1 Applied Catalysis A General 505 (2015) 467-477 http://dx.doi.org/:10.1016/j.apcata.2015.05.011 Boosting the visible-light photoactivity of Bi2WO6 using acidic carbon additives Rocio J. Carmona1, Leticia F. Velasco2, M. Carmen Hidalgo3, José A. Navío3, Conchi O. Ania1* 1ADPOR Group, Instituto Nacional del Carbón (INCAR), Consejo Superior de Investigaciones Científicas (CSIC), Apdo. 73, 33080 Oviedo, Spain 2 Dpt. Chemistry, Royal Military Academy, Renaissancelaan 30, 1000 Brussels, Belgium 3 Instituto de Ciencia de Materiales de Sevilla (ICMS), Consejo Superior de Investigaciones Científicas (CSIC) - Universidad de Sevilla, Américo Vespucio 49, 41092 Sevilla, Spain *-Corresponding author. Tel.: +34 985 118846. Fax: +34 985297662. E-mail address: [email protected] (CO Ania).
2 Abstract We have explored the role of the physicohemical properties of carbon materials as additives to bismuth tungstate on its structure, optical properties, and photocatalytic activity for the degradation of rhodamine B under visible light. For this purpose, C/Bi2WO6 hybrid composites were prepared following two different routes: i) physical mixture of the catalyst components, and ii) one-pot hydrothermal synthesis of the semiconductor in the presence of the carbon additive. Three carbons with different properties were selected as additives: biomass-derived activated carbon, carbon nanotubes and carbon spheres obtained from polysaccharides. Data has shown the outstanding role of the acidic/basic nature of the carbon additive, and of the synthetic method on the photocatalytic performance of the resulting composites. For a given additive, the degradation rate of RhB is greatly improved for the catalysts prepared through a one-step hydrothermal synthesis, where there is low shielding effect of the carbon matrix. Carbon additives of acidic nature boost the surface acidity of the hybrid photocatalyst, thereby enhancing the photodegradation of RhB under visible light via a coupled mechanism (photosensitization, semiconductor photocatalysis and carbon-photon mediated reactions). Keywords: nanoporous carbons, heterogeneous photocatalysis, visible light, bismuth tungstate
3 1. Introduction Triggered by the low photonic efficiency of common semiconductors under visible light, many research efforts are currently being conducted on developing novel photocatalysts with enhanced activity, aiming at achieving a more efficient use of sunlight for its application in several fields such as environmental remediation or energy conversion [1,2]. Among others, bismuth-based materials and particularly Bi2WO6 have revealed as suitable alternatives to widespread used TiO2 [3-5]. Bi2WO6 has a layered structure with perovskite-like slabs of WO6 and [Bi2O2]2+ layers, shows good light absorption properties in the visible range and has been found to present good photocatalytic activity for organic compounds and dyes degradation under visible light irradiation [4-7]. However, the physical features of Bi2WO6 (surface area, morphology, particle size, crystallinity) and hence its photoactivity and stability under illumination are strongly affected by the synthesis method [4-7], constituting a major drawback of this material. Thus, improving its photocatalytic activity and stability is still needed to efficiently exploit its potentialities. On the other hand, carbon materials have been successfully used -either as additives or porous supports to semiconductorsin a number of photoassisted reactions [8-10]. Carbon/semiconductor composites display superior photocatalytic performance than bare semiconductors, and overcome the operational drawbacks associated to the recovery and reuse of nanosized catalyst powders [11]. The origin of the increased photoconversion yields of carbon/semiconductor catalysts depends on the nature of the carbon additive (e.g., nanoporous carbons, nanotubes, graphene), and has been mostly discussed in terms of: i) the enhanced visible light absorption of the carbon component, ii) an enhanced mass transfer due to adsorption in the porous support, and iii) strong interfacial electronic effects between certain carbon nanostructures and the semiconductor [8-10].
