Abstract

Abstract The feasibility of using thermally activated persulfate (TAP) to degrade chloramphenicol (CAP) in aqueous solution was evaluated. Results showed that CAP degradation followed a pseudo-first-order model under all conditions tested and the observed rate constants well fitted the Arrhenius equation. CAP degradation rate constants (kobs) increased with increased temperature and sodium persulfate (SPS) dosage. A lower pH resulted in a greater increase in CAP degradation and the highest degradation efficiency was obtained at pH 2.96. Scavenging tests suggested that sulfate radicals ( SO 4 - ) predominated under acidic conditions, whereas hydroxyl radicals (HO ) gradually predominated under alkaline conditions. Coexisting Cl− ions slightly enhanced decomposition at an appropriate concentration ([Cl−]0/[SPS]0 = 1:1) but inhibited degradation at other levels. The effects of NO 3 - , H 2 PO 4 - and HPO 4 2 - on CAP degradation were negligible, whereas NO 2 - , HCO 3 - , and HA significantly inhibited CAP decomposition. The highest degradation rate was achieved with a single SPS injection. Considering that CAP oxidation in the multi-phases of wastewater matrices by TAP presented slower kinetics, 62.2–96.3% removal efficiencies were achieved within 160 min. The TOC removal ratios after 160 min TAP oxidation increased from 10.7% to 90.1% as the [SPS]0/[CAP]0 increased from 1:1 to 80:1, respectively. Overall, eleven intermediate products during TAP oxidation were identified, and a primary reaction mechanism was proposed.

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