992 resultados para FENTON REACTION


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The addition of 0.5 mM catechol is shown to accelerate the degradation and mineralization of the anionic surfactant DOWFaX (TM) 2A1 (sodium dodecyldiphenyloxide disulfonate) under conventional Fenton reaction conditions (Fe(II) plus H(2)O(2) at pH 3). The catalytic effect causes a 3-fold increase in the initial rate (up to ca. 20 min) of conversion of the surfactant to oxidation products (apparent first-order rate constants of 0.021 and 0.061 min(-1) in the absence and presence of catechol, respectively). Although this catalytic rate increase persists for a certain amount of time after complete disappearance of catechol itself (ca. 8 min), the reaction rate begins to decline slowly after the initial 20 min towards that observed in the absence of added catechol. Total organic carbon (TOC) measurements of net mineralization and cyclic voltammetric and high performance liquid chromatographic (HPLC) measurements of the initial rate of reaction of catechol and the surfactant provide insight into the role of catechol in promoting the degradation of the surfactant and of degradation products as the eventual inhibitors of the Fenton reaction. (C) 2010 Elsevier B.V. All rights reserved.

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The degradation of DDT [1,1-bis(4-chlorophenyl)-2,2,2-trichloroethane] and DDE [2,2-bis(4-chlorophenyl)-1,1-dichloroethylene] in highly and long-term contaminated soil using Fenton reaction in a slurry system is studied in this work. The influence of the amount of soluble iron added to the slurry versus the mineral iron originally present in the soil, and the influence of H2O2 concentration on the degradation process are evaluated. The main iron mineral species encountered in the soil, hematite (Fe2O3), did not show catalytic activity in the decomposition of H2O2, resulting in low degradation of DDT (24%) and DDE (4%) after 6 h. The addition of soluble iron (3.0 mmol L-1) improves the reaction reaching 53% degradation of DDT and 46% of DDE. The increase in iron concentration from 3.0 to 24 mmol L-1 improves slightly the degradation rate of the contaminants. However, similar degradation percentages were obtained after 24 h of reaction. It was observed that low concentrations of H2O2 were sufficient to degrade around 50% of the DDT and DDE present in the soil, while higher degradation percentages were achieved only with high amounts of this reagent (1.1 mol L-1). (c) 2006 Elsevier B.V. All rights reserved.

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The addition of Cu2+ ions to the classical Fenton reaction (Fe2+ plus H2O2 at pH 3) is found to accelerate the degradation of organic compounds. This synergic effect causes an approximately 15 % additional reduction of the total organic carbon (TOC), representing an overall improvement of the efficiency of the mineralization of phenol. Although Fe2+ exhibits a high initial rate of degradation, the degradation is not complete due to the formation of compounds refractory to the hydroxyl radical. The interference of copper ions on the degradation of phenol by the Fenton reaction was investigated. In the presence of Cu2+, the degradation is slower, but results in a greater reduction of TOC at the end of the reaction (t = 120 min). In the final stages of the reaction, when the Fe3+ in the solution is complexed in the form of ferrioxalate, the copper ions assume the role of the main catalyst of the degradation.

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A novel amperometric sensor based on the incorporation of ruthenium oxide hexacyanoferrate (RuOHCF) into multiwalled carbon nanotubes (MWCNTs) immobilized on a glassy carbon electrode is described. Cyclic voltammetry experiments indicated that the cathodic reduction of hydrogen peroxide at the RuOHCF/MWCNTs100/GC modified electrode is facilitated, occurring at 0.0 V vs. Ag/AgCl/KCl(sat). Following the optimization of the experimental conditions, the proposed sensor presented excellent analytical properties for hydrogen peroxide determination, with a low limit of detection (4.7 mu mol L-1), a large dynamic concentration range (0.1-10 mmol L-1) and a sensitivity of 1280 mu A mmol(-1) L cm(-2). The usefulness of the RuOHCF/MWCNTs100/GC electrochemical sensor was confirmed by monitoring the consumption of hydrogen peroxide during the degradation of phenol by the Fenton reaction. (C) 2012 Elsevier B.V. All rights reserved.