4 Recent investigations including our own have reported that the photocatalytic performance of Bi2WO6 can be enhanced by the use of certain amounts of carbon additives [12,13], although the effect of the carbon component has been barely addressed. Also, we have recently demonstrated the intrinsic photoactivity of several semiconductor-free nanoporous carbons under UV and visible light [14,15], and their ability to photogenerate O-radicals as the key aspect to achieve high photooxidation conversions of pollutants in aqueous solution [16]. Knowing this, the objective of this work was to provide a deep insight in the photocatalytic performance of hybrid Bi2WO6/carbon composites by exploring the role of the carbon additive. The novelty of this work is to clarify the effect of the characteristics of the carbon additive, in terms of structure, porosity and surface chemistry. Our results provide new insights on the photodegradation mechanism of a dye using Bi2WO6/carbon catalysts, and highlight the outstanding importance of the synthetic route followed for the incorporation of the carbon additive on the performance of the composite. To achieve this goal our approach consisted on the synthesis of carbon/Bi2WO6 composites using carbon materials with different physicochemical properties (nanotubes, spheres and nanoporous carbon). All of them are also characterized by a non-negligible intrinsic photochemical activity under UV light [15,17,18]. To obtain a deeper knowledge of the C/Bi2WO6 composites, catalysts were prepared following two different approaches: i) physical mixture of the components, and ii) through a one-pot route consisting on carrying out the hydrothermal synthesis of Bi2WO6 in the presence of the carbon additive. Rhodamine B was selected as model compound representing a recalcitrant dye frequently found in wastewater. 2. Experimental 2.1. Materials synthesis
5 Bi2WO6 (BWO) was prepared by following a hydrothermal procedure described elsewhere [12]. Briefly, about 0.01 mol of Bi(NO3)3·5H2O were dissolved in 10 mL of glacial acetic acid, and the stoichiometric amount of the tungsten precursor (0.005 mol of Na2WO4·2H2O) were dissolved in 90 mL of distilled water. These two solutions were finally mixed to form a white suspension (~pH 2), kept under stirring for 30 min, and then transferred into a Teflon lined stainless steel autoclave. The hydrothermal treatment was performed at 140 °C for 20 h. The yellowish precipitate was then filtered, repeatedly washed and dried overnight at 120 °C. An aliquot of the powders was calcined at 300 °C for 4 h (labeled as calc). For the preparation of the composites, a weight ratio of 2% was selected based on our previous studies [12]. As mentioned, two synthetic approaches were envisaged for the incorporation of the carbon additive to the semiconductor: i) physical mixture of the carbon and Bi2WO6 powders (series PM) in a mortar, and ii) through a one-pot route adding the carbon material to the precursors mixture for the preparation of Bi2WO6 (series HS). For the latter, the suspension of carbon material + BWO precursors was sonicated for 15 min and kept under stirring for other 15 min to allow a good dispersion before the hydrothermal treatment. The obtained powders displayed from brownish to grey color depending on the nature of the carbon additive and on the synthesis conditions (Figure 1). The hybrid composites were labeled as BWO/X -being X the corresponding acronym of the carbon material used as additive-, followed by the indication of the synthetic route (either PM or HS). The catalysts of the HS series were neither calcined (in air) nor annealed (inert atmosphere) above 120ºC, to avoid modifications of the carbon component arising from burning-out and/or oxidation reactions. Indeed, it is well known that carbon materials prepared through a low temperature profile (i.e., sample CS) are very prone to oxidation in air at temperatures above 200ºC, and that the composition of highly functionalized carbons (i.e., samples CL and CS)
6 can be easily modified upon thermal annealing (see Figure S1 in the Electronic Supporting Information, ESI). Several carbon additives with varied physicochemical and structural characteristics were selected in this study: a nanoporous activated carbon prepared by chemical activation of a lignocellulosic precursor (sample CL), carbon spheres prepared by hydrothermal carbonization of polysaccharides (sample CS), and commercially available multiwall carbon nanotubes (sample CNT, Nanocyl, average nanotubes diameter 9.5 nm, average length 1.5 mm, carbon purity was 90%; see also www.nanocyl.com). Further details on the carbon additives (Raman and XRD spectroscopies) are compiled in Table 1 and Figures S2 and S3. In a typical synthesis of the carbon spheres, about 250 mL of 0.5 M glucose solution was placed in a 400 mL Teflon-lined autoclave, and maintained at 180 ºC for 10 hours to allow hydrothermal carbonization of the polysaccharide. The brownish solid obtained was isolated from the solution by centrifugation, washed several times with water and ethanol and dried at 60 ºC. All the carbon materials were previously washed in distilled water in order to eliminate impurities. Selected characteristics of the carbon materials are shown in Table 1. 2.2. Characterization of the catalysts The porosity of the samples was characterized by measuring the N2 adsorption isotherms at -196 ºC in a volumetric analyzer (ASAP 2020, Micromeritics). Before the experiments, the samples were outgased under vacuum (ca. 10-3 torr) at 120 °C overnight. The isotherms were used to calculate the specific surface area, SBET and total pore volume, Vtotal; micropore volume was analyzed using the Dubinin–Radushkevich formulism (Vmicro) [19]. Elemental analysis was carried out in LECO CHNS-932 and LECO VTF-900 automatic analyzers. The hydrophobic/hydrophilic nature of the materials was characterized by the determination of the surface pH and proton binding curves by potentiometric titration. Briefly, subsamples of the
