Effects of sodium persulfate and percarbonate on the degradation of 2,4- dichlorophenol in a dielectric barrier discharge reactor

IF 3.8 3区 工程技术 Q3 ENERGY & FUELS Chemical Engineering and Processing - Process Intensification Pub Date : 2024-08-23 DOI:10.1016/j.cep.2024.109953
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Abstract

The detection of micropollutants in surface and groundwater bodies has drawn global concern due to their environmental persistence and risk to human and aquatic life. The dielectric barrier discharge (DBD) plasma reactor was employed to degrade the micropollutant 2,4-dichlorophenol (2,4-DCP). The efficiency of the reactor was investigated, and the plasma degradation process was intensified by introducing three eco-friendly oxidants, sodium percarbonate (SPC), sodium persulfate (SPS), and hydrogen peroxide (HPO), into the reactor. Results indicated that 2,4-DCP removal increased from 62.73 % to 76.37 %, 81.93 %, 100 %, and 90.02 % when 1 mM SPC, 1 mM SPS, 3 mM HPO, and 1 mM SPS + 0.33 mM SPC was added to the wastewater solution, respectively. The synergy between the oxidants and the plasma in the DBD reactor was also explored. The largest synergistic factor (1.792) was achieved when 3 mM HPO was added to the DBD reactor, followed by 0.089 for 1 mM SPC, 0.07 for 1 mM SPS, and 0.041 for 1 mM SPS+0.33 mM SPC. The main active species that catalyzed 2,4-DCP degradation were hydroxyl and sulfate radicals, and introducing the oxidants augmented their production in the solution. The synergy between the DBD+SPS+SPC led to a 58.7 % total organic carbon removal. In conclusion, the 2,4-DCP degradation intermediates and mechanisms were deduced accordingly. The findings reaffirm the effectiveness of the oxidant-coupled DBD reactor in the degradation of micropollutants.

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过硫酸钠和过碳酸钠对介质阻挡放电反应器中 2,4- 二氯苯酚降解的影响
地表水和地下水中检测到的微污染物因其环境持久性以及对人类和水生生物的风险而引起全球关注。采用介质阻挡放电(DBD)等离子体反应器降解微污染物 2,4-二氯苯酚(2,4-DCP)。研究了反应器的效率,并通过在反应器中引入过碳酸钠(SPC)、过硫酸钠(SPS)和过氧化氢(HPO)这三种环保型氧化剂来强化等离子体降解过程。结果表明,在废水中加入 1 mM SPC、1 mM SPS、3 mM HPO 和 1 mM SPS + 0.33 mM SPC 时,2,4-二氯丙醇的去除率分别从 62.73% 增加到 76.37%、81.93%、100% 和 90.02%。此外,还探讨了 DBD 反应器中氧化剂与等离子体之间的协同作用。在 DBD 反应器中加入 3 mM HPO 时协同系数最大(1.792),其次是 1 mM SPC 0.089、1 mM SPS 0.07 和 1 mM SPS+0.33 mM SPC 0.041。催化 2,4-DCP 降解的主要活性物质是羟基自由基和硫酸根自由基,氧化剂的引入增加了溶液中羟基自由基和硫酸根自由基的产生。DBD+SPS+SPC 的协同作用使有机碳的总去除率达到 58.7%。总之,研究人员据此推断出了 2,4-DCP 降解的中间产物和机理。研究结果再次证实了氧化剂耦合 DBD 反应器在降解微污染物方面的有效性。
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来源期刊
CiteScore
7.80
自引率
9.30%
发文量
408
审稿时长
49 days
期刊介绍: Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.
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