EFFECT OF ELECTROLYTE ON ELECTROCHEMICAL OXIDATION OF THE CARBOFURAN USING Ti/BDD ANODES M. R. Baldan1*; W. D. Toledo1; M. R. V. Lanza2; N.G. Ferreira1; N. M. Santos1 1 National Institute for Space Research, São José dos Campos, SP, Brazil 2 University of São Paulo (USP/IQSC), São Carlos, Brazil. Pesticide removal by the electrochemical oxidation was investigated with commercial Carbofuran with an electrolyte containing aqueous solutions K2SO4 0.1 mol L-1 or H2SO4 0.1 mol L-1 thermo stated at 20ºC, in a flow reactor with recirculation system. The degradation reactions were performed at constant applied current densities in the range 10 to 200 mAcm-2, flow rates of 50 and 300 Lh-1 for a total of 5 hours. The electrochemical oxidation of carbofuran pesticides has been carried using as anode four Ti/BDD electrodes, produced by Hot Filament Chemical Vapor Deposition reactor. The morphological and structural characterizations of the electrodes were evaluated by Scanning Electron Microscopy and by Raman Scattering Spectroscopy techniques. The electrochemical of Ti/BDD electrodes was performed by Cyclic Voltammetry in presence of the electrolytes. The effect of pH of the electrolyte in the electrochemical degradation of carbofuran was monitored by UV–Vis Spectrophotometry, Total Organic Carbon and High Performance Liquid Chromatography. The reducing the TOC concentration promoted the mineralization of pesticide contributing to the formation of carbofuran intermediates resulting from the reaction of oxidation. A completely degraded of the pesticide was obtained under an acid pH and current densities of 200 mAcm2. Keywords: BDD anodes, carbofuran, wastewater treatment, electrochemical oxidation. Introduction The electrochemical oxidation (EO) has been gained great interests as outstanding effective technologies to remove toxic micro pollutants [1-3]. In the EO process, hydroxyl radicals (OH) is mainly generated at the anode surface from water oxidation and carbon dioxide in a non-selected way, whose production rate is determined by the character of the anode material [4]. On the other hand, the high-efficiency electrode of conductive-diamond (BDD) anodes, with a promotion of higher mineralization rate of organics, has been widely applied to treat persistent pollutants [5, 6]. The experiments were designed to study the effect of electrolyte, and current density on EO process of the carbofuran, in which condition would benefit the higher production of •OH at BDD anode surface. The aim was to find the optimum values for operating conditions. A detailed study of the oxidation process on carbofuran by EO was provided to assess the environmental impact of the treatments. Experimental part The EO of carbofuran pesticides has been carried in an electrochemical reactor comprising two parallel polypropylene plates fitted with four Ti/BDD anodes and four 316 L stainless steel cathodes. The reactor was connected to a recirculation system through which electrolytes could be supplied at laminar and turbulent flow conditions and at different applied current densities for a total of 5 h with an aqueous electrolyte containing potassium sulphate or sulphuric acid (0.1 mol L−1) and 400 mg L−1 of commercial carbofuran thermo stated at 20 °C. The UV–Vis spectra were collected samples, the concentration of pesticide in the electrolyte was monitored by high performance liquid chromatography (HPLC) and the variation in total organic carbon (TOC) in the samples of electrolyte was measured using a Shimadzu TOCVCPN analyzer. BDD electrodes were produced on pure titanium substrate by Hot Filament Chemical Vapor Deposition reactor (HFCVD) using CH4/H2 gas mixtures. Boron was obtained from H2 forced to pass through a bubbler containing trimetylborate BO3(CH3)3 dissolved in methanol (CH3OH). The BDD electrodes morphology and quality were evaluated by SEM, micro-Raman scattering spectroscopy and the electrochemical characterization was performed by cyclic voltammetry. Results and discussion The representative spectra obtained by UV-Vis showed an absorption band variation centered on 276 nm that could be detected after 10 min of electrolysis. Increases in the intensity of this band were more pronounced in the spectral set obtained when electrolysis was performed at a density current of 200 mA cm−2. These results indicate that the electrolyte was modified in a time-dependent manner during electrolysis, possibly as a result of the degradation of the components of commercial carbofuran with formation of intermediaries’ products. HPLC chromatograms of the electrolyte containing pesticide showed peaks at 2.16 min corresponding to the supporting electrolyte and peak at 4.20 min corresponding to pesticide. The Raman scattering spectra of the BDD electrodes presented a sharp peak at around 1332 cm−1 corresponding to the first-order phonon line in diamond, a emergent band at 1220 cm−1 may be attributed to disorder in the diamond structure caused by the incorporation of boron and the band at around 500 cm−1 is associated with the vibration of boron pairs in the diamond lattice. SEM images revealed continuous and homogeneous BDD electrodes covering the entire substrates. Conclusions This study shows BDD electrodes are capable of rapidly oxidizing carbofuran to inorganic reaction products. The process likely involves direct oxidation via electron transfer and indirect oxidation via reaction with hydroxyl radicals produced from water oxidation. It can be concluded that the EO treatment with Ti/BDD as anode is highly effective for the rapid degradation and mineralization of carbofuran and the increasing current density accelerates the degradation and mineralization processes. The total degradation arised from hydroxylation on the aromatic moiety and also through the homolytic bond dissociation and hydrolysis of the carbamate C–O bond. References [1] Martinez-Huitle, C.A., Ferro, S., Chem. Society Reviews, 2006, 35, 1324. [2] Pimentel, M., Oturan, N., Dezotti, M., Oturan, M.A., Appl. Catal. B: Env., 2008, 83, 140. [3] Oturan, M.A., Oturan, N., Lahitte, C., Trevin, S., J. Electroanal. Chem., 2001, 50, 796. [4] Brillas, E., Sirés, I., Oturan, M.A., Chem. Reviews, 2009,109, 6570. [5] Panizza, M., Martinez-Huitle, C.A., Chemosphere, 2013, 90, 1455. [6] Cañizares, P., García-Gómez, J., Lobato, J., Rodrigo, M.A., Ind. & Eng. Chem. Research, 2003, 42, 956. Acknowledgement: The authors gratefully acknowledge the following Brazilian funding authorities for financial support: FAPESP, CAPES and CNPq.
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