cSchool of Science and Technology, Physics Division, University of Camerino, Via Madonna delle Carceri 9, 62032 Camerino, Italy
First published on 23rd September 2016
The aim of this study was the preparation of a graphene/TiO2 heterogeneous catalyst supported on polypropylene for visible light photocatalysis. Aqueous graphene dispersions were prepared by liquid-phase exfoliation of graphite in the presence of a non-ionic surfactant, Triton X-100. The obtained graphene dispersion was characterized by X-ray diffraction, dynamic light scattering and UV-Visible spectroscopy and was subsequently used for the preparation of graphene/TiO2 photocatalyst. As-prepared photocatalysts were tested for the photocatalytic degradation of a refractory dye, Alizarin Red S, in water solutions as target pollutant. Graphene/TiO2 nanocomposites showed higher adsorption of Alizarin Red S on the catalyst surface and higher photocatalytic activity for its degradation under visible light irradiation, in respect to those obtained with pure TiO2.
The chemical nature of carbon in these materials comes from its hybridization states, which also determines the features of a variety of organic compounds.2 Allotropes of carbon such as 0D fullerenes,3 1D carbon nanotubes4 and 3D graphite and diamond5,6 have been known for a long time.
The mother element of some carbon allotropes is graphene. Graphene is the 2D building block for all other dimensionalities of carbon materials. It can be wrapped up into 0D fullerenes, rolled into 1D nanotubes, or stacked into 3D graphite.7
The production of graphene in large quantities is an ongoing challenge for large-scale applications. Different processes are used to produce graphene from graphene oxide and need strong oxidizing and reducing agents. However, graphene fabricated under these chemical conditions tends to have a certain number of structural defects.8 For that purpose, top-down methods such as the exfoliation of graphite powder in liquid-phase by sonication are a very promising routes due to their simplicity, versatility and low-cost;9 besides, ultrasound treatment offers a suitable option to create high-quality graphene in great quantity.8
The direct exfoliation of graphite and a good dispersion of the resulting graphene sheets need to use stabilizers to prevent their stacking. Various stabilizers have been proposed, in both organic and aqueous media, such as ionic and non-ionic surfactants,10 ionic liquids,11 polymers,12 organic salts13 and aromatic molecules.14
Graphene with the thickness of a single carbon atom owns unique physical and chemical properties including highly flexible structure,15 large surface area,16 high electrical and thermal conductivity17,18 and high chemical stability. Moreover, electrons in graphene have a linear relation between energy and momentum, so its band structure has no energy gap.19 Accordingly, graphene is an attractive material in applications that require a fast electron transfer, such as energy storage20,21 and photocatalysis.22,23
TiO2 photocatalysis has emerged as a promising technology that could decisively contribute on the decrease of environmental pollution based on the utilization of solar energy. TiO2 is mainly active under UV light irradiation due to its wide band gap (3.2 eV); considering that the percentage of UV light is less than 5% of the total solar spectrum incident on the earth, in recent years research has focused on the exploration of photocatalysts which would respond in the visible light region.24
Because of their properties, it has been reported that graphene based semiconductor nanocomposites are considered as good photocatalyst for pollutant degradation.25 Graphene is an ideal nanomaterial for doping TiO2 thanks to the formation of Ti–O–C bonds that extends the visible light absorption of TiO2. Moreover, electrons are easily transported from TiO2 to the graphene nano-sheets and the electron–hole recombination is significantly reduced, enhancing the oxidative reactivity.26
To test photocatalytic activity of new materials based on TiO2, a high number of studies uses dyes as target pollutants.23,27–30
In our previous study we have successfully used polypropylene (PP) coated TiO2 in the visible light photodegradation of Alizarin Red S (ARS) obtaining efficient dye degradation, with addition advantage of easy separation of photocatalyst and possibility of reuse.31 ARS is a common water soluble anthraquinone dye extensively employed for cotton and silk dyeing and also used in clinical practices and in geology.32 Due to synthetic origin and complex structure of aromatic rings, ARS is considered refractory pollutant difficult to remove by general chemical, physical and biological processes.33 For this, wide ranges of technologies have been developed to remove this dye from wastewaters applying catalytic and photochemical methods.34
In this work, in order to obtain higher efficiently material, graphene/TiO2 heterogeneous catalysts supported on polypropylene (PP) were prepared and investigated for the first time as visible light photocatalysts in water. To reach this aim, an aqueous solution of Triton X-100 has been used for the direct exfoliation of graphite by sonication to obtain graphene (GR) dispersion. Triton X-100 is a non-ionic surfactant able to work as dispersing agent and as stabilizer to prevent layer stacking. Graphene/TiO2 heterogeneous catalysts supported on polypropylene (PP@GR–TiO2) were prepared from the GR dispersion. PP@GR–TiO2 nanocomposites were used to treat water with ARS as target pollutant by photocatalytic reaction under visible light.
