Investigation on the performance of plasma microreactor with cavitation channel for the oxidation degradation of methylene blue

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Ruiqi Gao , Jianfeng Yu , Jiejun Zhao , Huiyang Liu
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引用次数: 0

Abstract

Ozonation degradation has attracted extensive attention due to its effectiveness in oxidizing organic pollutants. As a typical ozone (O3) generator, the plasma microreactor generates active oxygen species by ionizing gas-liquid streams in microchannels. However, insufficient mixing occurs between reactive oxygen species in the gas phase and the liquid phase due to the uniform width of the flow channel. Thus, a newly plasma microreactor with a cavitation channel was conceived to induce cavitation effects and increase the O3-liquid mass transfer intensity. The influence of three channel geometries on cavitation performance was clarified by fluid dynamic simulations. The hyperbolic channel showed higher cavitation intensity than the cylindrical and conical channels. By examining the effects of initial concentration, initial pH, inlet flow rate, and input voltage on the ozonation degradation of methylene blue, the optimal operating conditions were identified. Under optimal conditions, the plasma microreactor with a hyperbolic channel achieved a significant degradation rate of 95.7 % within 10 min. This work presents a new type of microreactor for the efficient degradation of dye pollutants.
空化通道等离子体微反应器氧化降解亚甲基蓝的性能研究
臭氧化降解因其对有机污染物的有效氧化而受到广泛关注。等离子体微反应器是一种典型的臭氧(O3)发生器,通过电离微通道内的气液流产生活性氧。然而,由于流道宽度均匀,气相和液相中的活性氧混合不足。因此,设计了一种新型的等离子体微反应器,通过空化通道诱导空化效应,提高o3 -液体传质强度。通过流体动力学模拟,阐明了三种通道几何形状对空化性能的影响。双曲线通道的空化强度高于圆柱形和锥形通道。通过考察初始浓度、初始pH、进口流速和输入电压对臭氧氧化降解亚甲基蓝的影响,确定了最佳操作条件。在最佳条件下,双曲通道等离子体微反应器在10 min内降解率达到95.7% %。提出了一种新型高效降解染料污染物的微反应器。
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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