7 initial materials (~ 0.125 g) were added to NaNO3 (10mM, 50 mL) and equilibrated under stirring overnight. The suspensions are acidified in 0.1M HCl until pH 3 and titrated with 0.1 M NaOH up to pH 11 using an automatic analyzer. During the titration the suspension was purged with N2 to eliminate the influence of atmospheric CO2. The experimental data was transformed into proton binding curves, Q(H+), representing the total amount of protonated sites [20]. The morphology of the samples was characterized by scanning electron microscopy recorded using a FE-SEM apparatus (QuantaSEM, FEI), with metallic coating of the samples to obtain high quality images. The crystalline phase composition and degree of crystallinity of the samples were estimated by X-ray diffraction (XRD), using a Bruker instrument (D8 Advance) operating at 40 kV and 40 mA and using CuKα (0.15406 nm) radiation. Crystallite sizes of the different phases were estimated from the line broadening of the corresponding XRD peaks by using the Scherrer equation τ = 0.9λ/βcosθ, where λ is the wavelength of the incident X-rays, β is the full width at half maximum height in radians, and θ is the diffraction angle. The optical features of the catalysts were determined by UV-Vis diffuse reflectance spectroscopy, recorded on a Shimadzu spectrometer (UV-2501) equipped with an integrating sphere and using BaSO4 as a blank reference. Measurements were recorded in the diffuse reflectance mode (R) and transformed to a magnitude proportional to the extinction coefficient through the Kubelka-Munk function, F(R∞). X-ray photoelectron spectroscopy (XPS) measurements were carried out in a SPECS spectrometer, using Mg Kα radiation (150 W, 10 kV, 1253.6 eV) and a multichannel detector for the analysis of the core level signals of Bi 4f, W 4f, O 1s and C 1s. Binding energies for the high resolution spectra were calibrated by setting C 1s to 284.6 eV. CasaXPS software package was used for acquisition and data analysis; during data processing, a Shirley-type background correction was applied to the signal, and recorded spectra were fitted using Gauss-Lorentz functions, in order to determine the binding energy of the different element
8 core levels more accurately. The assignment of the distinct surface groups was performed upon the binding energies according to literature [21]. 2.3. Photodegradation runs The photocatalytic activity of the samples was evaluated towards Rhodamine B (RhB) photooxidation in water using a batch reactor (250 mL) illuminated with an Osram Ultra- Vitalux lamp (300 W) with sunlike radiation spectrum (the incident photon flux on the solution as measured by chemical actinometry [22] was 3.7 x 10-6 einsteins/s). All prepared catalysts were gently homogeneized in a mortar before being dispersed into the solution. Before each experiment, a catalysts loading of 1 g/L was settled in suspension with a RhB solution and allowed to equilibrate under stirring and darkness until no further adsorption took place (between ca. 2-12 hours), and hence the concentration of RhB from solution was constant (ca. 10 ppm). A constant oxygen flow of ca. 35 L/h was maintained in the solution during the photocatalytic runs. The photocatalytic reaction was followed by the evolution of RhB concentration and N-deethylated intermediates by spectrophotometry and HPLC provided with a diode array detector (C18 reverse phase column, mobile phase water (H2SO4 5mM)/methanol H2O:CH3OH = 35:65 v/v, flow rate of 0.8 mL/min, injection volume 50 ml). Aliquots of ca. 2 mL were removed periodically during the experiments and filtered (0.45 mm membrane filter) before measurement. Total organic carbon was followed also by means of a TOC analyzer (Shimadzu TOC VCPH). The stability of the carbon phase in the composites during the photodegradation reaction was confirmed by characterizing aqueous dispersions of the composites exposed to 2 hours of irradiation in the absence of RhB, with no evidences of changes in the composition or the structure of the carbon component detected by XRD and XPS analysis (Table S1, Figure S4).
9 3. Results and discussion The choice of the nanoporous carbons selected in this work for the preparation of the semiconductor/carbon photocatalysts was based on our previous studies reporting their intrinsic photochemical activity towards phenol photooxidation and their ability to generate radicals when exposed to UV light [14-18]. We herein describe their use as additives to BWO and discuss the effect on the catalytic performance of hybrid BWO/carbon composites under visible light for the degradation of a dye. 3.1 Structural and textural characterization of the materials A detailed characterization of the synthesized composites and the as-received carbon materials was carried out before the photocatalytic runs. Figure 2 shows the XRD patterns of the photocatalysts; the diffraction patterns of Bi2WO6 were well indexed to the russellite phase (JCPDS 39-0256, orthorhombic phase), constituted of a layered structure containing WO6 octahedra and (Bi2O2)2+ layers and H2O molecules [23]. For the composites of the HS series, no evidences of diffraction peaks corresponding to Bi2O3 or WO3 were observed, indicating the complete hydrolysis and assembly of the BWO precursors when the carbon component was present in the reaction medium. No other reflections associated to carbon phases (either amorphous or ordered) were seen in any of the XRD patterns of the composites. This is somehow expected due to the low amount of carbon additive (ca. 2wt.%) used in the preparation of the composites and their high dispersion in samples. However, the carbon additives themselves presented very different patterns pointing out the differences in their structural order (following the sequence: CNT>>> CL>CS, see Figure S3). The line widths of the diffraction peaks were broad in all the samples, indicating small crystalline domain sizes. Crystallite size values obtained from the Scherrer’s equation applied to the 131 plane (Table 1) were ~ 10 and 9 nm for pristine calcined and non-calcined Bi2WO6,
16 Adsorption capacities of 110, 370 and 155 mg RhB adsorbed/g were obtained for CS, CL and CNT, respectively. To understand these large differences we must have in mind that the adsorption of ionic dyes as RhB on a porous material depends not only on the porosity of the adsorbent but also on the specific interactions at the adsorbent surface involving the different charged forms. RhB is an amphoteric dye with a permanent positive charge (diethylamino group) and a negative charge upon dissociation of the carboxylic moiety. Under our experimental conditions RhB is in the zwitterionic form in the aqueous solution, with predominance of positive charges. Thus, the uptake of RhB is controlled by the electrostatic interactions between the catalyst surface and the charges of the dye [28,34]. The electrostatic interactions at the solution/solid interfaces also control the preferential orientation of the adsorbed RhB molecules [34,35]: on negative surfaces, RhB is adsorbed by the diethylamino group (positively charged), whereas for positively charged surfaces the preferred adsorption mode is through the carboxylic group of RhB. Knowledge on the adsorption modes of the pollutant on the surface of photocatalysts is of paramount importance as it may determine its photocatalytic degradation pathway [33,36]. Considering the different RhB adsorption capacities of the carbon additives, the photocatalytic runs were carried out on catalysts previously exposed to RhB under darkness, so as to allow the adsorption of the pollutant at equilibrium conditions. Hence the initial concentration of RhB in the solution was adjusted for each BWO/carbon composite so as to obtain the same value at the beginning of the illumination period (after adsorption in the dark). 3.2.2. Rhodamine B conversion Figure 6 and Table 3 show the effect of the carbon additive on the photocatalytic activity of Bi2WO6 for the photodegradation of RhB under visible light irradiation in terms of pollutant conversion and mineralization (evaluated by the TOC values) from the solution. First of all, it
