Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts

This paper reports the mineralization of an aromatic pharmaceutical as clofibric acid and the dye indigo carmine in 0.05 M Na2SO4 of pH 3.0 by electrochemical advanced oxidation processes such as anodic oxidation without and with electrogenerated H2O2, electro-Fenton and photoelectro-Fenton using a boron-doped diamond (BDD) anode. These procedures produce the strong oxidant hydroxyl radical in the form of BDD(·OH) from water oxidation at BDD and/or ·OH from Fenton’s reaction between added Fe2+ and H2O2 generated at the cathode by two-electron O2 reduction. Comparative degradation of both compounds is performed with an undivided electrolytic cell of 100 mL with an O2-diffusion cathode. The effect of current density and pollutant concentration on the degradation rate and current efficiency of the different methods is discussed. The decay kinetics of clofibric acid and indigo carmine and the evolution of their aromatic by-products and final carboxylic acids like oxalic and/or oxamic are described to clarify their reaction sequences. Anodic oxidation is able to completely mineralize both compounds mainly with BDD(·OH). Aromatic pollutants are more rapidly destroyed in electro-Fenton due to their faster reaction with ·OH, but final Fe(III)-oxalate and Fe(III)-oxamate can only be oxidized with BDD(·OH). The most efficient method is photoelectro-Fenton due to the parallel photolysis of Fe(III)-oxalate complexes with UVA light, although Fe(III)-oxamate complexes are not photodecomposed. Under these conditions, the degradation rate can be enhanced using Cu2+ as co-catalyst because Cu(II)-oxalate and Cu(II)-oxamate complexes are quickly destroyed by ·OH. Results on the fast mineralization of 2.5 L of cresols solutions of pH 3.0 by solar photoelectro-Fenton using a flow plant coupled to a solar photoreactor are also reported. The high efficiency and very low operational cost found for this procedure make it useful for the treatment of industrial wastewaters

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Main Authors: Brillas,E., Garrido,J.A., Rodríguez,R.M., Arias,C., Cabot,P.L., Centellas,F.
Format: Digital revista
Language:English
Published: Sociedade Portuguesa de Electroquímica 2008
Online Access:http://scielo.pt/scielo.php?script=sci_arttext&pid=S0872-19042008000100002
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spelling oai:scielo:S0872-190420080001000022008-10-06Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as CatalystsBrillas,E.Garrido,J.A.Rodríguez,R.M.Arias,C.Cabot,P.L.Centellas,F. clofibric acid indigo carmine cresols anodic oxidation electro-Fenton photoelectro-Fenton solar photoelectro-Fenton This paper reports the mineralization of an aromatic pharmaceutical as clofibric acid and the dye indigo carmine in 0.05 M Na2SO4 of pH 3.0 by electrochemical advanced oxidation processes such as anodic oxidation without and with electrogenerated H2O2, electro-Fenton and photoelectro-Fenton using a boron-doped diamond (BDD) anode. These procedures produce the strong oxidant hydroxyl radical in the form of BDD(·OH) from water oxidation at BDD and/or ·OH from Fenton’s reaction between added Fe2+ and H2O2 generated at the cathode by two-electron O2 reduction. Comparative degradation of both compounds is performed with an undivided electrolytic cell of 100 mL with an O2-diffusion cathode. The effect of current density and pollutant concentration on the degradation rate and current efficiency of the different methods is discussed. The decay kinetics of clofibric acid and indigo carmine and the evolution of their aromatic by-products and final carboxylic acids like oxalic and/or oxamic are described to clarify their reaction sequences. Anodic oxidation is able to completely mineralize both compounds mainly with BDD(·OH). Aromatic pollutants are more rapidly destroyed in electro-Fenton due to their faster reaction with ·OH, but final Fe(III)-oxalate and Fe(III)-oxamate can only be oxidized with BDD(·OH). The most efficient method is photoelectro-Fenton due to the parallel photolysis of Fe(III)-oxalate complexes with UVA light, although Fe(III)-oxamate complexes are not photodecomposed. Under these conditions, the degradation rate can be enhanced using Cu2+ as co-catalyst because Cu(II)-oxalate and Cu(II)-oxamate complexes are quickly destroyed by ·OH. Results on the fast mineralization of 2.5 L of cresols solutions of pH 3.0 by solar photoelectro-Fenton using a flow plant coupled to a solar photoreactor are also reported. The high efficiency and very low operational cost found for this procedure make it useful for the treatment of industrial wastewatersinfo:eu-repo/semantics/openAccessSociedade Portuguesa de ElectroquímicaPortugaliae Electrochimica Acta v.26 n.1 20082008-01-01info:eu-repo/semantics/articletext/htmlhttp://scielo.pt/scielo.php?script=sci_arttext&pid=S0872-19042008000100002en
institution SCIELO
collection OJS
country Portugal
countrycode PT
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access En linea
databasecode rev-scielo-pt
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region Europa del Sur
libraryname SciELO
language English
format Digital
author Brillas,E.
