Journal
CHEMOSPHERE
Volume 311, Issue -, Pages -Publisher
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.chemosphere.2022.137001
Keywords
Fenitrothion; Trifluralin; Chlorothalonil; Bi -PbO 2 electrode; Anodic oxidation process; Simultaneous degradation
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In this study, a modified Bi-PbO2 electrode was used to simultaneously degrade fenitrothion, trifluralin, and chlorothalonil in synthetic and pesticide wastewater. A high-performance liquid chromatography method was developed to identify the pesticides simultaneously. Quadratic models were developed to investigate the effects of operating parameters and predict the degradation efficiencies. The maximum degradation efficiencies obtained were 99.7%, 100%, and 100% for fenitrothion, trifluralin, and chlorothalonil, respectively.
In this work, modified Bi-PbO2 electrode was fabricated and employed for simultaneous degradation of fenitrothion (FT), trifluralin (TF), and chlorothalonil (CT) from synthetic and pesticide wastewater through the anodic oxidation process. A novel high-performance liquid chromatography method was developed and optimized to identify the pesticides simultaneously. Quadratic models were developed to investigate the effects of main operating parameters and predict the degradation efficiencies of the treatment processes. The R2 of the degradation efficiencies were obtained of 0.9847, 0.9910, and 0.9821 for FT, TF, and CT, respectively, which indicates the degree of conformity between the experimental and the actual values of degradation efficiencies, and the adjusted R2 values for the degradation efficiency of FT, TF, and CT in proposed models were 0.9826, 0.9898, and 0.9796, and the values of the predicted R2 were 0.9792, 0.9875, and 0.9755, respectively. The maximum degradation efficiencies of 99.7, 100, and 100% obtained for FT, TF, and CT, respectively, under the optimal operating condition of FT, TF, and CT concentration of 10.0, 6.0, and 8.0 mg L-1, respectively, pH 6.0, the current density 6.0 mA cm-2, and electrolysis time of 60 min. Chemical oxygen demand removal and energy consumption were 64.7% and 5.1 kWh m-3. Eventually, the generated intermediates and other produced species of pesticides through the treatment process was evaluated using a gas chromatography-mass spectrometry method, and their degradation pathways were proposed.
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