17 should be pointed out that degradation of RhB by direct photolysis was very low under our irradiation (Figure 6), with an overall mineralization below 5 % (Table 3). Also, it is observed that the calcination of the semiconductor has a small effect on the conversion of RhB (Figure 6, inset); conversions at short times are similar, but the calcined sample showed a less steep profile after 60 min suggesting that the degradation is gradually slowed down after some time, likely as a result of the simultaneous degradation of the intermediates along with that of RhB itself. This contrasts with the similar morphology and crystallinity of both samples (Table 1), and points out that the slight differences in surface acidity and porosity are important in the photocatalytic properties of BWO [37-39]. Secondly, with the exception of BWO/CNT, the conversion of RhB was enhanced for the composites prepared by incorporation of the carbon additive before the hydrothermal synthesis of the semiconductor (series HS). The superior photocatalytic activity of BWO/carbon composites with nominal carbon contents between 0.5 and 25 wt.% has been reported for other additives (e.g., activated carbons, graphene or glucose-derived carbons) [12,13,24]. In our case the effect was very pronounced for BWO/CS, particularly within the first 60 min of illumination leading to almost full RhB conversion. Nonetheless, the overall conversion and mineralization after 2 hours of irradiation was quite similar for all the samples. It is interesting to note that BWO/CNT composite showed lower catalytic activity than bare BWO, also displaying the lowest mineralization extent (Table 3). This shows that despite the high electron mobility of carbon nanotubes (that would anticipate a lower recombination of the photogenerated exciton), their use as additives to semiconductors does not grant a superior photocatalytic performance of the resulting composites. In our case, we believe this is attributed to the strong light absorption of the nanotubes, as revealed by the poor optical features of the composite shown in Figure 5.
18 Comparatively, a poor photocatalytic activity was obtained for the composites prepared by physical mixture of the precursor’s powders, regardless the carbon material. Conversions below 70 % were obtained for all the samples, far below those of BWO, and the effect is noticed at short illumination periods. This contrasts with the wide number of studies (including our own) on other semiconductor/carbon composites prepared by physical mixture where the effect of the carbon additive is quite the opposite [8-11]. We attribute this to the large particle size of BWO (Figure 3) compared to usually nanometric size of other semiconductors, that would limit the contact between the carbon particles and the semiconductor. All this points out the importance of the synthetic method followed to build an effective interface between the carbon and semiconductor particles and to achieve a superior photocatalytic performance with a given photocatalysts. 3.2.2. Intermediates speciation and/or degradation mechanism Regarding intermediates, the evolution of the N-deethylated compounds for the HS series of catalysts is shown in Figure 7. The concentration of poly-N-deethylated compounds (DER<DR~ER< EER<R) gradually increases with time for all the catalysts; the most N- deethylated intermediate is only detected after 60 min, showing that RhB photooxidation occurs via successive N-deethylation reactions rather than by direct chromophore cleavage [12]. The degradation mechanism follows a similar pattern for the BWO/carbon composites, indicating that the effect of the carbon additive is linked to the kinetics of the photooxidation reaction rather than to a mechanistic change. Indeed, Figure 7 shows that the rate of the successive N-deethylation reactions is enhanced for BWO/CS and BWO/CL, with almost no intermediates detected after 70-80 min, indicating a high conversion involving the total degradation of RhB (Table 3). At least twice longer times are needed to achieve similar results for BWO and BWO/CNT.
19 These findings are in good agreement with the preferred adsorption mode of RhB on the surface of the catalysts, as discussed above. Under our experimental conditions, the surface of the composites of the HS series is negatively charged (Figure 4b), thus RhB is preferentially adsorbed by the diethylamino group (positively charged) [34,40]. Consequently, the degradation of RhB is favored by the attack of the active oxygen species generated nearside the adsorption sites to the auxochromic C2H5 groups of RhB, inducing the deethylation of the alkylamine moiety. This is supported by the marked gradual hypsocromic shift in the UV-vis spectra of the aqueous dye solution (an example of the progress in the photocatalytic degradation of RhB by a catalyst of the HS series is presented in Figure S9), that is associated to the stepwise formation of N-deethylated degradation subproducts [34,40]. The strict requirements needed for the N-deethylation process (i.e., formation of the excited state of the dye and transfer of electrons from the dye to the conduction band of the semiconductor) point out the good chemical contact between the catalyst surface and the dye, provided by the incorporation of the acidic carbon additives. Additionally, the concentration of RhB faded completely after 60 min for BWO/CS and BWO/CL (HS series); this evidences that N-deethylation is not the only mechanism, as the reaction would then terminate with the formation of the fully N-deethylated intermediate. Based on the RhB conversion and high mineralization values (Table 3), degradation via the chromophore cleavage also occurs simultaneously. This seems plausible as both mechanisms are independent and can proceed side by side (Figure 8). In the case of positively charged catalyst’s surfaces (sample CNT/BWO HS and the catalysts of the PM series), the preferred adsorption mode of RhB is through the negative charge of the carboxylic moiety; as the relative abundance of negative charges on RhB aqueous solution is low, the interactions with the catalyst surface are lesser (weaker). This partially suppresses the degradation via the deethylation process (although still present as seen in Figures 7 and S7),
