Simultaneous persulfate activation by electrogenerated H2O2 and anodic oxidation at a boron-doped diamond anode for the treatment of dye solutions

dc.contributor.authorDos Santos, Alexsandro Jhones
dc.contributor.authorBrillas, Enric
dc.contributor.authorCabot Julià, Pere-Lluís
dc.contributor.authorSirés Sadornil, Ignacio
dc.date.accessioned2020-09-02T09:03:33Z
dc.date.available2022-08-06T05:10:21Z
dc.date.issued2020-08-06
dc.date.updated2020-09-02T09:03:33Z
dc.description.abstractThe development of new or upgraded electrochemical water treatment technologies is considered a topic of great interest. Here, Tartrazine azo dye solutions were treated by means of a quite innovative dual electrochemical persulfate (S2O8 2 −, PS) activation that combines H2O2 generation at an airdiffusion cathode and anodic oxidation (AO) at a boron-doped diamond (BDD) anode using a stirred tank reactor. This so-called AO-H2O2/PS process was compared to AO with stainless steel cathode, both in 50 mM Na2SO4 medium, finding the oxidation power increasing as: AO < AO-H2O2 < AO/PS < AOH2O2/PS. In the latter, the dye and its products were mainly destroyed by: (i) hydroxyl radicals, formed either from water oxidation at BDD surface or via reaction between H2O2 and S2O8 2−, and (ii) sulfate radical anion, formed from the latter reaction, thermal PS activation and cathodic S2O8 2− reduction. Hydroxyl radicals prevailed as oxidizing agents, as deduced from trials with tert-butanol and methanol. The reaction between S2O8 2 − and accumulated H2O2 was favored as temperature increased from 25 to 45 °C. The effect of PS content up to 36 mM, dye concentration within the range 0.22-0.88 mM, current density (j) between 8.3 and 33.3 mA cm−2 and pH between 3.0 and 9.0 on the process performance was examined. All decolorization profiles agreed with a pseudo-first-order kinetics. The best results for treating 0.44 mM dye were attained with 36 mM PS at pH 3.0, j = 16.7 mA cm−2 and 45 °C, yielding total loss of color, 62% TOC removal and 50% mineralization current efficiency after 360 min. The slow mineralization was attributed to the persistence of recalcitrant byproducts like maleic, acetic, oxalic, formic and oxamic acids. It is concluded that the novel AO-H2O2/PS process is more effective than AO/PS to treat Tartrazine solutions, being advisable to extend the study to other organic pollutants.
dc.format.mimetypeapplication/pdf
dc.identifier.idgrec702985
dc.identifier.issn0048-9697
dc.identifier.urihttps://hdl.handle.net/2445/170148
dc.language.isoeng
dc.publisherElsevier B.V.
dc.relation.isformatofVersió postprint del document publicat a: https://doi.org/10.1016/j.scitotenv.2020.141541
dc.relation.ispartofScience of the Total Environment, 2020, vol. 747, num. 141541
dc.relation.urihttps://doi.org/10.1016/j.scitotenv.2020.141541
dc.rightscc-by-nc-nd (c) Elsevier B.V., 2020
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 de l'aigua
dc.subject.classificationOxidació electroquímica
dc.subject.otherWater purification
dc.subject.otherElectrolytic oxidation
dc.titleSimultaneous persulfate activation by electrogenerated H2O2 and anodic oxidation at a boron-doped diamond anode for the treatment of dye solutions
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:eu-repo/semantics/acceptedVersion

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