Coagulation-flocculation sequential with Fenton or Photo-Fenton processes as an alternative for the industrial textile wastewater treatment
dc.citation.journalTitle | Journal of Environmental Management | eng |
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 | Desarrollo y Diseño de Procesos | spa |
dc.date.accessioned | 2021-04-12T19:06:20Z | |
dc.date.available | 2021-04-12T19:06:20Z | |
dc.date.issued | 2017-04-15 | |
dc.description.abstract | In this study, the industrial textile wastewater was treated using a chemical-based technique (coagulation-flocculation, C-F) sequential with an advanced oxidation process (AOP: Fenton or Photo-Fenton). During the C-F, Al2(SO4)3 was used as coagulant and its optimal dose was determined using the jar test. The following operational conditions of C-F, maximizing the organic matter removal, were determined: 700 mg/L of Al2(SO4)3 at pH = 9.96. Thus, the C-F allowed to remove 98% of turbidity, 48% of Chemical Oxygen Demand (COD), and let to increase in the BOD5/COD ratio from 0.137 to 0.212. Subsequently, the C-F effluent was treated using each of AOPs. Their performances were optimized by the Response Surface Methodology (RSM) coupled with a Box-Behnken experimental design (BBD). The following optimal conditions of both Fenton (Fe2+/H2O2) and Photo-Fenton (Fe2+/H2O2/UV) processes were found: Fe2+ concentration = 1 mM, H2O2 dose = 2 mL/L (19.6 mM), and pH = 3. The combination of C-F pre-treatment with the Fenton reagent, at optimized conditions, let to remove 74% of COD during 90 min of the process. The C-F sequential with Photo-Fenton process let to reach 87% of COD removal, in the same time. Moreover, the BOD5/COD ratio increased from 0.212 to 0.68 and from 0.212 to 0.74 using Fenton and Photo-Fenton processes, respectively. Thus, the enhancement of biodegradability with the physico-chemical treatment was proved. The depletion of H2O2 was monitored during kinetic study. Strategies for improving the reaction efficiency, based on the H2O2 evolution, were also tested. © 2017 Elsevier Ltd | eng |
dc.identifier | https://eafit.fundanetsuite.com/Publicaciones/ProdCientif/PublicacionFrw.aspx?id=6187 | |
dc.identifier.doi | 10.1016/j.jenvman.2017.01.015 | |
dc.identifier.issn | 03014797 | |
dc.identifier.issn | 10958630 | |
dc.identifier.other | WOS;000396957300020 | |
dc.identifier.other | PUBMED;28092755 | |
dc.identifier.other | SCOPUS;2-s2.0-85009227831 | |
dc.identifier.uri | http://hdl.handle.net/10784/28248 | |
dc.language.iso | eng | |
dc.publisher | Editorial Board | |
dc.relation | DOI;10.1016/j.jenvman.2017.01.015 | |
dc.relation | WOS;000396957300020 | |
dc.relation | PUBMED;28092755 | |
dc.relation | SCOPUS;2-s2.0-85009227831 | |
dc.relation.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85009227831&doi=10.1016%2fj.jenvman.2017.01.015&partnerID=40&md5=bff195637266fdf8ce395a962e71f9b1 | |
dc.rights | https://v2.sherpa.ac.uk/id/publication/issn/0301-4797 | |
dc.source | Journal of Environmental Management | |
dc.subject | aluminum sulfate | eng |
dc.subject | ferrous gluconate | eng |
dc.subject | hydrogen peroxide | eng |
dc.subject | organic matter | eng |
dc.subject | hydrogen peroxide | eng |
dc.subject | industrial waste | eng |
dc.subject | iron | eng |
dc.subject | waste water | eng |
dc.subject | water pollutant | eng |
dc.subject | biodegradation | eng |
dc.subject | chemical oxygen demand | eng |
dc.subject | coagulation | eng |
dc.subject | dose-response relationship | eng |
dc.subject | experimental design | eng |
dc.subject | flocculation | eng |
dc.subject | industrial waste | eng |
dc.subject | numerical method | eng |
dc.subject | organic matter | eng |
dc.subject | oxidation | eng |
dc.subject | physicochemical property | eng |
dc.subject | pollutant removal | eng |
dc.subject | wastewater treatment | eng |
dc.subject | analysis of variance | eng |
dc.subject | Article | eng |
dc.subject | biochemical oxygen demand | eng |
dc.subject | biodegradability | eng |
dc.subject | chemical oxygen demand | eng |
dc.subject | controlled study | eng |
dc.subject | effluent | eng |
dc.subject | experimental design | eng |
dc.subject | flocculation | eng |
dc.subject | oxidation | eng |
dc.subject | pH | eng |
dc.subject | response surface method | eng |
dc.subject | textile industry | eng |
dc.subject | turbidity | eng |
dc.subject | waste water management | eng |
dc.subject | flocculation | eng |
dc.subject | industrial waste | eng |
dc.subject | oxidation reduction reaction | eng |
dc.subject | sewage | eng |
dc.subject | textile | eng |
dc.subject | waste water | eng |
dc.subject | water pollutant | eng |
dc.subject | Flocculation | eng |
dc.subject | Hydrogen Peroxide | eng |
dc.subject | Industrial Waste | eng |
dc.subject | Iron | eng |
dc.subject | Oxidation-Reduction | eng |
dc.subject | Textiles | eng |
dc.subject | Waste Disposal | eng |
dc.subject | Fluid | eng |
dc.subject | Waste Water | eng |
dc.subject | Water Pollutants | eng |
dc.subject | Chemical | eng |
dc.title | Coagulation-flocculation sequential with Fenton or Photo-Fenton processes as an alternative for the industrial textile wastewater treatment | eng |
dc.type | info:eu-repo/semantics/article | |
dc.type | info:eu-repo/semantics/publishedVersion | |
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 |
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