20 accounting for the lower conversions of these composites. Similar results have been reported for TiO2 and TiO2/SiO2 surfaces, with an accelerated degradation rate for negatively charged surfaces due to successive N-deethylation reactions [34,40]. To further analyze the effect of the nature of the carbon additive we must consider the differences between the catalysts in terms of porosity, composition and acidic nature. First of all, it should be noticed that both RhB and BWO absorb light during the photocatalytic runs [37]. As shown in Figure 5, BWO absorbs light at λ<400 nm, whereas RhB absorbs in the range 460-600 nm (Figure S9) owing to intramolecular ð-ð* transitions leading to the formation of an excited state of the dye. Consequently, the photodegradation of RhB can proceed via two different mechanisms: photocatalysis or photosensitization (Figure 8). As seen in Figure 6, direct degradation of RhB upon illumination is very low (ca. below 5 %), indicating that degradation via the photosensitized process does not occur in the absence of a catalyst. In the presence of BWO, the excited state of RhB is firstly formed and the photoelectrons are injected into the conduction band of Bi2WO6, where they can be captured by the dissolved oxygen in the solution (preventing the recombination) and leaving holes in the valence band capable of direct oxidation. The succeeding reactions involving oxygen radical species and/or direct hole oxidation would lead to the mineralization of the dye, as seen in Table 3 [29,41]. The photosensitized process would only occur if the interaction between RhB and the surface of the catalysts is strong enough to have an efficient injection of electrons from the dye to the surface of the semiconductor [42-44]. Simultaneously, the photocatalytic process initiated by the light-excitation of Bi2WO6 also takes place, leading to RhB degradation; in fact, the light-excited semiconductor reaction is usually a much faster reaction than the photosensitized degradation. In the case of BWO/carbon composites of the HS series the photosensitized mechanism would be expected due to the chemical and textural characteristics of the catalysts provided by the
21 carbon additives. The high adsorption capacity of the carbon materials and the acidic nature of the composites favor strong interactions between RhB and the photocatalyst surface in acidic materials, which is crucial for an efficient photosensitized process [37]. This would explain why the photooxidation yield obtained for BWO/CNT is similar to that of bare BWO; even though the adsorption capacity on the CNT is not negligible, the interaction between RhB and the photocatalyst surface is weak due to the basic nature of the carbon additive (Table 1 and Figure 4). Hence, the degradation is expected to occur only via the photocatalytic process. For acidic catalysts as BWO, BWO/CS and BWO/CL, the interaction between the RhB and the acidic sites seems strong enough to promote the photosensitized process, in addition to the photocatalytic one. Furthermore, according to literature, the photosensitized pathway leads to the N-deethylation of RhB, which commensurate with the evolution in intermediates seen in Figure 7, and confirms the interaction of the catalysts acid sites through the diethylamino group. Also, it should be mentioned that the carbon additives herein used showed a non-negligible intrinsic photoactivity under UV-Vis illumination due to the ability to photogenerate oxygen radical species [14-16]. The superior activity of the hybrid BWO/carbon composites studied could also be partly boosted by the carbon-photon interactions, as they are capable of propagate through the material and generate oxygen radical species nearby the adsorbed molecules [14,15]. Thus, similarly to the role of RhB, the carbon additive would act as either a photosensitizer injecting electrons to the semiconductor, or as an electron acceptor (Figure 8) contributing to enhance the charge separation (due to the delocalization of the electrons in the π-electron density of the graphenic layers) in a process analogous to that reported for deposited noble metals [45]. The charge separation ability of the carbon additives should be related to their structural and electronic properties, and hence would be favored for the composites incorporating CNT (electrical conductivity values of ca. 13, 0.22 and 0.01
22 S/cm for CNT, CL and CS, respectively). However, this trend does not explain either the superior activity of BWO/CS and BWO/CL compared to BWO/CNT, or that of HS over PM series, indicating that other factors need to be considered. We attribute the low performance of the composites prepared by physical mixture to the shielding effect of the carbon matrix (Figure 1 shows the darker color of the PM composites) incorporated outside the semiconductor particles. For the catalysts prepared by the one-pot route, the carbon particles would be embedded in the core of the semiconductor (Figure 3), reducing the shielding effect while improving dispersion and contact between both components. Summarizing, all this points out that the impact of introducing carbon additives in the formulation of semiconductors goes beyond the increased surface area and electron mobility reported in the literature [8,9,29,30]. The carbon material is capable of boosting the surface acidity of the hybrid photocatalyst, thus enhancing the photodegradation of RhB under visible light via a coupled mechanism. The incorporation of only 2 wt.% of CL and CS acidic carbons as additives renders much faster photodegradation kinetics. This is most remarkable bearing in mind that both are amorphous carbons obtained from low-cost precursors, compared to nanostructured and high-cost carbon nanotubes. 4. Conclusions We have investigated the influence of the properties of carbon additives on the catalytic performance of Bi2WO6 towards the photooxidation of RhB from solution under visible irradiation. Besides the textural and chemical characteristics of the carbon, the synthetic route chosen to incorporate the additive is important to obtain an effective interface between the catalyt’s components, and thus an enhanced photocaltytic performance. The presence of a low nominal content of carbon additives does not modify significantly the hydrothermal synthesis of the semiconductor: yield, particle morphology or crystallinity
23 remained the same, with just a small shrinkage of the particle sizes. In contrast, noticeable changes are observed in the optical properties of the composites, with an increase in the absorption in the visible range. This effect seems to be linked to the degree of evolution of the carbon additive incorporated. Regarding the photocatalytic experiments, the degradation of RhB was much faster for those composites prepared through a one-step hydrothermal synthesis than for the ones obtained by physical mixture, where the shielding effect of the carbon matrix was more pronounced. Moreover, the photocatalytic performance of the HT series was higher than for the bare BWO, with the exception of the BWO/CNT composite. The superior photoactivity of the hybrid BWO/CS HT and BWO/CL HT is likely atributed to the formation of carbon-semiconductor heterojunctions and to their acidic nature, favoring the degradation of the pollutant by a photosensitized process, in addition to the photocatalytic one. Also, the superior activity of the corresponding hybrid composites could also be partially due to the carbon-photon interactions leading to the formation of O-radicals. ACKNOWLEDGMENTS The authors thank the financial support of MINECO (grants CTM2011/23378 and CTQ2011/26617) and PCTI Asturias (Fondos Feder 2007-2013, grant PC10-002). RJC thanks PCTI Asturias for her Severo Ochoa fellowship. References [1] N. Serpone, E. Pelizzetti, Photocatalysis: fundamental and applications; Wiley Interscience, New York, 1989.
