Electrochemical Degradation of Acid Yellow 23 by Anodic OxidationOptimization of Operating Parameters
dc.citation.journalTitle | Journal Of Environmental Engineering, Asce | |
dc.contributor.author | GilPavas, Edison | |
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 | Dobrosz-Gomez, Izabela | |
dc.creator | Angel Gomez-Garcia, Miguel | |
dc.date.accessioned | 2021-04-16T20:27:38Z | |
dc.date.available | 2021-04-16T20:27:38Z | |
dc.date.issued | 2016-11-01 | |
dc.description.abstract | In this study, the electrochemical oxidation (EO) process was implemented and optimized to effectively decolorize and degrade wastewater containing Acid Yellow 23 (Y23). The experiments were carried out in a laboratory-scale batch cell reactor, with monopolar configuration of electrodes, made of graphite (anode) and titanium (cathode). The response surface methodology (RSM), coupled with Box-Behnken experimental design (BBD), was used to evaluate the single and interactive effects of different variables of the EO process on (1)degradation percentages of both chemical oxygen demand (%DCOD) and color (%DC) and (2)energy consumption (EC). Thus, the following experimental factors were considered: initial dye concentration (40-100mg/L), current density (10-20mA/cm2), and conductivity (1,000-4,000S/cm). Thus, the subsequent conditions were found to be optimal for decolorization and degradation of Y23: initial dye concentration = 100mg/L; current density = 20mA/cm2; and conductivity = 4,000S/cm. At these conditions, the EO process allowed to reach approximately 99% of color degradation and 76% of COD degradation. Because NaCl was used as an electrolyte, chorine formation was monitored, and its effect on %DC and %DCOD was also evaluated. | eng |
dc.identifier | https://eafit.fundanetsuite.com/Publicaciones/ProdCientif/PublicacionFrw.aspx?id=5182 | |
dc.identifier.doi | 10.1061/(ASCE)EE.1943-7870.0001127 | |
dc.identifier.issn | 07339372 | |
dc.identifier.issn | 19437870 | |
dc.identifier.other | WOS;000386358500006 | |
dc.identifier.other | SCOPUS;2-s2.0-84991709202 | |
dc.identifier.uri | http://hdl.handle.net/10784/29393 | |
dc.language.iso | eng | |
dc.publisher | American Society of Civil Engineers (ASCE) | |
dc.relation.uri | https://www.scopus.com/inward/record.uri?eid=2-s2.0-84991709202&doi=10.1061%2f%28ASCE%29EE.1943-7870.0001127&partnerID=40&md5=1e9bc083fc7e211dc11c54de80e9242c | |
dc.rights | https://v2.sherpa.ac.uk/id/publication/issn/0733-9372 | |
dc.source | Journal Of Environmental Engineering, Asce | |
dc.subject | Acid Yellow 23 | eng |
dc.subject | Degradation | eng |
dc.subject | Electro-oxidation | eng |
dc.subject | Graphite anode | eng |
dc.subject | Optimization | eng |
dc.title | Electrochemical Degradation of Acid Yellow 23 by Anodic OxidationOptimization of Operating Parameters | 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 |