Assessing the HClO/Fe^2+Fenton-like reaction for the degradation of metronidazole in a flow cell equipped with a Ti-Ru-Ir oxides anode

Assessing the HClO/Fe<sup>2+</sup> Fenton-like reaction for the degradation of metronidazole in a flow cell equipped with a Ti-Ru-Ir oxides anode

dc.contributor.author
Rodríguez, Juan F.
dc.contributor.author
Cornejo, Oscar M.
dc.contributor.author
Sirés Sadornil, Ignacio
dc.contributor.author
Nava, José L.
dc.date.accessioned
2026-03-11T19:53:16Z
dc.date.available
2026-03-11T19:53:16Z
dc.date.issued
2026-03-10T16:48:41Z
dc.date.issued
2026-02-09
dc.date.issued
2026-03-10T16:48:45Z
dc.date.issued
info:eu-repo/date/embargoEnd/2028-02-08
dc.identifier
2213-3437
dc.identifier
https://hdl.handle.net/2445/227983
dc.identifier
768293
dc.identifier.uri
https://hdl.handle.net/2445/227983
dc.description.abstract
This work examines the electrochemical mineralization of metronidazole (MTZ) via the photoelectro-Fenton-like (PEF-like) process in a flow plant utilizing a filter-press electrolyzer with a Ti|Ti-Ru-Ir-oxides anode. The process uses the chloride ions contained in a dilute solution to form HClO through direct anodic oxidation on the Ti|Ti-Ru-Ir-oxides anode. Then, HClO reacts with ferrous ion (Fe<sup>2+</sup>) to yield ferryl-oxo species (Fe<sup>IV</sup>O<sup>2+</sup>) and hydroxyl radicals (<sup>•</sup>OH), which are responsible for the mineralization of MTZ to CO<sub>2</sub>. The influence of the current density (<em>j</em>), as well as the initial Cl<sup>-</sup>, Fe<sup>2+</sup>, and MTZ concentrations was systematically examined to determine the best experimental conditions for MTZ degradation. A comparison of electro-oxidation aided with active chlorine (EO-HClO), electro-Fenton-like (EF-like), and PEF-like processes for the elimination of MTZ indicates the superiority of the latter one. The use of scavengers indicates that Fe<sup>IV</sup>O<sup>2+</sup> is the main oxidant (58 %), with minor contributions from <sup>•</sup>OH (13 %) and other routes, such as electro-oxidation and chlorination. Optimum PEF-like conditions for the complete degradation of 20 mg L<sup>-1</sup> MTZ involved the use of 0.4 mM Fe<sup>2+</sup> in a 35 mM NaCl+ 50 mM Na<sub>2</sub>SO<sub>4</sub> electrolyte, at <em>j</em> = 16 mA cm<sup>-2</sup> and <em>u</em> = 10 cm s<sup>-1</sup>, with an electrolytic energy consumption of 0.9 kWh (g TOC)<sup>-1</sup>. Up to 78 % of mineralization was attained, where the residual dissolved organic matter mainly consisted of oxalic acid and N-derivatives.
dc.format
31 p.
dc.format
application/pdf
dc.language
eng
dc.publisher
Elsevier
dc.relation
Versió postprint del document publicat a: https://doi.org/10.1016/j.jece.2026.121711
dc.relation
Journal of Environmental Chemical Engineering, 2026, vol. 14, num.2
dc.relation
https://doi.org/10.1016/j.jece.2026.121711
dc.rights
cc-by-nc-nd (c) Elsevier, 2026
dc.rights
http://creativecommons.org/licenses/by-nc-nd/4.0/
dc.rights
info:eu-repo/semantics/embargoedAccess
dc.subject
Reacció d'oxidació-reducció
dc.subject
Compostos azoics
dc.subject
Oxidation-reduction reaction
dc.subject
Azo compounds
dc.title
Assessing the HClO/Fe^2+Fenton-like reaction for the degradation of metronidazole in a flow cell equipped with a Ti-Ru-Ir oxides anode
dc.title
Assessing the HClO/Fe<sup>2+</sup> Fenton-like reaction for the degradation of metronidazole in a flow cell equipped with a Ti-Ru-Ir oxides anode
dc.type
info:eu-repo/semantics/article
dc.type
info:eu-repo/semantics/acceptedVersion


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