Comparative Study of Atenolol Photodegradation by Fe(III)-Complex Activated Peroxydisulfate/Peroxymonosulfate Systems

Over the past 20 years, the iron-activated persulfate systems have been widely used for removing pharmaceuticals and personal care products (PPCPs) from water. However, slow Fe(III)/Fe(II) redox cycling and precipitation of iron, unless in very acidic conditions, were the main limitations. Thus, two ligand-assisted Fe(III)/persulfate systems, Fe(III)-acetohydroxamic acid (AHA)/peroxydisulfate (PDS) and Fe(III)-nitrilotriacetic acid (NTA)/peroxymonosulfate (PMS), were comparatively investigated for the degradation of atenolol (ATL) in this study. The experimental results showed that the Fe(III)-NTA/PMS system worked much better than the AHA system. However, the cost of PMS is higher than that of PDS, which should be considered. The primary advantage of the NTA system was its ability to overcome the pH limitations. It worked well over a wide pH range (3.0–10.0), whereas the AHA system could only be used in a narrower pH window (pH 2.4 to 6.5). The investigation of radicals that contributed to ATL degradation revealed that sulfate radicals (SO4•−) were dominant in the NTA system, while hydroxyl radicals (•OH) and SO4•− were the primary and secondary radicals in the AHA system. These results provided useful insight into the comparative behavior of two ligand-assisted Fe(III)/persulfate systems for ATL degradation, with the Fe(III)-NTA/PMS system showing clear potential under neutral or near-neutral conditions, while Fe(III)-AHA/PDS may still represent a lower-cost option under acidic conditions.

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Publication Details

Journal
Separations
Published
2026-04-22
DOI
https://doi.org/10.3390/separations13050130
Primary Topic
Advanced oxidation water treatment
Type
article
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article

Comparative Study of Atenolol Photodegradation by Fe(III)-Complex Activated Peroxydisulfate/Peroxymonosulfate Systems

Yanlin Wu, Lanhua Luo, 石尚华, Gilles Mailhot et al.
Separations
Advanced oxidation water treatment
article

Comparative Study of Atenolol Photodegradation by Fe(III)-Complex Activated Peroxydisulfate/Peroxymonosulfate Systems

Yanlin Wu, Lanhua Luo, 石尚华, Gilles Mailhot, Yuan Li, Xiaoning Wang, Wenbo Dong
article en

Abstract

Over the past 20 years, the iron-activated persulfate systems have been widely used for removing pharmaceuticals and personal care products (PPCPs) from water. However, slow Fe(III)/Fe(II) redox cycling and precipitation of iron, unless in very acidic conditions, were the main limitations. Thus, two ligand-assisted Fe(III)/persulfate systems, Fe(III)-acetohydroxamic acid (AHA)/peroxydisulfate (PDS) and Fe(III)-nitrilotriacetic acid (NTA)/peroxymonosulfate (PMS), were comparatively investigated for the degradation of atenolol (ATL) in this study. The experimental results showed that the Fe(III)-NTA/PMS system worked much better than the AHA system. However, the cost of PMS is higher than that of PDS, which should be considered. The primary advantage of the NTA system was its ability to overcome the pH limitations. It worked well over a wide pH range (3.0–10.0), whereas the AHA system could only be used in a narrower pH window (pH 2.4 to 6.5). The investigation of radicals that contributed to ATL degradation revealed that sulfate radicals (SO4•−) were dominant in the NTA system, while hydroxyl radicals (•OH) and SO4•− were the primary and secondary radicals in the AHA system. These results provided useful insight into the comparative behavior of two ligand-assisted Fe(III)/persulfate systems for ATL degradation, with the Fe(III)-NTA/PMS system showing clear potential under neutral or near-neutral conditions, while Fe(III)-AHA/PDS may still represent a lower-cost option under acidic conditions.

SeparationsVol. 13(5)
Centre National de la Recherche Scientifique (FR), Shanghai Polytechnic University (CN), Fudan University (CN), Soochow University (CN), Institut de Chimie de Clermont-Ferrand (FR)
Univerzita Komenského v Bratislave, China Scholarship Council
Clean water and sanitation
Openalex Percentile: Top 17%
Advanced oxidation water treatment
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