Treatment of amoxicillin by O3/Fenton process in a rotating packed bed

Abstract In this study, simulated amoxicillin wastewater was treated by the O 3 /Fenton process in a rotating packed bed (RPB) and the results were compared with the Fenton process and the O 3 followed by Fenton (O 3  + Fenton) process. The chemical oxygen demand (COD) removal rate and the ratio of 5-day biological oxygen demand to chemical oxygen demand (BOD 5 /COD) in the O 3 /Fenton process were approximately 17% and 26%, respectively, higher than those in the O 3  + Fenton process with an initial pH of 3. The COD removal rate of the amoxicillin solution reached maximum at the Fe(II) concentration of 0.6 mM, temperature of 25 °C, rotation speed of 800 rpm and initial pH of 3. The BOD 5 /COD of the amoxicillin solution increased from 0 to 0.38 after the solution was treated by the O 3 /Fenton process. Analysis of the intermediates indicated that the pathway of amoxicillin degradation in the O 3 /Fenton process was similar to that in the O 3  + Fenton process. Contrast experiment results showed that amoxicillin degradation was significantly intensified in the RPB.