| Number test | Graphite (g) | Solvent (mL) | Ultrasonic bath (h) | Ultrasonic probe (h) |
|---|---|---|---|---|
| 1 | 0.5 | 50 | 4 | 1 |
| 2 | 0.2 | 100 | 5 | — |
| 3 | 0.2 | 100 | 9 | — |
After ultrasonic treatments, dispersions were first centrifuged with a centrifuge Hermlez 323 K for 30 min at 3150 rpm and then for 30 min at 5150 rpm to sediment non-exfoliate graphite and to collect the GR dispersion. To obtain concentration data, a precisely measured volume of dispersion was filtered under high vacuum onto a polycarbonate membrane of known mass. The resulting film was washed with 25 mL of water, dried at room temperature and the mass was then determined using a microbalance.
Different samples were prepared by H2O dilution and by addition of various amounts of Triton X-100 to obtain the same surfactant concentrations and analysed by Dynamic Light Scattering (DLS) and UV-Visible (UV-Vis). DLS analysis was performed using Malvern Zetasizer nano S (Malvern instrument Worcestershire, UK) equipped with a back-scattered light detector operating at 173°. UV-Vis characterization was carried out with a Cary 8454 Diode Array System spectrophotometer (Agilent Technologies Measurements).
Successively, photocatalysts were supported on PP strips through dip coating technique, dried and clean with diluted HCl to remove the excess of TiO2 particles.
Adsorption and photodegradation processes were monitored by UV-Vis, in real-time mode every 7 minutes, using a quartz cuvette in continuous flux (Hellma Analytics, 178.710-QS, light path 10 mm) connected through a peristaltic pump Gilson miniplus 3 to the photo reactor.
In order to obtain a structural characterization of GR, the dispersion was filtered and XRD measurements were carried out. In Fig. 2 XRD patterns of SFG44 graphite, SFG44 exfoliated graphite and its smoothed pattern were reported. In this figure (pattern c) is visible a broad peak (002) related to the periodic lamellar structure of graphite, that suggests a strong reduction of the long-range periodicity associated with the c-axis of graphite. However, after the exfoliation treatment, the other peaks of SFG44 graphite decreased significantly or disappeared. This confirm the loss of crystallinity of graphite structure after the ultrasound treatment and a random packing of graphene sheets.
In order to identify the best condition for the preparation of GR dispersions, DLS analysis was performed. In Fig. 3 are reported DLS spectra of GR dispersions obtained as a function of different preparation conditions (Table 1), with different GR concentrations, from 3.00 to 30.00 mg L−1 as reported in map legend, and with the same surfactant concentrations in all samples. All traces show the presence of three peaks. The peak at about 10 nm is associated to Triton X-100, that centred at about 220 nm is associated to GR, while the peak at about 5.56 μm is associated to non-exfoliate graphite remained at the end of the exfoliation process.
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| Fig. 3 DLS spectra of GR dispersions obtained by test number 1, 2 and 3 (Table 1) respectively; in the map legend GR concentrations in mg L−1 of all samples are reported. | ||
GR dispersion obtained by the test number 1 showed DLS spectra where the Triton X-100 and GR are characterized by peaks with different positions, width and, in same case, also shape; this is probably due to the high initial concentration of graphite and to the short ultrasonic time. GR dispersions obtained by test numbers 2 and 3 instead showed DLS spectra characterized by reproducible size distributions for Triton X-100 and GR. In addition, spectra of GR dispersions obtained by test number 2 were characterized by peaks of GR having a higher intensity compared to those obtained by the test number 3. This indicates that the condition applied in the test number 2 provided more concentrated GR dispersion in aqueous medium. For this reason, GR obtained at these conditions was further characterized and then applied in photocatalytic experiments. The GR concentration obtained by high vacuum filtration of a precisely measured volume of this dispersion was 30 mg L−1.
Fig. 4 illustrates UV-Vis absorption spectra obtained by various dilutions with water up to 10 mL of as prepared exfoliated GR dispersion (in the map legend were reported dilution factors of all samples). Triton X-100 concentration varied from 1.284 to 0.032 g L−1 while GR concentration varied from 0.300 to 0.008 mg L−1.
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| Fig. 4 UV-Vis absorption spectra of different amounts of GR dispersion obtained by dilution with water; in the map legend dilution factors (D.F.) of all samples are reported. | ||
As it may be observed in the Fig. 4, spectra showed three different groups of bands in the region 190–290 nm (signed as λ1, λ2 and λ3) with changes in wavelength and intensity for any specific Triton X-100 and GR concentration.