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A study of the interference of Zn2+ ions on phenol degradation by Fenton reaction (Fe2+/Fe3(+) + H2O2) is reported. One of the first intermediates formed in the reaction, catechol, can reduce Fe3+ to Fe2+ and, in the presence of H2O2 initiates an efficient catalytic redox cycle. In the initial stages of the reaction, this catechol-mediated cycle becomes the principal route of thermal degradation of phenol and its oxidation products. The Zn2+ ion addition enhances the persistence time of catechol, probably by stabilization of the corresponding semiquinone radical via complexation.

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A study of the interference of Zn2+ ions on phenol degradation by Fenton reaction (Fe2+/Fe3+ + H2O2) is reported. One of the first intermediates formed in the reaction, catechol, can reduce Fe3+ to Fe2+ and, in the presence of H2O2 initiates an efficient catalytic redox cycle. In the initial stages of the reaction, this catechol-mediated cycle becomes the principal route of thermal degradation of phenol and its oxidation products. The Zn2+ ion addition enhances the persistence time of catechol, probably by stabilization of the corresponding semiquinone radical via complexation.

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The addition of Cu2+ ions to the classical Fenton reaction (Fe2+ plus H2O2 at pH 3) is found to accelerate the degradation of organic compounds. This synergic effect causes an approximately 15 % additional reduction of the total organic carbon (TOC), representing an overall improvement of the efficiency of the mineralization of phenol. Although Fe2+ exhibits a high initial rate of degradation, the degradation is not complete due to the formation of compounds refractory to the hydroxyl radical. The interference of copper ions on the degradation of phenol by the Fenton reaction was investigated. In the presence of Cu2+, the degradation is slower, but results in a greater reduction of TOC at the end of the reaction (t = 120 min). In the final stages of the reaction, when the Fe3+ in the solution is complexed in the form of ferrioxalate, the copper ions assume the role of the main catalyst of the degradation

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Discoloration and mineralization of Reactive Red HE-3B were studied by using a laponite clay-based Fe nanocomposite (Fe-Lap-RD) as a heterogeneous catalyst in the presence of H2O2 and UV light. Our experimental results clearly indicate that Fe-Lap-RD mainly consists of Fe2O3 (meghemite) and Fe2Si4O10(OH)2 (iron silicate hydroxide) which have tetragonal and monoclinic structures, respectively, and has a high specific surface area (472m(2) / g) as well as a high total pore volume (0.547 cm(3)/g). It was observed that discoloration of HE-3B undergoes a much faster kinetics than mineralization of HE-3B. It was also found that initial HE-3B concentration, H2O2 concentration, UV light wavelength and power, and Fe-Lap-RD catalyst loading are the four main factors that can significantly influence the mineralization of HE-3B. At optimal conditions, complete discoloration of 100 mg/L HE-3B can be achieved in 30 min and the total organic carbon removal ratio can attain 76% in 120 min, illustrating that Fe-Lap-RD has a high photo-catalytic activity in the photo-assisted discoloration and mineralization of HE-3B in the presence of UV light (254nm) and H2O2. (C) 2003 Elsevier Science Ltd. All rights reserved.

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A novel nanocomposite of iron oxide and silicate, prepared through a reaction between a solution of iron salt and a dispersion of Laponite clay, was used as a catalyst for the photoassisted Fenton degradation of azo-dye Orange II. This catalyst is much cheaper than the Nafion-based catalysts, and our results illustrate that it can significantly accelerate the degradation of Orange II under the irradiation of UV light (lambda = 254 nm). An advantage of the catalyst is its long-term stability that was confirmed through using the catalyst for multiple runs in the degradation of Orange II. The effects of the H2O2 molar concentration, solution pH, wavelength and power of the LTV light, catalyst loading, and initial Orange II concentration on the degradation of Orange 11 were studied in detail. In addition, it was also found that discoloration of Orange 11 undergoes a faster kinetics than mineralization of Orange II and 75% total organic carbons of 0.1 mM Orange II can be eliminated after 90 min in the presence of 1.0 g of Fe-nanocomposite/L, 4.8 mM H2O2, and 1 x 8W UVC.

