分散式电解消毒工程,在饮用水氯化物含量变化的情况下保持稳定的氯气生成。

Aksana Atrashkevich, Sergi Garcia-Segura
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摘要

原位电氯化法可以为分散式水消毒提供高效可行的解决方案。遗憾的是,目前仅有少数研究探讨了具有代表性流量的单程流动池系统在家庭中的应用,尤其是在氯化物浓度变化的情况下。这项工作旨在评估单程中的阳极材料,并研究横流速度、电流密度和氯化物浓度对氯气产量和能耗等各种反应的影响。主要目的是确定流动池是否能在持续运行的情况下达到理想的氯含量,而同时水中的氯化物含量会发生变化。利用不同的代表性阳极(包括 Ti/RuO2、Ti/IrO2 和掺硼金刚石),在单程设置中评估了氯(Cl2/HOCl/OCl-)、二氧化氯(ClO2)的产生量和有毒氧阴离子(ClO3 -、ClO4 -)。在这些材料中,Ti/RuO2 阳极最适合有效生成氯,同时最大限度地减少 ClO3 - 和 ClO4 - 的形成。在流动池中使用 Ti/RuO2 阳极进行原位电氯化的性能表明,横流速度对氯生成的影响最大,而氯含量和电流密度则主要影响能耗。对操作参数的优化表明,即使氯化物浓度在 50 至 250 毫克/升之间大幅波动,也能保持 2 至 4 毫克/升的稳定氯浓度,从而使每 634 升处理量的日能耗低于 0.07 千瓦时(即小于 0.11 Wh/升)。这些实验结果为将电消毒系统提升到更高的技术准备水平带来了希望。
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Engineering decentralized electrodisinfection to sustain consistent chlorine generation under varying drinking water chloride content.

In situ electrochlorination can offer an efficient and feasible solution to enable decentralized water disinfection. Unfortunately, there has been only a limited number of studies exploring single-pass flow cell systems with representative flowrates used at household level, particularly under varying chloride concentrations. This work aims to assess anode materials in a single pass and examine the impact of cross velocity, current density, and chloride concentration on various responses such as chlorine production and energy consumption. The primary objective is to determine whether the flow cell can achieve desirable chlorine levels under consistent operation while chloride content of water varies. Chlorine (Cl2/HOCl/OCl-), chlorine dioxide (ClO2) production, and toxic oxyanions (ClO3 -, ClO4 -) were assessed in a single pass setup utilizing different representative anodes including Ti/RuO2, Ti/IrO2, and Boron-doped diamond. Among these materials, the Ti/RuO2 anode emerged as the most suitable for effective chlorine generation while minimizing the formation of ClO3 - and ClO4 -. The performance of in situ electrochlorination using the Ti/RuO2 anode in the flow cell revealed that cross velocity exerted the most significant influence on chlorine generation, while chloride content and current density primarily impacted energy consumption. Optimization of the operating parameters illustrated that stable chlorine concentrations ranging from 2 to 4 mg L-1 could be maintained even with significant fluctuations in chloride concentration from 50 to 250 mg L-1, resulting in a daily energy consumption of less than 0.07 kWh per treated volume of 634 L (i.e., < 0.11 Wh L-1). These experimental findings hold promise for advancing electrodisinfection systems to higher technological readiness level.

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Engineering decentralized electrodisinfection to sustain consistent chlorine generation under varying drinking water chloride content.
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