Abstract

The activity of iron oxychloride (FeOCl) in advanced oxidation processes (AOPs) was limited by the redox cycle of Fe(III)/Fe(II). To resolve this problem, FeOCl loading on WS2 (FW-X) was successfully synthesized with the different ratios of Fe/W (X = 0.5, 1, 2, 3) to active peroxymonosulfate (PMS). Among them, FW-3 displayed excellent catalytic performance which activated 0.5 mM PMS to degrade 97 % thiamphenicol (TAP) in 45 min. FW-3/PMS performed well in a wide pH range (3–10). Besides, the anions (Cl-,NO3-,H2PO4-,HPO42-andHCO3-) and humic acid inhibited the oxidation of TAP in varying degrees. During the catalytic process, H2O and PMS were adsorbed on the surface of FW-3 with the formation of surface hydroxyl groups (Fe–OH) and Fe–HOOSO3. Surface hydroxyls as a bridge promoted the electron transfer between O–O bond and Fe sites. Then O–O bond broke to generate reactive oxygen species (ROS, HO·, SO4∙-, Fe(IV), O2∙- and 1O2), and SO4∙- was the dominant ROS for the degradation of TAP. Additionally, WS2 as a co-catalyst broke the limitation of the iron redox cycle. Under the attack of these ROS, TAP produced eighteen intermediates through four possible degradation pathways. According to ecotoxicity assessment, toxicity of some intermediates produced from path of S-C bond breakage was less harmful than TAP. After three consecutive cycles, FW-3 maintained outstanding catalytic performance. Additionally, FW-3/PMS possessed a good non-selectivity that could remove different contaminants. In a word, this paper proved the potential of FW-3/PMS in practical wastewater remediation.

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