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A Casa da Moeda do Brasil (CMB) é uma empresa nacional, com mais de 300 anos de experiência na produção de valores e impressos de segurança. A produção de cédulas, realizada pelo Departamento de Cédulas (DECED), consiste de três etapas de impressão, off-set, calografia e tipografia, seguida de acabamento e embalagem semi-automatizado. A impressão calcográfica consome solução de limpeza, composta de soda cáustica e óleo sulfonado, para limpeza do cilindro de impressão, gerando um efluente líquido saturado de tinta. Este efluente apresenta baixa biodegradabilidade, apresentando uma relação DBO / DQO de aproximadamente 1:4. Em termos de tratabilidade, as estações de tratamento de efluentes (ETE) apresentam uma configuração convencional, por via biológica, demonstram pouca eficiência na degradação da matéria orgânica deste efluente. Com compostos recalcitrantes, torna-se necessária a inclusão de uma etapa terciária que permita sua degradação por via química, permitindo o descarte do efluente com características menos danosas ao ambiente. Neste trabalho, aplicou-se a reação de Fenton no efluente do DECED por sua capacidade de converter a matéria orgânica em gás carbônico e água ou, caso seja utilizado em pré-tratamentos, torna-os biodegradáveis. Foram estudadas diferentes condições para medir a influência de diferentes parâmetros na eficiência da reação. A reação de Fenton consiste na geração de radicais hidroxil (HO), por diferentes rotas, em quantidades suficientes para a degradação de matéria orgânica. Esses radicais são gerados a partir de peróxido de hidrogênio (H2O2) em reações com diferentes precursores como ozônio (O3), luz UV (ultravioleta), ultra-som e sais de ferro. No presente trabalho restringiu-se às reações com sais de ferro. Dentre os resultados obtidos, verificou-se o tempo mínimo para reação em 10 minutos. A relação entre íons ferro e peróxido de hidrogênio é menor do que a literatura normalmente sugere, 1:2, contra 1:3. Como a solução de sulfato ferroso é muito instável, passando os íons ferrosos a férricos, utilizou-se a adição direta do sal. Em escala industrial, a solução de sulfato ferroso deve ser preparada em poucas quantidades para que tenha baixo tempo de estocagem, a fim de não ser degradada. A temperatura, na faixa estudada (de 20C à 45C), é um parâmetro que tem pouca influência, pois a redução da eficiência da reação foi pequena (de 99,0% para 94,9%). O ferro utilizado na reação não se demonstrou uma nova fonte de transtornos para o ambiente. Nas condições utilizadas, a concentração de ferro residual esteve próxima ao limite permitido pela legislação no efluente tratado, necessitando apenas de alguns ajustes para a correção do problema