24 [2] T. Oppelander, Potochemical purification of water and air: advanced oxidation processes (AOPs): Principles, reaction mechanisms, reactor concepts; Wiley-VHC, Weinheim, 2003. [3] M.A. Henderson, Surf. Sci. Reports 66 (2011) 185-297. [4] G. Colón, S. Murcia-López, M.C. Hidalgo, J.A. Navío, Chem. Commun 46 (2010) 4809-4811. [5] J.G. Yu, J.F Xiong, B. Cheng, Y. Yu, J.B. Wang, J. Solid State Chem 178 (2005) 1968- 1972. [6] C. Zhang, Y.F Zhu, Chem. Mater. 17 (2005) 3537-3545. [7] J.W. Tang, Z.G. Zou, J. Ye, Catal. Lett. 92 (2004) 53-56. [8] R. Leary, A. Westwood, Carbon 49 (2011) 741-72. [9] J.L. Faria, W. Wang, Carbon materials in photocatalysis, in: P. Serp, J.L. Figueiredo (Eds.), Carbon materials for catalysis, John Wiley & Sons, New York, 2009, pp. 481- 506. [10] C.O. Ania, L.F. Velasco, T. Valdes-Solis, Photochemical response of carbon materials. in: J.M.D. Tascon (Ed.), Novel Carbon Adsorbents, Elsevier, London, 2012, pp. 521- 547. [11] J. Araña, J.M. Doña-Rodríguez, E. Tello Rendón, C. Garriga i Cabo, O. González-Díaz, J.A. Herrera-Melián, J. Pérez-Peña, G. Colón, J.A. Navío, Appl. Catal. B: Environ. 44 (2003) 161-172. [12] S. Murcia-López, M.C. Hidalgo, J.A. Navío, Appl. Catal. A: Gen. 466 (2013) 51-59. [13] Y.Y. Li, J.P. Liu, X.T. Huang, J.G. Yu, J. Chem. Soc. Dalton Trans. 39 (2010) 3420- 3425. [14] L.F. Velasco, I.M. Fonseca, J.B. Parra, J.C. Lima, C.O. Ania, Carbon 50 (2012) 249- 258.
25 [15] L.F. Velasco, J.C. Lima, C.O. Ania, Angew. Chem. Int. Ed. 53 (2014) 4146-4148. [16] L.F. Velasco, V. Maurino, E. Laurenti, C.O. Ania, Appl. Catal. A: Gen. 453 (2013) 310- 315. [17] L.F. Velasco, R.J. Carmona, J. Matos, C.O. Ania, Carbon 73 (2014) 206-2015. [18] L.F. Velasco, Ph.D. Thesis, University of Oviedo, 2012. Available at: http://digital.csic.es/bitstream/10261/72354/1/Tesis_Leticia%20Fdez%20Velasco 2012.pdf [19] J. Rouquerol, F. Rouquerol, P. Llewellyn, G. Maurin, K.S.W. Sing, Adsorption by Powders and Porous Solids. Principles, Methodology and Applications, second ed., Academic Press, Amsterdam, 2014. [20] J. Jagiello, T.J. Bandosz, J.A. Schwarz, Carbon 32 (1994) 1026. [21] J.F. Moulder, W.F. Stickle, P.E. Sobol, K.D. Bomben, Standard Spectra for Identification and Interpretation of XPS data, Perkin Elmer, Eden Prairie, MN, 1992. [22] H.K Kuhn, S.E. Braslavsky, R. Schmidt, Pure App. Chem. 76 (2004) 2105-2146. [23] C. Ng, A. Iwase, Y.H. Ng, R. Amal, J. Phys. Chem. Lett. 3 (2012) 913. [24] Y. Cui, L. Huiquan, H. Wenshan, F. Suhua, Z. Liangjun, Powder Technol. 247 (2013) 151-160. [25] L.W. Zhang, Y.F. Zhu, Catal. Sci. Technol. 2 (2012) 694. [26] C. Contescu, J. Jagiello, J.A. Schwarz, Langmuir 9 (1993) 1754-1765. [27] L. Yue, S. Wang, G. Shan, W. Wu, L. Qiang, L. Zhu, Appl. Catal. B: Envir. 176 (2015) 11–19. [28] H. Fu, C. Pan, W. Yao, Y. Zhu, J. Phys. Chem. B 190 (2005) 22432-22439. [29] J. Matos, A. García, L. Zhao, M.M. Titirici, Appl. Catal. A: Gen. 390 (2010) 175-182. [30] J. Araña, J.M. Doña-Rodriguez, E. Tello Rendón, C. Garriga i Cabo, C. González-Díaz, J.A. Herrera-Melián, J. Pérez-Peña, G. Colón, J.A. Navío, Appl. Catal. B: Environ. 44 (2003) 153-160.
