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通过侧向曝气和改性阴极增强电芬顿系统中的原位 HO 电合成和渗滤液浓缩降解。

Enhanced in situ HO electrosynthesis and leachate concentrate degradation through side-aeration and modified cathode in an electro-Fenton system.

机构信息

Faculty of Environment and Life, Beijing University of Technology, No.100 Pingleyuan, Chaoyang District, Beijing 100124, China.

Faculty of Environment and Life, Beijing University of Technology, No.100 Pingleyuan, Chaoyang District, Beijing 100124, China.

出版信息

Waste Manag. 2024 Sep 15;186:35-45. doi: 10.1016/j.wasman.2024.05.047. Epub 2024 Jun 8.

Abstract

The active graphite felt (GF) catalytic layer was effectively synthesized through a wet ultrasonic impregnation-calcination method, modified with CB and PTFE, and implemented in a pioneering side-aeration electrochemical in-situ HO reactor. The optimal mass ratio (CB: PTFE 1:4) for the modified cathode catalytic layer was determined using a single-factor method. Operating under optimum conditions of initial pH 5, 0.5 L/min air flow, and a current density of 9 mA/cm, the system achieved a remarkable maximum HO accumulation of 560 mg/L, with the HO production capacity consistently exceeding 95 % over 6 usage cycles. The refined mesoporous structure and improved three-phase interface notably amplified oxygen transfer, utilization, and HO yield. Side aeration led to an oxygen concentration near the cathode reaching 20 mg/L, representing a five-fold increase compared to the 3.95 mg/L achieved with conventional bottom aeration. In the final application, the reaction system exhibited efficacy in the degradation of landfill leachate concentrate. After a 60-minute reaction, complete removal of chroma was attained, and the TOC degradation rate surpassed 60 %, marking a sixfold improvement over the conventional system. These results underscore the substantial potential of the system in HO synthesis and environmental remediation.

摘要

通过湿超声浸渍-煅烧法有效合成了活性石墨毡(GF)催化层,并用 CB 和 PTFE 进行了改性,并在开创性的侧向曝气电化学原位 HO 反应器中实施。通过单因素法确定了改性阴极催化层的最佳质量比(CB:PTFE 1:4)。在初始 pH 值为 5、空气流速为 0.5 L/min 和电流密度为 9 mA/cm 的最佳条件下运行时,该系统实现了显著的最大 HO 积累量 560 mg/L,并且在 6 个使用周期内,HO 的产率始终超过 95%。精细的介孔结构和改进的三相界面显著放大了氧气的转移、利用和 HO 的产率。侧向曝气使得阴极附近的氧气浓度达到 20 mg/L,比传统底部曝气的 3.95 mg/L 增加了五倍。在最终的应用中,反应系统在降解垃圾渗滤液浓缩物方面表现出了功效。反应 60 分钟后,色度完全去除,TOC 降解率超过 60%,比传统系统提高了六倍。这些结果突显了该系统在 HO 合成和环境修复方面的巨大潜力。

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