A detailed analysis of λ2 showed a wavelength shift of the different dilutions of GR dispersion as function of Triton X-100 concentration (Fig. 5). In particular, a blue shift from 237 nm to 220 nm was firstly obtained when Triton X-100 concentration moved from 1.284 to 0.214 g L−1, while a red shift from 220 nm to 223 nm was then observed at lower Triton X-100 concentration.
In the spectrum of Fig. 4 absorption bands at around 270 nm (λ3), owing to π–π* transitions of graphene,35 for all dispersions were observed; the intensity of these bands depends by the GR amount and decreases according to the increase of dilution with water. It is possible to establish a linear Pearson relationship (adjusted determination coefficient = 0.99122) between the concentration of GR in H2O/Triton X-100 solvent and the intensity of the corresponding absorbance spectrum at 270 nm as reported in Fig. 6.
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| Fig. 6 Pearson correlation between GR concentration (mg L−1) and the intensity of the corresponding absorbance at 270 nm. | ||
To better understand the observed behaviour, the GR amount was keep constant varying only the Triton X-100 concentration. Fig. 7 illustrates UV-Vis absorption spectra obtained by dispersion of 0.008 mg of as prepared exfoliated GR with different amounts of Triton X-100 (in the map legend were reported the Triton X-100 concentration in g L−1 of all samples). In this case, the obtained spectra showed that, although the amount of GR is the same, the intensity of absorption band at around 270 nm increases with the increase of amount of Triton X-100. In addition, changes in wavelength and intensity were observed in the bands at around 190 and 240 nm at specific Triton X-100 concentrations.
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| Fig. 7 UV-Vis absorption spectra obtained by 0.008 mg of GR with different amounts of Triton X-100; in the map legend Triton X-100 concentration in g L−1 of all samples are reported. | ||
A detailed analysis of λ2 showed the change of wavelength as function of Triton X-100 concentration as reported in Fig. 8. A red shift from 224 nm to 236 nm was obtained with the increase of Triton X-100 concentration. This spectral change can be probably due to different interaction of Triton X-100 on exfoliated GR planes.
From the analysis of wavelength shifts, it is possible to deduce that the increase of surfactant concentration gives a red shift, while a blue shift is observed by increasing water. This behaviour is probably due to the variation of aggregation degree of graphene layers, depending to solvent composition. In particular, surfactant molecules balance the inter-sheet attractive forces of graphene flakes.
To confirm this hypothesis, DLS analysis was performed on samples prepared by various H2O dilutions in which GR concentration varies from 3.0 to 30.0 mg L−1 while Triton X-100 concentration varies from 0.128 to 1.284 g L−1.
Obtained spectra are reported in Fig. 9a. Analysing the central peak, it is possible to note a rightward shift (towards greater sizes) when the amount of water increases. Plotting the size change versus surfactant concentration (Fig. 9b), it is clearly visible a GR size increase although the total amount of GR decreases with the dilution. This behaviour can be explained considering that to a minor size correspond a higher Triton X-100 concentration.
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| Fig. 9 DLS spectra of samples prepared by various H2O dilutions (a); size (nm) versus Triton X-100 concentration (g L−1) (b). In the map legend dilution factors (D.F.) of all samples are reported. | ||
DLS was also performed on GR dispersion with a GR concentration from 3.0 to 30.0 mg L−1 at constant Triton X-100 concentration (Fig. 10a). The different % of the intensity of both Triton X-100 and GR peaks is associated to the different amount of GR in samples. In fact, at an increase of GR concentration corresponds an increase in intensity of the peak at 220 nm (associated with GR) without any variation of size, and a simultaneous decrease of the peak at 10 nm (associated with Triton X-100). This effect is shown in Fig. 10b.
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| Fig. 10 Effect of GR concentrations (mg L−1) on DLS spectra (a); intensity% of both GR and Triton X-100 versus GR concentration (mg L−1) (b). | ||
Obtained results show that the exfoliated GR sheets have a size in the range 164–255 nm as a function of the Triton X-100 amount. Specifically, higher concentration of surfactant is necessary to reduce the graphene layers aggregation.
In the first step, in order to obtain information about dye adsorption process and equilibrium data, different starting ARS concentrations were used. The resulting absorbance changes were monitored at 424 nm for different ARS concentrations and analysed by linear forms of Freundlich (1) and Langmuir (2) isotherms models.31
| Qe = kFCe1/n | (1) |
![]() | (2) |
In these equations, Ce is the ARS concentration in solution, Qe is the concentration of ARS adsorbed on PP@mgGR–TiO2 at the equilibrium, kF is a constant value that represents the ability of adsorption, and 1/n is the adsorption intensity; kL and aL are the Langmuir constants.
