Central composite rotatable design for non-convex optimization of removal efficiency of hydroxychloroquine in an electrochemical cell

被引:2
|
作者
Regalado-Mendez, Alejandro [1 ]
Vasquez-Hernandez, Daniel [1 ]
Natividad, Reyna [2 ]
Peralta-Reyes, Ever [1 ]
机构
[1] Univ Mar Campus Puerto Angel, Res Labs, San Pedro Pochutla 70902, Mexico
[2] Univ Autonoma Estado Mexico, Chem Engn Lab, Ctr Conjunto Invest Quim Sustentable, UAEM UNAM, Km 14-5 Toluca Atlacomulco Rd, Toluca 50200, Mexico
关键词
Batch electrochemical cell; BDD electrode; Electrochemical degradation; Hydroxychloroquine; Non-convex optimization; WASTE-WATER TREATMENT; HYDROXYL RADICALS; OXIDATION; DEGRADATION; POLLUTANTS; ELECTRODE; REACTOR;
D O I
10.1007/s10008-024-05962-y
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
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 boron-doped 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 (Omega): 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 Omega = 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.
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页数:19
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