Unraveling different mechanisms of persulfate activation by graphite felt anode and cathode to destruct contaminants of emerging concern
[Display omitted] •Electrolyte is a key factor in GF anode/PS system, but not in GF cathode/PS system.•Superoxide radicals are significant for activation of PS in GF cathode/PS system.•SO4•−, OH•, and 1O2 are responsible for ATZ degradation in GF anode/PS system.•Eight products of ATZ were identifie...
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Veröffentlicht in: | Applied catalysis. B, Environmental Environmental, 2019-09, Vol.253, p.140-148 |
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Sprache: | eng |
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•Electrolyte is a key factor in GF anode/PS system, but not in GF cathode/PS system.•Superoxide radicals are significant for activation of PS in GF cathode/PS system.•SO4•−, OH•, and 1O2 are responsible for ATZ degradation in GF anode/PS system.•Eight products of ATZ were identified in GF anode and cathode/PS system.
The electro-activation of persulfate (PS) by graphite felt (GF) electrode is a novel advanced oxidation process applied for the degradation of contaminants of emerging concern (CECs). Both GF anode and cathode can electro-activate PS to degrade CECs, including atrazine (ATZ), bisphenol S, ethinylestradiol, and ibuprofen. The study examines the removal performance of ATZ in sulfate, nitrate, and perchlorate electrolyte. The degradation of ATZ followed the order of sulfate (36.3 L (Ah)−1) > perchlorate (22.2 L (Ah)−1) > nitrate (5.8 L (Ah)−1) in GF anode/PS system, while electrolytes had little influence on the degradation of ATZ (15.8–21.3 L (Ah)−1) in GF cathode/PS system. The mechanisms of PS electro-activation by GF anode and GF cathode were compared and investigated for the first time, through kinetic experiments, radical identification, and products analysis. Quenching experiments demonstrated that O2− and 1O2 were generated in GF cathode/PS and GF anode/PS systems respectively, besides HO and SO4−. Degradation pathways of ATZ in these two systems showed slight difference, and a total of eight transformation products of ATZ were identified. Acute toxicity of the treated ATZ solution decreased at the beginning and then increased in both systems at electric charge of 0.11 Ah L−1. Furthermore, both GF electrodes/PS systems exhibited satisfactory performance for actual effluent from wastewater treatment plants in the presence of 30 mM perchlorate (with ATZ removal of 78% at electric charge of 0.11 Ah L−1), leaving a potential possibility for its practical application. |
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ISSN: | 0926-3373 1873-3883 |
DOI: | 10.1016/j.apcatb.2019.04.030 |