Abstract
In this work, the oxidation of methylene blue textile dye in the presence of hydrogen peroxide, using niobium oxide impregnated with different proportions of tin (1, 5 and 10% in mass) as catalyst was studied. The materials were characterized by TPR, XPS, XRD and FTIR. The oxidation tests monitored by ESI-MS showed that the composite containing the higher amount of tin was the most efficient in the removal of the dye. The XRD, XPS, and TPR data presented evidence of the formation of the tin-niobium oxide composite containing Sn0 and supported SnO2.
niobium oxide; tin; organic dye
ARTIGO
Utilization of Sn/Nb2O5 composite for the removal of methylene blue
Fabiane de Oliveira Cantão*; Walclée de Carvalho Melo; Luiz Carlos Alves Oliveira; Aline Ribeiro Passos; Adilson Cândido da Silva
Departamento de Química, Universidade Federal de Lavras, CP 3037, 37200-000 Lavras - MG, Brasil
ABSTRACT
In this work, the oxidation of methylene blue textile dye in the presence of hydrogen peroxide, using niobium oxide impregnated with different proportions of tin (1, 5 and 10% in mass) as catalyst was studied. The materials were characterized by TPR, XPS, XRD and FTIR. The oxidation tests monitored by ESI-MS showed that the composite containing the higher amount of tin was the most efficient in the removal of the dye. The XRD, XPS, and TPR data presented evidence of the formation of the tin-niobium oxide composite containing Sn0 and supported SnO2.
Keywords: niobium oxide; tin; organic dye.
INTRODUCTION
Industrial activity causes numerous environmental problems; water contamination by organic molecules is a good example. The growing development of the textile industry is a great contributor, because a large part of these pollutants is dye generated by this type of industry.
Due to their own nature, the dyes are easily detected by the naked eye, being visible in some cases at concentrations as low as 1 mg L-1. That behavior presents advantages and disadvantages, because a small amount thrown in aquatic effluents can cause an accentuated change of coloration in the rivers, but can also be easily detected by environmental control authorities.1 As a result, much effort has been made to degrade and even remove these dyes which constitute an environmental problem and a serious problem faced by modern society.2
Catalytic processes have been applied to the solution of several environmental problems, because it provides faster, low cost reactions, with higher selectivity. The interest in materials containing niobium oxides (Nb2O5) has been increasing in recent years due to the fact that this material can be applied in diverse fields of study,3 being used as a catalyst and as a catalytic support. The use of niobium oxide in Brazil becomes appealing due to its natural abundance in the country.4,5
In the search for new materials with catalytic properties, the interest in the study of the effects of oxide supported metals has been increasing. The metal-oxide interaction induces important modifications in the adsorption and catalysis properties of the metal in different reactions.6 Furthermore, its use is justified by its having a larger area of contact between the metal and the organic molecule, which is not observed using the metal alone.
The introduction of transition metals, such as tin, on the surface of different supports results in high activity and selectivity for catalysis.7 The presence of metal dispersed on the surface acts as centers that present Lewis acid characteristics, which are desired as a reinforcer of the catalytic activity. In the investigation of surface catalytic properties, the acidity/basicity stands out, because it promotes alterations in the adsorption capacity, related to the properties of the exposed sites.8
In that context, the objective of this work was the preparation of tin on niobium oxide composites. Those materials were thermically treated for the formation of Sn0 (metallic tin) seeking their use as catalysts for H2O2 decomposition and methylene blue dye oxidation.
EXPERIMENTAL
Synthesis of catalyst Sn/Nb2O5
Different amounts of tin nitrate (1, 5 and 10% in mass) were incorporate with 2 g of niobium oxide, leading to samples containing different levels of the metal. The niobium oxide was put in contact with the tin nitrate solution and the volume was completed with water to 100 mL, soon afterwards, the material was kept under constant agitation a 100 ± 1 ºC until dry. The produced solid was taken to an oven for complete drying of the material, and then calcinated, in air, at 500 ºC for 3 h. For the obtaining of the metallic tin on the niobium oxide surface, the materials were treated with N2/H2 (5%) at temperatures predetermined by temperature-programmed reduction analyses (TPR).
Characterization of catalysts
The materials were characterized by X Ray diffraction in a Rigaku Geigerflex equipment, CuKα radiation (λ = 1.54056 A°) with 40 kV and 35 mA, infrared (FT-IR) spectroscopy, Digilab Excalibur, FTS 3000 series, scanning electron microscopy (SEM), LEO EVO 40XVP, UV-Vis spectroscopy, (Shimadzu-UV-1601 PC) and X Ray photoelectron spectroscopy (XPS), Kratos Analytical XSAM 800 cpi ESCA equipped with a Mg anode (Mg Kα radiation, 1253.6 eV) and spherical analyzer operating at 15 kV and 15 mA. The reduction profile of the materials was studied by Temperature-programmed reduction (TPR) in a Quantachrome ChemBet 3000.