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Alguns cientistas ambientais prevêem que a poluição dos solos será um dos maiores legados com grandes impactos para as gerações futuras, pois atualmente ainda existe desconhecimento das fontes poluidoras e da sua extensão. O Brasil, devido a sua extensão territorial, suas bacias hidrográficas, número de postos de abastecimentos e controles ambientais ainda ineficazes, está muito exposto a esse tipo de poluição. Atualmente, há no Brasil mais de 34.300 postos de combustíveis, com volume de 65.000.000 m3 de gasolina e diesel consumidos anualmente, conforme dados da Agência Nacional do Petróleo Gás Natural e Biocombustíveis , ANP, em 2008. Sendo assim, a exposição e contaminação dos solos e dos lençóis freáticos com constituintes aromáticos do diesel e gasolina torna-se um sério problema ambiental. Dentro deste grupo, encontram-se o benzeno, tolueno, xileno, conhecido como BTEX e os hidrocarbonetos policíclicos aromáticos, conhecido como PAH. Este trabalho tem como objetivo estudar a remediação in-situ de um posto de combustíveis na região do ABC Paulista, no Estado de São Paulo. Aplicando-se a técnica de Processo Oxidativo Avançado via reagente de Fenton (H2O2 + Fe2+ → Fe3+ + OH- + OH . ), o radical hidroxila gerado mineraliza compostos aromáticos, decompondo-os definitivamente. Amostras de água do posto em estudo apresentavam elevados teores de BTEX e PAH, 2,58 mg.L-1 e 0,298 mg.L-1 respectivamente, estando em níveis não tolerados pelo órgão ambiental paulista CETESB sendo necessária a intervenção para tratamento da área. Com os níveis de poluentes e o perfil hidrogeológico identificados, a remediação foi iniciada com injeções no solo de peróxido de hidrogênio a 8%v.v, FeSO4 a 0,40 mg.L-1 e solução à base de NPK (nitrogênio, fósforo e nitrogênio) a 100 mg.L-1 como nutrientes para os microorganismos do solo. Estes valores são provenientes de experimentos anteriores e tratamentos já realizados. Foram conduzidas campanhas de injeção trimestrais com 100 litros desta solução completa como reagente , e medições trimestrais de BTEX, PAH e outros parâmetros de controle, que foram indicando o sucesso do tratamento. Após 18 meses o local foi considerado tratado pelo órgão ambiental, onde monitoramentos semestrais estão em continuidade para garantir o resultado do tratamento e das ações corretivas. Assim, o estudo real da remediação de solos contaminados com os poluentes orgânicos via processo de Fenton, com concentração de H2O2 a 8%v/v, e FeSO4 a 0,40 mg.L-1 demonstrou-se uma técnica de sucesso. O entendimento dos resultados da remediação, mesmo sujeitos aos fenômenos naturais, como intempéries e chuvas, é uma experiência grande, pois por mais reais que simulações em laboratório possam ser, é muito difícil incluir nestes sistemas, as variações que um tratamento real está exposto

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Optimization of photo-Fenton degradation of copper phthalocyanine blue was achieved by response surface methodology (RSM) constructed with the aid of a sequential injection analysis (SIA) system coupled to a homemade photo-reactor. Highest degradation percentage was obtained at the following conditions [H(2)O(2)]/[phthalocyanine] = 7, [H(2)O(2)]/[FeSO(4)] = 10, pH = 2.5, and stopped flow time in the photo reactor = 30 s. The SIA system was designed to prepare a monosegment containing the reagents and sample, to pump it toward the photo-reactor for the specified time and send the products to a flow-through spectrophotometer for monitoring the color reduction of the dye. Changes in parameters such as reagent molar ratios. residence time and pH were made by modifications in the software commanding the SI system, without the need for physical reconfiguration of reagents around the selection valve. The proposed procedure and system fed the statistical program with degradation data for fast construction of response surface plots. After optimization, 97% of the dye was degraded. (C) 2009 Elsevier B.V. All rights reserved.

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This work presents the use of sequential injection analysis (SIA) and the response surface methodology as a tool for optimization of Fenton-based processes. Alizarin red S dye (C.I. 58005) was used as a model compound for the anthraquinones family. whose pigments have a large use in coatings industry. The following factors were considered: [H(2)O(2)]:[Alizarin] and [H(2)O(2)]:[FeSO(4)] ratios and pH. The SIA system was designed to add reagents to the reactor and to perform on-line sampling of the reaction medium, sending the samples to a flow-through spectrophotometer for monitoring the color reduction of the dye. The proposed system fed the statistical program with degradation data for fast construction of response surface plots. After optimization, 99.7% of the dye was degraded and the TOC content was reduced to 35% of the original value. Low reagents consumption and high sampling throughput were the remarkable features of the SIA system. (C) 2008 Published by Elsevier B.V.

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Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)

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Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)