Sequential electrocoagulation–ozonation treatment: Effect of suspended solids removal on sulfide elimination in tannery wastewater

dc.contributor.authorAguilar-Ascón, Edwar
dc.contributor.authorMarrufo-Saldaña, Liliana del Rosario
dc.contributor.authorBarra-Hinojosa, Julio Alexis
dc.date.accessioned2026-07-13T15:30:28Z
dc.date.available2026-07-13T15:30:28Z
dc.date.issued2026-07-01
dc.date.submitted2026-01-08
dc.description.abstractThe treatment of tannery wastewater is a complex environmental challenge. These effluents have high loads of total suspended solids (TSS) and, especially, sulfides, pollutants that require advanced technologies due to their toxicity and difficulty in removal. This study presents and evaluates an integrated electrocoagulation (EC) and ozonation (O3) system as an alternative for the comprehensive treatment of this effluent. In the EC stage, it was optimized using the response surface methodology (RSM) with a 3k factorial design, using current intensity (I) and treatment time (t) as factors to maximize TSS removal. The EC results demonstrated high TSS removal efficiency, reaching 97.91% under optimal conditions (p < 0.05), which significantly facilitates subsequent treatment. The most critical finding of the study lies in the ineffectiveness of EC for dissolved contaminants: the removal of sulfides was extremely limited, with an efficiency of only 4.2%. In contrast, the subsequent ozonation stage achieved more than 99% elimination of sulfides using a dose of 12 g h-1 of ozone after 20 minutes of reaction. This result justifies the need for an integrated system, where EC handles the load of solids (TSS) and other contaminants and ozonation performs the essential chemical oxidation of sulfides. The operating cost of the combined EC–O3 treatment was determined to be US$ 0.707 m-3, demonstrating the economic viability of the technology. The results confirm that the EC–O3 system is a synergistic solution for the environmental management of tannery wastewater, enabling compliance with maximum permissible limits.
dc.formatapplication/pdf
dc.identifier.doihttps://doi.org/10.12911/22998993/220121
dc.identifier.urihttps://hdl.handle.net/20.500.14523/889
dc.language.isoeng
dc.publisherJournal of Ecological Engineeringes_PE
dc.relation.ispartofurn:issn:2299-8993
dc.rightshttp://purl.org/coar/access_right/c_abf2es_PE
dc.rights.urihttps://creativecommons.org/licenses/by/4.0/es_PE
dc.subjecttannery wastewater
dc.subjectelectrocoagulation
dc.subjectozonation
dc.subjectresponse surface methodology
dc.subjectsulfide removal
dc.subjectadvanced oxidation processes
dc.subject.ocdehttps://purl.org/pe-repo/ocde/ford#2.07.01
dc.subject.ocdehttps://purl.org/pe-repo/ocde/ford#2.04.02
dc.subject.ocdehttps://purl.org/pe-repo/ocde/ford#2.04.01
dc.titleSequential electrocoagulation–ozonation treatment: Effect of suspended solids removal on sulfide elimination in tannery wastewater
dc.typehttp://purl.org/coar/resource_type/c_2df8fbb1

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