Multistage Generation Mechanisms of Reactive Oxygen Species and Reactive Chlorine Species in a Synergistic System of Anodic Oxidation Coupled with in Situ Free Chlorine and H<sub>2</sub>O<sub>2</sub> Production

Electro-oxidation (EO) is an efficient approach to removing refractory organics in wastewater. However, the interference from chlorine ions (Cl<sup>-</sup>) can generate reactive chlorine species (RCS), potentially leading to the production of undesirable chlorinated byproducts. A novel approach involving the cathodic oxygen reduction reaction (ORR) for in situ H<sub>2</sub>O<sub>2</sub> production has emerged as a promising strategy to counteract this issue. This study systematically investigated the dynamics and transformation of RCS and reactive oxygen species (ROS) in an ORR/chloride-containing EO (EO-Cl) system, elucidating their respective roles in organic removal and chlorinated byproduct minimization. Distinct generation rates and patterns were observed for free chlorine and H<sub>2</sub>O<sub>2</sub> in the ORR/EO-Cl system. The rapid generation of free chlorine at the anode quickly reached a dynamic equilibrium, which contrasted with the moderate, continuous cathodic production of H<sub>2</sub>O<sub>2</sub>, resulting in considerable H<sub>2</sub>O<sub>2</sub> accumulation over time. This difference established kinetics-driven ROS and RCS formation and distribution, influencing the subsequent organic degradation process. Three distinct stages were identified in the degradation process. In stage I, free chlorine was the primary species, along with reactive species including Cl<sub>2</sub><sup>•-</sup>, <sup>1</sup>O<sub>2</sub>, ClO<sup>•</sup>, HO<sup>•</sup>, and Cl<sup>•</sup>. In stage II, the gradual accumulation of H<sub>2</sub>O<sub>2</sub> consumed free chlorine, favoring the formation of <sup>1</sup>O<sub>2</sub> and HO<sup>•</sup>. In stage III, excessive H<sub>2</sub>O<sub>2</sub> quenched the free radicals. Insights into these multistage mechanisms reveal that the rapid degradation of chlorinated byproducts by <sup>1</sup>O<sub>2</sub> and HO<sup>•</sup> occurs in stage II of the ORR/EO-Cl system.

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Publication Details

Journal
Environmental Science & Technology
Published
2024-12-11
DOI
https://doi.org/10.1021/acs.est.4c09855
Citations
31
Primary Topic
Advanced oxidation water treatment
Type
article
Field-Weighted Citation Impact
6.25

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article

Multistage Generation Mechanisms of Reactive Oxygen Species and Reactive Chlorine Species in a Synergistic System of Anodic Oxidation Coupled with in Situ Free Chlorine and H2O2 Production

Shujuan Meng, Ao Zhang, Dawei Liang, Yu Chen et al.
31 citations
Environmental Science & Technology
Advanced oxidation water treatment
6.25
article

Multistage Generation Mechanisms of Reactive Oxygen Species and Reactive Chlorine Species in a Synergistic System of Anodic Oxidation Coupled with in Situ Free Chlorine and H2O2 Production

Shujuan Meng, Ao Zhang, Dawei Liang, Yu Chen, Xiaohu Li, Chao Qu, Jingyun Fang, Na Ren
article en
31 citations

Abstract

Electro-oxidation (EO) is an efficient approach to removing refractory organics in wastewater. However, the interference from chlorine ions (Cl<sup>-</sup>) can generate reactive chlorine species (RCS), potentially leading to the production of undesirable chlorinated byproducts. A novel approach involving the cathodic oxygen reduction reaction (ORR) for in situ H<sub>2</sub>O<sub>2</sub> production has emerged as a promising strategy to counteract this issue. This study systematically investigated the dynamics and transformation of RCS and reactive oxygen species (ROS) in an ORR/chloride-containing EO (EO-Cl) system, elucidating their respective roles in organic removal and chlorinated byproduct minimization. Distinct generation rates and patterns were observed for free chlorine and H<sub>2</sub>O<sub>2</sub> in the ORR/EO-Cl system. The rapid generation of free chlorine at the anode quickly reached a dynamic equilibrium, which contrasted with the moderate, continuous cathodic production of H<sub>2</sub>O<sub>2</sub>, resulting in considerable H<sub>2</sub>O<sub>2</sub> accumulation over time. This difference established kinetics-driven ROS and RCS formation and distribution, influencing the subsequent organic degradation process. Three distinct stages were identified in the degradation process. In stage I, free chlorine was the primary species, along with reactive species including Cl<sub>2</sub><sup>•-</sup>, <sup>1</sup>O<sub>2</sub>, ClO<sup>•</sup>, HO<sup>•</sup>, and Cl<sup>•</sup>. In stage II, the gradual accumulation of H<sub>2</sub>O<sub>2</sub> consumed free chlorine, favoring the formation of <sup>1</sup>O<sub>2</sub> and HO<sup>•</sup>. In stage III, excessive H<sub>2</sub>O<sub>2</sub> quenched the free radicals. Insights into these multistage mechanisms reveal that the rapid degradation of chlorinated byproducts by <sup>1</sup>O<sub>2</sub> and HO<sup>•</sup> occurs in stage II of the ORR/EO-Cl system.

Environmental Science & TechnologyVol. 58(51)
Sun Yat-sen University (CN), Beijing University of Technology (CN), Beihang University (CN)
National Natural Science Foundation of China, Beijing Municipal Natural Science Foundation, Fundamental Research Funds for the Central Universities
Openalex Percentile: Top 3%
Advanced oxidation water treatment
6.25
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