Catalytic tests
Oxidation of methylene blue dye
The catalytic properties of the materials were tested through the degradation of the methylene blue textile dye, model organic molecule. The oxidation tests were done using a 9.9 mL solution of methylene blue at a concentration of 25 mg L-1, 0.1 mL of 30% H2O2 solution and 10 mg of the Sn/Nb2O5 composite, under constant agitation at 100 rpm.
The degradation was monitored by UV-visible spectroscopy (Shimadzu-UV-1601 PC) in the maximum absorption wavelength of methylene blue: 645 nm. The degradation products were analyzed by ESI-MS (Agilent-1100). The sample was inserted in the apparatus by infusion at a flow of 5 µL min-1, with charge control in the quadrupole (ICC) set to 30,000 and positive mode. The drying gas (N2) temperature was 325 ºC with a flow rate of 4 L min- 1, with an ion extraction potential of -3500 V.
RESULTS AND DISCUSSION
Characterization of the catalysts
For the determination of the treatment temperature for obtaining metallic tin on niobium oxide, the material impregnated with SnO2, after being calcinated, was characterized by TPR. The programmed temperature reduction profiles for the SnO2 sample on niobium oxide (SnO2/Nb2O5, 10% tin in mass) and of the support are shown in Figure 1. The observed reactions were described by the Equations 1 and 2:9
The peak centered approximately at 427 ºC, shown in Figure 1, corresponds to the reduction of Sn4+ to Sn2+ as schematized in Equation 1. The reduction of the active phase for Sn0 occurs at approximately 619 ºC, as shown in Equation 2, indicating the treatment temperature for obtaining the material containing metallic tin. The samples containing 1 and 5% tin on niobium oxides presented reduction profiles similar to those observed in Figure 1. Moreover, the reduction of the Nb2O5 support, could be observed close to 900 ºC, as reported in the literature.3
In Figure 2 the X-ray diffractograms of the Sn/Nb2O5 samples (1, 5 and 10% in mass) are shown.
Due to the reflections presented by the DRX analyses it can be noted that the reverse-oxidation of part of the metallic phase probably occurred, because the presence of SnO2/Nb2O5 and SnO/Nb2O5 as well as Sn0/Nb2O5 composites were evident.10-12 These results could be confirmed by the XPS analysis, Figure 3.
The mean crystalline size for the different tin phases and for the best peaks of each tin phase, in this case SnO2 (2θ = 26.95º) and Sn0 (2θ = 63.67º) were calculated through the Scherrer equation: d = kλβcosθ, in which d represents the mean diameter of the particles, k is the Scherrer constant, which depends on the morphology of the crystals, λ is the radiation length used, in this case Kα do Cu (1.5418 Å) and β corresponds to the value of the maximum width at half the height of the reflection of interest. In Table 1 the results for the mean particle size of the tin dioxide and the metallic tin are presented.
Reflections referring to niobium oxide were not observed, suggesting the occurrence of an amorphous material.13
The tin phases were also characterized by XPS. In Figure 3, the spectrum obtained for the Sn0/Nb2O5-5 % composite is presented.
By XPS analysis, the presence of the reduced species Sn0 (BE = 485.1 eV) and the oxidized state Sn2+ (BE = 494.8) and Sn4+ (BE = 493.7 eV),14 can be verified.
The vibrational spectra in the infrared region for the niobium oxide, before and after heat treatment, are shown in Figure 4.
The spectrum of Figure 4 presents bands characteristic of amorphous niobium oxide,15 characterized mainly by the bands centered at 621 and 908 cm-1. Furthermore, it presents vibrations referring to OH surface groups and adsorbed H2O at1626 and 3380 cm-1.
The spectra in the infrared region shown in Figure 1S, supplementary material, indicates tin presence on the surface of the niobium oxide represented by the peaks 807 and 873 cm-1. The band centered at 560 cm-1 is associated with the Sn-O-Sn asymmetrical stretching.10
Decomposition of H2O2
The decomposition of H2O2 was carried out as the first evaluation of the catalytic activity presented by the material. In view of this, the pure niobium oxide and the materials obtained by the thermal reduction of the niobium oxide impregnated with different levels of tin were studied as catalysts in the decomposition of hydrogen peroxide.
Decomposition of H2O2 in aqueous solution and decomposition of H2O2 in the presence of MB
The decomposition capacity of H2O2 is indirectly measured by the volume of O2 formed, given by the Equation 3:
The decomposition of H2O2 is accelerated as the tin level on the surface of the niobium oxide (Figure 5) increases until the tin level of 5%. Considering that the beginning of the reaction is of pseudo-first order kinetics in relation to H2O2 one has Vdecomp. = Kdecomp..[H2O2 ] and the constants of velocity exhibited by the materials were 0.0006; 0.0017; 0.007 and 0.0001 min-1, for the samples: pure niobium oxide, Sn0/Nb2O5-1%, Sn0/Nb2O5-5%, Sn0/Nb2O5-10%, respectively.
