Efficient treatment for textile wastewater through sequential electrocoagulation, electrochemical oxidation and adsorption processes: Optimization and toxicity assessment
dc.citation.journalTitle | JOURNAL OF ELECTROANALYTICAL CHEMISTRY | |
dc.contributor.author | GilPavas E. | |
dc.contributor.author | Dobrosz-Gómez I. | |
dc.contributor.author | Gómez-García M.-Á. | |
dc.contributor.department | Universidad EAFIT. Departamento de Ingeniería de Procesos | spa |
dc.contributor.researchgroup | Procesos Ambientales (GIPAB) | spa |
dc.creator | GilPavas E. | |
dc.creator | Dobrosz-Gómez I. | |
dc.creator | Gómez-García M.-Á. | |
dc.date.accessioned | 2021-04-16T20:27:40Z | |
dc.date.available | 2021-04-16T20:27:40Z | |
dc.date.issued | 2020-01-01 | |
dc.description.abstract | In this work, the sequential Electrocoagulation + Electro-oxidation + Activated carbon adsorption (EC + EO + AC) process was studied as an alternative for the treatment of an industrial textile wastewater (TWW) issuing from a manufacturing company located in Medellín (Colombia). The EC's and EO's operational conditions were optimized using a Box-Behnken experimental design, the Response Surface Methodology and a constrained nonlinear optimization algorithm in terms of organic matter degradation efficiency. The best performance for EC (i. e., dye removal = 94%, COD and TOC degradation of 45 and 40%, respectively) was obtained using Fe anode and Boron Doped Diamond (BDD) cathode, with current density, jEC, equals to 5 mA/cm2, pH = 9.3, 60 RPM and 10 min of electrolysis. After EC treatment, the effluent biodegradability (evaluated as the BOD5/COD ratio) increases from 0.14 to 0.23. Regrettably, EC was not effective for the removal of acute toxicity to Artemia salina since the treated effluent remained very toxic (100%). The treatment of EC's effluent by EO enhanced organic pollutant removal. For EC + EO sequential process, EO optimal operational conditions (jEO = 10 mA/cm2, pH = 3, 240 RPM, BDD as anode and Fe as cathode) allowed reduction of 100% of color, 88% of COD and 79% of TOC after 30 min of electrolysis. Moreover, the BOD5/COD ratio increased from 0.23 to 0.58; however, the treated effluent remained very toxic to the Artemia salina. Consequently, an activated carbon adsorption step was included to complete the treatment process. Thus, by coupling the EC + EO + AC process, effluent's acute toxicity decreased completely. From molecular weight distribution analysis, it was concluded that EC + EO was efficient in eliminating low molecular weight (< 5 kDa) compounds. Finally, the operation cost, which includes chemical reagents, electrodes, energy consumption, and sludge disposal, for the EC + EO + AC sequential process was estimated in 3.83 USD /m3. © 2020 Elsevier B.V. | eng |
dc.identifier | https://eafit.fundanetsuite.com/Publicaciones/ProdCientif/PublicacionFrw.aspx?id=12158 | |
dc.identifier.doi | 10.1016/j.jelechem.2020.114578 | |
dc.identifier.issn | 15726657 | |
dc.identifier.issn | 18732569 | |
dc.identifier.other | WOS;000593969800015 | |
dc.identifier.other | SCOPUS;2-s2.0-85089855533 | |
dc.identifier.uri | http://hdl.handle.net/10784/29420 | |
dc.language.iso | eng | |
dc.publisher | Elsevier BV | |
dc.relation.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85089855533&doi=10.1016%2fj.jelechem.2020.114578&partnerID=40&md5=e80bea2e9508972219c0d9c71ac2c8eb | |
dc.rights | Elsevier BV | |
dc.source | JOURNAL OF ELECTROANALYTICAL CHEMISTRY | |
dc.subject | Activated carbon | eng |
dc.subject | Activated carbon treatment | eng |
dc.subject | Adsorption | eng |
dc.subject | Anodes | eng |
dc.subject | Biodegradability | eng |
dc.subject | Boolean functions | eng |
dc.subject | Cathodes | eng |
dc.subject | Chemical oxygen demand | eng |
dc.subject | Coagulation | eng |
dc.subject | Constrained optimization | eng |
dc.subject | Degradation | eng |
dc.subject | Effluent treatment | eng |
dc.subject | Electrochemical oxidation | eng |
dc.subject | Electrolysis | eng |
dc.subject | Electrooxidation | eng |
dc.subject | Energy utilization | eng |
dc.subject | Industrial water treatment | eng |
dc.subject | Iron | eng |
dc.subject | Molecular weight distribution | eng |
dc.subject | Nonlinear programming | eng |
dc.subject | Organic pollutants | eng |
dc.subject | Sludge disposal | eng |
dc.subject | Textile industry | eng |
dc.subject | Textiles | eng |
dc.subject | Toxicity | eng |
dc.subject | Wastewater disposal | eng |
dc.subject | Wastewater treatment | eng |
dc.subject | Activated carbon adsorption | eng |
dc.subject | Box-Behnken experimental design | eng |
dc.subject | Constrained non-linear optimizations | eng |
dc.subject | Low molecular weight | eng |
dc.subject | Manufacturing companies | eng |
dc.subject | Operational conditions | eng |
dc.subject | Organic matter degradations | eng |
dc.subject | Response surface methodology | eng |
dc.subject | Effluents | eng |
dc.title | Efficient treatment for textile wastewater through sequential electrocoagulation, electrochemical oxidation and adsorption processes: Optimization and toxicity assessment | eng |
dc.type | info:eu-repo/semantics/article | eng |
dc.type | article | eng |
dc.type | info:eu-repo/semantics/publishedVersion | eng |
dc.type | publishedVersion | eng |
dc.type.local | Artículo | spa |