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在无膜电化学系统中通过集成吸附和还原降解去除消毒副产物。

Removal of disinfection byproducts through integrated adsorption and reductive degradation in a membrane-less electrochemical system.

机构信息

Department of Energy, Environmental and Chemical Engineering, Washington University in St. Louis, St. Louis, MO 63130, United States.

Department of Chemical Engineering, Qatar University, Doha, Qatar.

出版信息

Water Res. 2023 Oct 1;244:120519. doi: 10.1016/j.watres.2023.120519. Epub 2023 Aug 23.

Abstract

Proper control/removal of disinfection byproducts (DBPs) is important to drinking water safety and human health. In this study, a membrane-less electrochemical system was developed and investigated to remove DPBs through integrated adsorption and reduction by granular activated carbon (GAC)-based cathode. Representative DPBs including trihalomethanes and haloacetonitriles at drinking water concentrations were used for removal experiments. The proposed system achieved >70% removal of most DBPs in a batch mode. The comparison with control tests under either open circuit or hydrolysis demonstrated the advantages of electrochemical treatment, which not only realized higher DPBs removal but also extended GAC cathode lifetime. Such advantages were further demonstrated with continuous treatment. High dechlorination and debromination efficiencies were obtained in both batch (82.2 and 94.3%) and continuous (79.3 and 87.6%) reactors. DBPs removal was mainly contributed by the electrochemical reduction and adsorption by the GAC-based cathode, while anode showed little oxidizing effect on DBPs and halide ions. Dehalogenated products of chloroform and dichloroacetonitrile were identified with toxicity reduction. The energy consumption of the continuously operated system was estimated to be 0.28 to 0.16 kWh m. The proposed system has potential applications for wastewater reuse or further purification of drinking water.

摘要

有效控制/去除消毒副产物(DBPs)对于饮用水安全和人类健康至关重要。在本研究中,开发了一种无膜电化学系统,通过基于颗粒活性炭(GAC)的阴极的吸附和还原集成来去除 DBP。以饮用水浓度的代表性 DBP,包括三卤甲烷和卤乙腈,进行了去除实验。该系统在批量模式下实现了大多数 DBP 的>70%去除。与开路或水解条件下的对照实验相比,电化学处理具有优势,不仅实现了更高的 DBP 去除率,而且延长了 GAC 阴极的寿命。这种优势在连续处理中得到了进一步证明。在间歇式(82.2%和 94.3%)和连续式(79.3%和 87.6%)反应器中均获得了较高的脱氯和脱溴效率。DBP 的去除主要归因于电化学还原和 GAC 基阴极的吸附,而阳极对 DBP 和卤化物离子几乎没有氧化作用。三氯甲烷和二氯乙腈的脱卤产物的毒性降低。连续运行系统的能耗估计为 0.28 至 0.16 kWh·m。该系统具有废水再利用或饮用水进一步净化的应用潜力。

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