32 Figure 4. Proton binding curves of the carbon materials, bare semiconductors and hybrid composites. 345678910 pH -1.00 -0.80 -0.60 -0.40 -0.20 0.00 0.20 Q (mmol H + /g) A) CS CL CNT BWO non calcined BWO calcined 345678910 pH -1.00 -0.80 -0.60 -0.40 -0.20 0.00 B) BWO non calcined BWO/CS HS BWO/CL HS BWO/CNT HS BWO/CS PM BWO/CL PM BWO/CNT PM
33 Figure 5. Diffuse Reflectance spectra of the synthesized catalysts. Figure 6. Rhodamine B conversion upon visible light irradiation of the catalysts prepared by incorporation of the carbon additives before the hydrothermal step (A) and by physical mixture of the powders (B). (inset) effect of the calcination treatment on the bare semiconductor. 0 255075100125 Time (min) 0 25 50 75 100 Conversion (%) A) BWO non calcined BWO/CS HS BWO/CL HS BWO/CNT HS direct photolysis 0 255075100125 Time (min) 0 25 50 75 100 BWO calcined BWO/CS PM BWO/CL PM BWO/CNT PM 0 25 50 75 100 125 0 25 50 75 100 B) 200 300 400 500 600 700 800 Wavelength [nm] 0.00 0.25 0.50 0.75 1.00 Reflectance A) BWO non calcined BWO/CS HS BWO/CL HS BWO/CNT HS TiO2 200 300 400 500 600 700 800 Wavelength [nm] 0.00 0.25 0.50 0.75 1.00 B) BWO calcined BWO/CS PM BWO/CL PM BWO/CNT PM
34 Figure 7. Evolution of RhB intermediates upon irradiation of the studied catalysts with visible light. 0 25 50 75 100 125 0 25 50 75 100 Area (a.u.) BWO 0 25 50 75 100 125 0 25 50 75 100 BWO/CS HS 0 25 50 75 100 125 Time [min] 0 25 50 75 100 Area (a.u.) BWO/CNT HS 0 25 50 75 100 125 0 25 50 75 100 BWO/CL HS R ER DR EER DER 0 25 50 75 100 125 Time [min] 0 25 50 75 100 BWO/CL PM 0 25 50 75 100 125 Time [min] 0 25 50 75 100 BWO/CS PM
35 Figure 8. Schematic representation of the different degradation routes of RhB in the presence of BWO and BWO/carbon photocatalysts. RhB* Bi 2 WO 6 Photosensitization RhB CO 2 +H 2 O O 2 •O 2 ‐ ,•OH Bi 2 WO 6 O 2 •O 2 ‐ ,•OH Vis Semiconductor Photocatalysis RhB CO 2 +H 2 O Carbon‐mediated photocatalysis Bi 2 WO 6 C ‐ ‐‐ ‐ ‐ ‐ ‐ ‐ RhB* RhB + Vis RhB CO 2 +H 2 O O 2 •O 2 ‐ ,•OH RhB + Vis Bi 2 WO 6 C RhB CO 2 +H 2 O O 2 •O 2 ‐ ,•OH Vis Bi 2 WO 6 O 2 •O 2 ‐ ,•OH Vis RhB CO 2 +H 2 O Bi 2 WO 6 C RhB CO 2 +H 2 O O 2 •O 2 ‐ ,•OH Vis C
36 Table 1. Main structural, textural and physicochemical parameters of the studied materials obtained from gas adsorption data, XRD and elemental analysis. SBET (m2g-1) Vtotal 1 (cm3g-1) Vmicro 2 (cm3g-1) surface pH d3 (nm) Band gap (eV) BWO/CS PM 28 0.104 0.008 5.5 10.6 2.68 BWO/CL PM 39 0.089 0.013 4.8 9.7 2.76 BWO/CNT PM 33 0.131 0.011 5.9 10.5 2.47 BWO/CS HS 41 0.106 0.013 4.6 8.3 2.84 BWO/CL HS 43 0.123 0.014 4.5 8.8 2.86 BWO/CNT HS 45 0.131 0.014 4.6 8.9 2.86 BWO calc 28 0.086 0.007 5.7 9.9 2.90 BWO non calc 33 0.08 0.01 4.9 9.1 2.89 CS 8 0.014 0.001 4.3 -- -- CL 1280 1.03 0.27 3.6 -- -- CNT 298 2.09 0.20 8.6 -- -- 1 evaluated at p/p0 = 0.9 2evaluated by DR method 3 crystallite size evaluated from XRD data Table 2 Surface concentration of elements (in at. % from XPS analysis) in the catalysts prepared through the one-pot synthesis (HS series) and chemical shift of the Bi 4f core level versus bare BWO. BWO BWO/CS HS BWO/CL HS BWO/CNT HS Bi (at. %) 21.4 21.0 20.8 21.24 W (at. %) 10.1 7.2 7.0 7.1 C (at. %) 1.6 38.1 44.9 27.6 O (at. %) 66.9 33.7 27.3 44.9 Chemical shift Bi 4f (eV) -- 0.1 0.3 0.2 Position Bi 4f (eV) 159.9 159.8 159.6 159.7
37 Table 3. TOC values upon 2 hours of irradiation of the studied catalysts. Initial TOC mg C/L Final TOC mg C/L Mineralization (%) [1-(Final TOC/InitialTOC)] RhB direct photolysis 6.8 6.5 4.4 BWO non calcined 6.8 0.3 95.6 BWO/CS HS 6.7 0.1 98.4 BWO/CL HS 8.2 0.3 96.4 BWO/CNT HS 6.2 1 83.9 BWO calcined 7.0 1.2 83.6 BWO/CS PM 8.0 2.3 71.4 BWO/CL PM 6.1 1.8 70.5 BWO/CNT PM 5.8 2.6 55.6