The relationship of adsorption data of PP@mgGR–TiO2 with Freundlich and Langmuir isotherms are reported in Fig. 11. The experimental data fit well with the Freundlich isotherm model (adjusted R2 = 0.976) generating a kF of 2.00 and 1/n of 1.38, confirming that, in the adsorption process of ARS on PP@mgGR–TiO2, multilayer adsorption mechanism can occur as in the case of only TiO2.31
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| Fig. 11 Linear regression analysis of data using the Freundlich (a) and Langmuir (b) isotherms models. | ||
The adsorbed concentration change of ARS on different PP@mgGR–TiO2, is reported in Fig. 12 as function of time.
The analysed results followed a pseudo first order kinetic as expressed by eqn (3):31
![]() | (3) |
| Catalyst name mgGR@TiO2 | kads × 102 (min−1) | Adj. Rads2 | kphoto × 103 (min−1) | Adj. Rphoto2 |
|---|---|---|---|---|
| PP@TiO2 | 2.54 | 0.9967 | 7.70 | 0.9960 |
| PP@0.03GR–TiO2 | 3.28 | 0.9981 | 9.70 | 0.9949 |
| PP@0.06GR–TiO2 | 3.31 | 0.9966 | 11.5 | 0.9920 |
| PP@0.12GR–TiO2 | 3.30 | 0.9986 | 11.2 | 0.9924 |
| PP@0.18GR–TiO2 | 3.31 | 0.9996 | 12.5 | 0.9939 |
Trends of the absorbed ARS concentration (Cads) at the end of adsorption process and kads versus mg of GR were reported in Fig. 13. All results showed that the presence of GR in TiO2 influenced positively the absorption kinetics of ARS respect to pure TiO2 but, in the range from 0.03 to 0.18 mg of GR, kads values were similar for all catalysts. On the contrary, with the increases of GR, in PP@mgGR–TiO2, an increase of Cads were observed for the concomitant GR adsorption due to π–π interactions and to increasing of absorption surface area. These nanocomposites showed higher adsorption performance of ARS respect to pure TiO2 and the relationship between Cads and the amount of graphene into catalysts can be described as a second order polynomial equation Cads = 3 × 10−7 mgGR2 to 4 × 10−7 mgGR + 5 × 10−5 with an adjusted determination coefficient of 0.998.
After ARS adsorption in dark conditions, in the second step, PP@mgGR–TiO2 catalysts were utilized for photocatalytic degradation of ARS as a model reaction under visible-light. In Fig. 14 are reported the photodegradation of ARS during time for different PP@mgGR–TiO2 photocatalysts, showing the positive effects of the presence of GR.
Kinetic evaluation of the photodegradation process of ARS showed that all as prepared PP@mgGR–TiO2 catalysts follows first order model according to the eqn (4)31
![]() | (4) |
The plot of the first term of eqn (4) versus photodegradation time gives kphoto and adjusted R2 values reported in Table 2. All results showed that, also in the photodegradation process, the presence of GR in TiO2 influences positively photodegradation kinetics respect to pure PP@TiO2 as demonstrated by the increase of kphoto values. While kads values were similar for all catalysts, the enhance of photocatalytic performance can be attributed of productive interaction between GR nano-sheets and TiO2 in which the photogenerated electrons of TiO2 are transferred on GR that act as electron acceptor inhibiting the electron–hole recombination.36
Obtained results prove that the addition of GR dispersion in the formulation of TiO2 paste promote, thanks to the favourable interaction with Triton X-100, the homogeneity of GR and TiO2 with consequent positive effect in efficacy of PP@GR–TiO2 photocatalyst. By modulation of GR concentration in the paste formulation is therefore possible to increase the ARS absorption and the rate of photodegradation.
By previous study, by using PP@TiO2,31 photodegradation constant values were inversely proportional to the initial ARS concentration, showing that the increase of adsorbed dye on the photocatalyst decelerates the rate of the process. In this case, although the adsorbed ARS concentration increases on the PP@GR–TiO2 due to positive effect of graphene, the obtained kphoto values showed the improvement of performance of this new photocatalyst.
A schematic representation of the mechanism of graphene/TiO2 photocatalysis for ARS degradation is reported in Fig. 15.
The presence of different amounts of GR showed positive effects increasing the adsorption of ARS on the catalyst surface, together with higher photocatalytic activity for dye degradation under visible light irradiation, respect to those obtained with pure PP@TiO2.
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