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

dc.contributor.author
Dos Santos, Alexsandro Jhones
dc.contributor.author
Brillas, Enric
dc.contributor.author
Cabot Julià, Pere-Lluís
dc.contributor.author
Sirés Sadornil, Ignacio
dc.date.issued
2020-09-02T09:03:33Z
dc.date.issued
2022-08-06T05:10:21Z
dc.date.issued
2020-08-06
dc.date.issued
2020-09-02T09:03:33Z
dc.identifier
0048-9697
dc.identifier
https://hdl.handle.net/2445/170148
dc.identifier
702985
dc.description.abstract
The 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
application/pdf
dc.language
eng
dc.publisher
Elsevier B.V.
dc.relation
Versió postprint del document publicat a: https://doi.org/10.1016/j.scitotenv.2020.141541
dc.relation
Science of the Total Environment, 2020, vol. 747, num. 141541
dc.relation
https://doi.org/10.1016/j.scitotenv.2020.141541
dc.rights
cc-by-nc-nd (c) Elsevier B.V., 2020
dc.rights
http://creativecommons.org/licenses/by-nc-nd/3.0/es
dc.rights
info:eu-repo/semantics/openAccess
dc.source
Articles publicats en revistes (Ciència dels Materials i Química Física)
dc.subject
Depuració de l'aigua
dc.subject
Oxidació electroquímica
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Water purification
dc.subject
Electrolytic oxidation
dc.title
Simultaneous persulfate activation by electrogenerated H2O2 and anodic oxidation at a boron-doped diamond anode for the treatment of dye solutions
dc.type
info:eu-repo/semantics/article
dc.type
info:eu-repo/semantics/acceptedVersion


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