2021-04-162020-01-011572665718732569WOS;000593969800015SCOPUS;2-s2.0-85089855533http://hdl.handle.net/10784/29420In 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.engElsevier BVActivated carbonActivated carbon treatmentAdsorptionAnodesBiodegradabilityBoolean functionsCathodesChemical oxygen demandCoagulationConstrained optimizationDegradationEffluent treatmentElectrochemical oxidationElectrolysisElectrooxidationEnergy utilizationIndustrial water treatmentIronMolecular weight distributionNonlinear programmingOrganic pollutantsSludge disposalTextile industryTextilesToxicityWastewater disposalWastewater treatmentActivated carbon adsorptionBox-Behnken experimental designConstrained non-linear optimizationsLow molecular weightManufacturing companiesOperational conditionsOrganic matter degradationsResponse surface methodologyEffluentsinfo:eu-repo/semantics/article2021-04-16GilPavas E.Dobrosz-Gómez I.Gómez-García M.-Á.10.1016/j.jelechem.2020.114578