4-Hydroxyphenylacetic acid oxidation in sulfate and real olive oil mill wastewater by electrochemical advanced processes with a boron-doped diamond anode

dc.contributor.authorFlores Tapia, Nelly Esther
dc.contributor.authorCabot Julià, Pere-Lluís
dc.contributor.authorCentellas Masuet, Francesc A.
dc.contributor.authorGarrido Ponce, José Antonio
dc.contributor.authorRodríguez González, Rosa Ma.
dc.contributor.authorBrillas, Enric
dc.contributor.authorSirés Sadornil, Ignacio
dc.date.accessioned2020-03-20T10:09:19Z
dc.date.available2020-03-20T10:09:19Z
dc.date.issued2016-09-24
dc.date.updated2020-03-20T10:09:19Z
dc.description.abstractThe degradation of 4-hydroxyphenylacetic acid, a ubiquitous component of olive oil mill wastewater (OOMW), has been studied by anodic oxidation with electrogenerated H2O2 (AO-H2O2), electro-Fenton (EF) and photoelectro-Fenton (PEF). Experiments were performed in either a 0.050 M Na2SO4 solution or in real OOMW at pH 3.0, using a cell with a boron-doped diamond (BDD) anode and an air-diffusion cathode for H2O2 generation. Hydroxyl radicals formed at the BDD surface from water oxidation in all processes and/or in the bulk from Fenton's reaction between added Fe2+ and generated H2O2 in EF and PEF were the main oxidants. In both matrices, the oxidation ability of the processes increased in the order AO-H2O2 < EF < PEF. The superiority of PEF was due to the photolytic action of UVA radiation on photosensitive by-products, as deduced from the quick removal of Fe(III)-oxalate complexes. The effect of current density and organic content on the performance of all treatments was examined. 4-Hydroxyphenylacetic acid decay obeyed a pseudo-first-order kinetics. The PEF treatment of 1.03 mM 4-hydroxyphenylacetic acid in 0.050 M Na2SO4 allowed 98% mineralization at 360 min even at low current density, whereas 80% mineralization and a significant enhancement of biodegradability were achieved with the real OOMW.
dc.format.extent10 p.
dc.format.mimetypeapplication/pdf
dc.identifier.idgrec664200
dc.identifier.issn0304-3894
dc.identifier.urihttps://hdl.handle.net/2445/153183
dc.language.isoeng
dc.publisherElsevier B.V.
dc.relation.isformatofVersió postprint del document publicat a: https://doi.org/10.1016/j.jhazmat.2016.09.057
dc.relation.ispartofJournal of Hazardous Materials, 2016, vol. 321, p. 566-575
dc.relation.urihttps://doi.org/10.1016/j.jhazmat.2016.09.057
dc.rightscc-by-nc-nd (c) Elsevier B.V., 2016
dc.rights.accessRightsinfo:eu-repo/semantics/openAccess
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es
dc.sourceArticles publicats en revistes (Ciència dels Materials i Química Física)
dc.subject.classificationDepuració d'aigües residuals
dc.subject.classificationOxidació electroquímica
dc.subject.classificationOli d'oliva
dc.subject.otherPurification of sewage
dc.subject.otherElectrolytic oxidation
dc.subject.otherOlive oil
dc.title4-Hydroxyphenylacetic acid oxidation in sulfate and real olive oil mill wastewater by electrochemical advanced processes with a boron-doped diamond anode
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/acceptedVersion

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