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dc.contributor.author | PERALTA REYES, EVER | |
dc.contributor.author | REGALADO MENDEZ, ALEJANDRO | |
dc.contributor.author | Amado Piña, Deysi | |
dc.contributor.author | CORDERO SANCHEZ, MARIO EDGAR | |
dc.contributor.author | NATIVIDAD RANGEL, REYNA | |
dc.contributor.author | MENTADO MORALES, JUAN | |
dc.contributor.author | Castellanos García, Mayra | |
dc.creator | PERALTA REYES, EVER; 87037 | |
dc.creator | REGALADO MENDEZ, ALEJANDRO; 101257 | |
dc.creator | Amado Piña, Deysi; 481734 | |
dc.creator | CORDERO SANCHEZ, MARIO EDGAR; 37450 | |
dc.creator | NATIVIDAD RANGEL, REYNA; 87755 | |
dc.creator | MENTADO MORALES, JUAN; 48694 | |
dc.creator | Castellanos García, Mayra;x1357844 | |
dc.date.accessioned | 2020-02-17T20:42:03Z | |
dc.date.available | 2020-02-17T20:42:03Z | |
dc.date.issued | 2020-02-05 | |
dc.identifier.issn | 2063-0212 | |
dc.identifier.uri | http://hdl.handle.net/20.500.11799/105670 | |
dc.description | Es un artículo científico publicado en una revista indizada en JCR | es |
dc.description.abstract | Synthetic solutions of 2-chlorophenol (2-CP, 1 mM) were treated in an undivided continuous flow electrochemical reactor equipped with boron-doped diamond (BDD) electrodes. The process was conducted at different current densities (j = 0.10, 0.125, and 0.14 A cm−2), initial pH (4.0, 7.3, and 9.0), and volumetric flow rate (Q = 0.5, 1.0, and 1.5 L min−1). The results of this study showed that the best operational conditions were: j = 0.14 A cm−2, pH = 7.3, and y Q = 1 L min−1. Under these operational conditions the degradation and mineralization of 2-CP were, 100% and 96%, respectively, after 6 h of electrolysis time. The by-products were identified by UHPLC. Also, it was found that the electrochemical degradation of 2-chlorophenol follows a pseudo-first order kinetics. Furthermore, these results demonstrate that the electrolysis process employed in this work allows high percentages (96%) of mineralization of 2-CP, a relative low treatment cost ($ 3 MXN/ 2.5 L of synthetic solution), and that the process is applicable to remediate wastewater. | es |
dc.description.sponsorship | CONACYT 269093 PRODEP 103/14/11350 | es |
dc.language.iso | eng | es |
dc.publisher | Journal of Flow Chemistry | es |
dc.rights | openAccess | es |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-sa/4.0 | |
dc.subject | electro-oxidation | es |
dc.subject.classification | INGENIERÍA Y TECNOLOGÍA | es |
dc.subject.classification | INGENIERÍA Y TECNOLOGÍA | |
dc.title | Electro-oxidation of 2-chlorophenol with BDD electrodes in a continuous flow electrochemical reactor | es |
dc.type | Artículo | es |
dc.provenance | Científica | es |
dc.road | Dorada | es |
dc.organismo | Química Unidad Cerrillo | es |
dc.ambito | Nacional | es |
dc.cve.CenCos | 20403 | es |
dc.audience | students | es |
dc.audience | researchers | es |
dc.type.conacyt | article | |
dc.identificator | 7 |