With these results, there is evidence that the presence of the metallic tin in the surface of the niobium oxide possesses an important function in the activation of the hydrogen peroxide. To try to elucidate the of H2O2 decomposition mechanism, the reaction was conducted in the presence of the organic compound methylene blue.
The decomposition of H2O2 in the presence of organic composition, species that with likeness for radicals, supplies information on the present mechanism in the oxidation with the composites and H2O2.
The results shown in Figure 2S, supplementary material, indicated an inhibition in the decomposition of the peroxide promoted by the addition of compounds which possess an affinity for hydroxylated radicals, that would be formed in the decomposition of the peroxide in a Fenton type system. It is inferred, with that, that those organic compounds participate in competitive processes during the decomposition of H2O2, in which the intermediate compounds that promote the formation of O2 react with the organic compound present, causing a decrease in the velocity constant by 0.0005; 0.0014; 0.006 and 0.0005 min-1 of Nb2O5, Sn0/Nb2O5-1%, Sn0/Nb2O5-5% and Sn0/Nb2O5-10%, respectively.
Oxidation of the methylene blue dye
The oxidation of the organic dye methylene blue by the Sn/Nb2O5 type catalysts containing different tin levels can be observed in Figure 6. The oxide of pure niobium did not present dye removal capacity.
It can be observed in Figure 6 that the sample containing 10% in mass of Sn in the surface of the niobium oxide presented higher discoloration capacity of the solution containing the of methylene blue dye during the whole interval of time studied. It is interesting to observe that the removal of the dye happens slowly up to 120 reaction min. After this time, an abrupt increase was observed in the discoloration until total removal of the dye from the aqueous medium.
Figure 3S, supplementary material, displays the ESI-MS study presenting hydroxylation signals and the break of the dye ring. Studies by electrospray coupled to a mass spectrometer of (ESI-MS) showed that up to 120 min only dye adsorption in the surface of the catalyst occurred, without oxidation intermediate formation. On the other hand, after 180 reaction min, the formation of hydroxylated intermediates with signals at m/z = 301 and 354 are presented, besides signals at m/z = 250 and 270 possibly due to the break of the dye aromatic ring, Figure 4S, supplementary material. The formation of these methylene blue dye oxidation intermediates is accompanied by the decrease of the signal m/z = 284 regarding the organic dye. It is important to point out that for the catalysts containing 1 or 5% of Sn0 the oxidation intermediate formation was not observed in the ESI-MS analyses, showing that the low removal of the dye by those materials, shown in Figure 6, occurred through adsorption processes.
Figure 4S, supplementary material, presents the possible structures responsible for the signals obtained in the ESI-MS spectra. The signal m/z = 284 (the dye structure) is hydroxylated, forming the structure with m/z = 300,16 and the signal m/z = 354, suggesting successive hydroxylations. It can be clearly noticed in Figure 7a, the spectrum with signal at m/z = 301 and the structure which represents a possible formation of the hydroxylated intermediate, presenting the value of 300. Studies of the mechanism involved seeking to propose the structure of the intermediate with signal m/z = 301 are being carried out. In Figure 4S the structures with m/z = 270 and 250 regarding the dye degradation are presented.
Reaction proposal involving the dye
The obtained results suggest that the tin impregnated in the structure of the niobium oxide favors the decomposition of the hydrogen peroxide, according to Equation 4.
According to Equation 5 that process is thermodynamically favorable.
Such a process is characterized by the reaction between the tin and the hydrogen peroxide leading to the formation of the OH radical, with strong oxidizing capacity. The radical can undergo two processes: oxidize the organic compound or react with H2O2 to form the hydroperoxide radical, OOH, that can regenerate the reactive site.
CONCLUSIONS
The obtained results showed that the system based on Sn/Nb2O5 containing 10% tin in mass presented good degradation capacity of the methylene blue textile dye. It is important to observe that the removal of the dye is accompanied by the formation of intermediate compounds, confirming the non-mineralization of the material.
The characterizations showed that part of Sn0 is oxidized after the reduction process with H2 which can be compromising the OH radical generation stage.
SUPPLEMENTARY MATERIAL
The supplementary material described below is available for free in http://quimicanova.sbq.org.br, in the form of PDF file: Figure 1S. Vibrational spectrum in the infrared region for the materials containing SnO2 and Sn0; Figure 2S. Profile of O2 liberation catalysed by niobium oxide materials and composites in the presence of MB; Figure 3S. ESI-MS in the presence of H2O2 and of the composites; Figure 4S. Proposed scheme for the formation of possible oxidation intermediates of the methylene blue dye.
ACKNOWLEDGEMENTS
The authors are extremely grateful to the Departamento de Química - UFLA (CAPQ) and CAPES, FAPEMIG and CNPq for financial support.
Recebido em 25/1/09; aceito em 2/10/09; publicado na web em 24/2/10
MATERIAL SUPLEMENTAR
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Publication Dates
-
Publication in this collection
19 Apr 2010 -
Date of issue
2010
History
-
Received
25 Jan 2009 -
Accepted
02 Oct 2009