TY - JOUR
T1 - Degradation of chloramphenicol by Ti-Ag/γ-Al2O3 particle electrode using three-dimensional reactor
AU - Sun, Yongjun
AU - Chen, Aowen
AU - Sun, Wenquan
AU - Zhou, Jun
AU - Shah, Kinjal J.
AU - Zheng, Huaili
AU - Shen, Hao
N1 - Publisher Copyright:
© 2019 Desalination Publications.
PY - 2019/9
Y1 - 2019/9
N2 - In this paper, highly efficient Ti-Ag/γ-Al2O3 particle electrodes were prepared for efficient degradation of chloramphenicol (CAP) by using three-dimensional electrocatalytic technology. The effects of preparation factors, such as mass ratio of Ti/Ag, loading times, and calcination temperature, on the electrocatalytic performance of Ti-Ag/γ-Al2O3 particle electrode were investigated. In addition, Ti-Ag/γ-Al2O3 particle electrodes under different conditions were characterized by SEM, EDS, XRF, and XRD. The optimal removal rate of chloramphenicol was 84.2% with initial concentration of chloramphenicol 100 mg/L, conductivity 6,000 µs cm-1, initial pH 4.0, current intensity I = 0.2 A, and flow rate 1.0 L/min. The elimination of •OH by addition of t-butanol reduced the chloramphenicol removal rate by 56.0% under the same working conditions, indicating that the degradation of chloramphenicol was caused by the combination of •OH indirect oxidation and anodic indirect oxidation. Meanwhile, the degradation process of chloramphenicol was approximately in accordance with the first-order kinetic equation.
AB - In this paper, highly efficient Ti-Ag/γ-Al2O3 particle electrodes were prepared for efficient degradation of chloramphenicol (CAP) by using three-dimensional electrocatalytic technology. The effects of preparation factors, such as mass ratio of Ti/Ag, loading times, and calcination temperature, on the electrocatalytic performance of Ti-Ag/γ-Al2O3 particle electrode were investigated. In addition, Ti-Ag/γ-Al2O3 particle electrodes under different conditions were characterized by SEM, EDS, XRF, and XRD. The optimal removal rate of chloramphenicol was 84.2% with initial concentration of chloramphenicol 100 mg/L, conductivity 6,000 µs cm-1, initial pH 4.0, current intensity I = 0.2 A, and flow rate 1.0 L/min. The elimination of •OH by addition of t-butanol reduced the chloramphenicol removal rate by 56.0% under the same working conditions, indicating that the degradation of chloramphenicol was caused by the combination of •OH indirect oxidation and anodic indirect oxidation. Meanwhile, the degradation process of chloramphenicol was approximately in accordance with the first-order kinetic equation.
KW - Chloramphenicol
KW - Degradation
KW - Electrocatalysis
KW - Particle electrode
UR - http://www.scopus.com/inward/record.url?scp=85073383777&partnerID=8YFLogxK
U2 - 10.5004/dwt.2019.24563
DO - 10.5004/dwt.2019.24563
M3 - 文章
AN - SCOPUS:85073383777
SN - 1944-3994
VL - 163
SP - 96
EP - 108
JO - Desalination and Water Treatment
JF - Desalination and Water Treatment
ER -