Mostrar el registro sencillo del objeto digital
| dc.contributor.author | REGALADO-MENDEZ, Alejandro
|
|
| dc.contributor.author | Natividad, Reyna
|
|
| dc.contributor.author | Peralta Reyes, Ever
|
|
| dc.contributor.author | Vasquez Hernández, D
|
|
| dc.date.accessioned | 2024-11-14T16:31:48Z | |
| dc.date.available | 2024-11-14T16:31:48Z | |
| dc.date.issued | 2024-06-13 | |
| dc.identifier.issn | 1433-0768 | |
| dc.identifier.uri | http://hdl.handle.net/20.500.11799/141664 | |
| dc.description | articulo científico | es |
| dc.description.abstract | Hydroxychloroquine sulfate (HCQ), an against-COVID-19 drug, is a dangerous organic compound in wastewater. In this study, 0.6 L of an HCQ solution (50!mg L−1) was electro-oxidized in a batch electrochemical cell (BEC) with two borondoped diamond (BDD) electrodes. The optimal operating conditions were established by DoE-driven non-convex constrained optimization. A central composite rotatable design (CCRD) was applied to model the chemical oxygen demand (COD) removal efficiency and to evaluate the influence of current density (j): 10–120!mA! cm−2, initial pH: 2–12, and stirring speed (!): 400–600!rpm. Experimental results were modeled by a reduced third-order polynomial function having a determination coefficient (R2), root mean square error (RMSE), mean square error (MSE), and coefficient of variation (C.V.) of 0.9906, 0.0460, 0.0021, and 3.72%, respectively. This validates the predictive capacity of the fitted model and the efficiency of the employed electro-oxidation process. The optimal operating vector was j = 46.36!mA! cm−2, pH0 = 12.04, and ! = 584!rpm within 5!h of reaction time, attaining a maximum COD removal efficiency of 85.55% with an energy consumption of 1.24!kW!h L−1 and a total operating cost of 0.067 USD$ L−1. Also, a total organic carbon removal of 52.5% was achieved. Additionally, mathematical models were established to fit the temporary profiles of HCQ degradation, COD, and TOC removal. The estimated apparent kinetic constants (kapp) were 1.21! h−1, 0.26! h−1, and 2.65!mg L−1! h−1, respectively. Finally, it was concluded that the assessed electrochemical process could help mineralizing wastewater containing HCQ. | es |
| dc.language.iso | eng | es |
| dc.publisher | Journal of Solid State Electrochemistry | es |
| dc.rights | embargoedAccess | es |
| dc.rights.uri | http://creativecommons.org/licenses/by-nc/4.0 | es |
| dc.subject | ELECTRO-OXIDACION | es |
| dc.subject | electrodos de diamante dopados con boro | es |
| dc.subject | DISEÑO DE EXPERIMENTOS | es |
| dc.subject.classification | INGENIERÍA Y TECNOLOGÍA | es |
| dc.title | Central composite rotatable design for non-convex optimization of removal efficiency of hydroxychloroquine in an electrochemical cell. Journal of Solid State Electrochemistry | es |
| dc.type | Artículo | es |
| dc.provenance | Científica | es |
| dc.road | Verde | es |
| dc.organismo | Química | es |
| dc.ambito | Nacional | es |
| dc.cve.CenCos | 20403 | es |
| dc.cve.progEstudios | 747 | es |
| dc.relation.vol | sn | |
| dc.validacion.itt | Si | es |