38 Supporting Information Boosting the visible-light photoactivity of Bi2WO6 using acidic carbon additives Rocio J. Carmona1, Leticia F. Velasco2, M. Carmen Hidalgo3, José A. Navío3, Conchi O. Ania1* 1ADPOR Group, Instituto Nacional del Carbón (INCAR), Consejo Superior de Investigaciones Científicas (CSIC), Apdo. 73, 33080 Oviedo, Spain 2 Dpt. Chemistry, Royal Military Academy, Renaissancelaan 30, 1000 Brussels, Belgium 3 Instituto de Ciencia de Materiales de Sevilla (ICMS), Consejo Superior de Investigaciones Científicas (CSIC) - Universidad de Sevilla, Américo Vespucio 49, 41092 Sevilla, Spain *Corresponding author. Tel.: +34 954489550/ +34 985 118846.
[email protected] (CO Ania) Figure S1. Thermal profiles of the carbon materials upon exposure to air at 300ºC, showing the effect of the calcination step in the surface chemistry of the carbon additive. Figure S2. Raman spectra of the three carbon materials used as additives. Figure S3. XRD patterns of the carbon additives used, showing the (002) and (10) bands characteristics of the structural order of carbon materials, following the sequence CNT>CL> CS. Figure S4. XRD patterns of pristine sample BWO-CL HS and after irradiation of an aqueous dispersion to explore the stability of the carbon component in the composites (irrad). Figure S5. SEM images and particle size distribution of the carbon materials used as additives. Figure S6. Nitrogen adsorption isotherms at 77K of the bare semiconductors and hybrid composites of the (A) HS series and (B) PM series. Figure S7. XPS data Bi core level of the composites of the HS series. Figure S8. Evaluation of the optical band gap by double linear fitting as the intersection of the extrapolated linear segments of the absorption edge and the photon energy axis in the experimental UV-Vis diffuse reflectance spectra. The double linear fit is a more accurate approach minimizing the fitting error in graphical data integration, as proposed in the literature [Chan et al. Inorg Chem 45 (2006) 8264]. Figure S9. Temporal evolution of the UV-vis spectra of RhB aqueous solution upon irradiation of BWO/CS HS, showing the hypsochromic shift characteristic of the formation of N-deethylated intermediates and the fading of RhB concentration after 60 min of irradiation. Table S1. Surface concentration of carbon species obtained by fitting the C 1s core level peak of the XPS spectra of composites BWO-CL and BWO-CS as received (fresh) and after irradiation of an aqueous dispersion to explore the stability of the carbon component.
39 Figure S1. Thermal profiles of the carbon materials upon exposure to air at 300ºC, showing the effect of the calcination step in the surface chemistry of the carbon additive. 100 300 500 700 900 Temperature [ºC] 0 1 2 3 DTG [%/min] CS 100 300 500 700 900 Temperature [ºC] 0 1 2 3CNT after calcination inital 100 300 500 700 900 Temperature [ºC] 0 1 2 3CL
40 Figure S2. Raman spectra of the three carbon materials used as additives.
41 Figure S3. XRD patterns of the carbon additives used, showing the (002) and (10) bands characteristics of the structural order of carbon materials, following the sequence CNT>CL> CS. 0 200 400 600 800 1000 1200 1400 2 22426282 2θ (º) Intensity (a.u.) CNT CL CS
48 Table S1. Surface concentration of carbon species obtained by fitting the C 1s core level peak of the XPS spectra of composites BWO-CL and BWO-CS as received (fresh) and after irradiation of an aqueous dispersion to explore the stability of the carbon component. Bond assignment (energy, eV) Fresh irradiated BWO-CL C-C (graphitic carbon - 284.6 eV) 59.3 62.7 C-O (phenolic, alcoholic, etheric - 286.1 eV) 13.8 13.1 C=O (carbonyl or quinone - 287.1 eV) 17.7 18.2 O-C=O (carboxyl or ester - 288.7 eV) 5.8 6.0 ππ∗ (291.0 eV) 3.4 3.5 BWO-CS C-C (graphitic carbon - 284.6 eV) 66.5 65.1 C-O (phenolic, alcoholic, etheric - 286.1 eV) 15.9 17.5 C=O (carbonyl or quinone - 287.1 eV) 6.8 7.8 O-C=O (carboxyl or ester - 288.7 eV) 7.5 8.2 ππ∗ (291.0 eV) 3.3 1.3