The Box-Benkhen experimental design for the optimization of the electrocatalytic treatment of wastewaters with high concentrations of phenol and organic matter.
dc.citation.journalTitle | WATER SCIENCE AND TECHNOLOGY | |
dc.contributor.author | GilPavas, Edison | |
dc.contributor.author | Betancourt, Alejandra | |
dc.contributor.author | Angulo, Monica | |
dc.contributor.author | Dobrosz-Gomez, Izabela | |
dc.contributor.author | Angel Gomez-Garcia, Miguel | |
dc.contributor.department | Universidad EAFIT. Departamento de Ingeniería de Procesos | spa |
dc.contributor.researchgroup | Procesos Ambientales (GIPAB) | spa |
dc.creator | GilPavas, Edison | |
dc.creator | Betancourt, Alejandra | |
dc.creator | Angulo, Monica | |
dc.creator | Dobrosz-Gomez, Izabela | |
dc.creator | Angel Gomez-Garcia, Miguel | |
dc.date.accessioned | 2021-04-16T20:27:36Z | |
dc.date.available | 2021-04-16T20:27:36Z | |
dc.date.issued | 2009-01-01 | |
dc.description.abstract | In this work, the Box-Benkhen experimental Design (BBD) was applied for the optimization of the parameters of the electrocatalytic degradation of wastewaters resulting from a phenolic resins industry placed in the suburbs of Medellin (Colombia). The direct and the oxidant assisted electro-oxidation experiments were carried out in a laboratory scale batch cell reactor, with monopolar configuration, and electrodes made of graphite (anode) and titanium (cathode). A multifactorial experimental design was proposed, including the following experimental variables: initial phenol concentration, conductivity, and pH. The direct electro-oxidation process allowed to reach ca. 88% of phenol degradation, 38% of mineralization (TOC), 52% of Chemical Oxygen Demand (COD) degradation, and an increase in water biodegradability of 13%. The synergetic effect of the electro-oxidation process and the respective oxidant agent (Fenton reactant, potassium permanganate, or sodium persulfate) let to a significant increase in the rate of the degradation process. At the optimized variables values, it was possible to reach ca. 99% of phenol degradation, 80% of TOC and 88% of COD degradation. A kinetic study was accomplished, which included the identification of the intermediate compounds generated during the oxidation process. | eng |
dc.identifier | https://eafit.fundanetsuite.com/Publicaciones/ProdCientif/PublicacionFrw.aspx?id=1446 | |
dc.identifier.doi | 10.2166/wst.2009.705 | |
dc.identifier.issn | 02731223 | |
dc.identifier.issn | 19969732 | |
dc.identifier.other | WOS;000272452900009 | |
dc.identifier.other | PUBMED;19934502 | |
dc.identifier.other | SCOPUS;2-s2.0-85000288396 | |
dc.identifier.uri | http://hdl.handle.net/10784/29367 | |
dc.language.iso | eng | |
dc.publisher | IWA PUBLISHING | |
dc.relation.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-85000288396&doi=10.2166%2fwst.2009.705&partnerID=40&md5=6abad7c1987f334a382b92defbe5f266 | |
dc.rights | https://v2.sherpa.ac.uk/id/publication/issn/0273-1223 | |
dc.source | WATER SCIENCE AND TECHNOLOGY | |
dc.subject | Biodegradation | eng |
dc.subject | Chemical oxygen demand | eng |
dc.subject | Chemicals removal (water treatment) | eng |
dc.subject | Degradation | eng |
dc.subject | Design | eng |
dc.subject | Graphite electrodes | eng |
dc.subject | Optimization | eng |
dc.subject | Oxidants | eng |
dc.subject | Oxidation resistance | eng |
dc.subject | Oxygen | eng |
dc.subject | Phenolic resins | eng |
dc.subject | Phenols | eng |
dc.subject | Potassium | eng |
dc.subject | Reaction intermediates | eng |
dc.subject | Resins | eng |
dc.subject | Sodium | eng |
dc.subject | Statistics | eng |
dc.subject | Titanium | eng |
dc.subject | Wastewater | eng |
dc.subject | Wastewater treatment | eng |
dc.subject | Batch cells | eng |
dc.subject | Colombia | eng |
dc.subject | Degradation process | eng |
dc.subject | Electro-oxidation process | eng |
dc.subject | Electrocatalytic | eng |
dc.subject | Experimental design | eng |
dc.subject | High concentration | eng |
dc.subject | Intermediate compound | eng |
dc.subject | Kinetic study | eng |
dc.subject | Laboratory scale | eng |
dc.subject | Organic matter | eng |
dc.subject | Oxidation process | eng |
dc.subject | Phenol concentration | eng |
dc.subject | Phenol degradation | eng |
dc.subject | Potassium permanganate | eng |
dc.subject | Sodium persulfate | eng |
dc.subject | Synergetic effect | eng |
dc.subject | Anodic oxidation | eng |
dc.subject | graphite | eng |
dc.subject | organic matter | eng |
dc.subject | permanganate potassium | eng |
dc.subject | phenol | eng |
dc.subject | resin | eng |
dc.subject | titanium | eng |
dc.subject | biodegradation | eng |
dc.subject | catalysis | eng |
dc.subject | chemical oxygen demand | eng |
dc.subject | electrode | eng |
dc.subject | experimental design | eng |
dc.subject | mineralization | eng |
dc.subject | optimization | eng |
dc.subject | organic matter | eng |
dc.subject | oxidant | eng |
dc.subject | oxidation | eng |
dc.subject | pH | eng |
dc.subject | phenol | eng |
dc.subject | reaction kinetics | eng |
dc.subject | resin | eng |
dc.subject | suburban area | eng |
dc.subject | titanium | eng |
dc.subject | wastewater | eng |
dc.subject | water treatment | eng |
dc.subject | biodegradability | eng |
dc.subject | chemical oxygen d | eng |
dc.title | The Box-Benkhen experimental design for the optimization of the electrocatalytic treatment of wastewaters with high concentrations of phenol and organic matter. | 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 |
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