Garrido,J.A.
Rodríguez,R.M.
Arias,C.
Cabot,P.L.
Centellas,F.
spellingShingle Brillas,E.
Garrido,J.A.
Rodríguez,R.M.
Arias,C.
Cabot,P.L.
Centellas,F.
Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts
author_facet Brillas,E.
Garrido,J.A.
Rodríguez,R.M.
Arias,C.
Cabot,P.L.
Centellas,F.
author_sort Brillas,E.
title Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts
title_short Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts
title_full Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts
title_fullStr Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts
title_full_unstemmed Wastewaters by Electrochemical Advanced Oxidation Processes Using a BDD Anode and Electrogenerated H2O2 with Fe(II) and UVA Light as Catalysts
title_sort wastewaters by electrochemical advanced oxidation processes using a bdd anode and electrogenerated h2o2 with fe(ii) and uva light as catalysts
description This paper reports the mineralization of an aromatic pharmaceutical as clofibric acid and the dye indigo carmine in 0.05 M Na2SO4 of pH 3.0 by electrochemical advanced oxidation processes such as anodic oxidation without and with electrogenerated H2O2, electro-Fenton and photoelectro-Fenton using a boron-doped diamond (BDD) anode. These procedures produce the strong oxidant hydroxyl radical in the form of BDD(·OH) from water oxidation at BDD and/or ·OH from Fenton’s reaction between added Fe2+ and H2O2 generated at the cathode by two-electron O2 reduction. Comparative degradation of both compounds is performed with an undivided electrolytic cell of 100 mL with an O2-diffusion cathode. The effect of current density and pollutant concentration on the degradation rate and current efficiency of the different methods is discussed. The decay kinetics of clofibric acid and indigo carmine and the evolution of their aromatic by-products and final carboxylic acids like oxalic and/or oxamic are described to clarify their reaction sequences. Anodic oxidation is able to completely mineralize both compounds mainly with BDD(·OH). Aromatic pollutants are more rapidly destroyed in electro-Fenton due to their faster reaction with ·OH, but final Fe(III)-oxalate and Fe(III)-oxamate can only be oxidized with BDD(·OH). The most efficient method is photoelectro-Fenton due to the parallel photolysis of Fe(III)-oxalate complexes with UVA light, although Fe(III)-oxamate complexes are not photodecomposed. Under these conditions, the degradation rate can be enhanced using Cu2+ as co-catalyst because Cu(II)-oxalate and Cu(II)-oxamate complexes are quickly destroyed by ·OH. Results on the fast mineralization of 2.5 L of cresols solutions of pH 3.0 by solar photoelectro-Fenton using a flow plant coupled to a solar photoreactor are also reported. The high efficiency and very low operational cost found for this procedure make it useful for the treatment of industrial wastewaters
publisher Sociedade Portuguesa de Electroquímica
publishDate 2008
url http://scielo.pt/scielo.php?script=sci_arttext&pid=S0872-19042008000100002
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