{"title":"Investigation on the performance of plasma microreactor with cavitation channel for the oxidation degradation of methylene blue","authors":"Ruiqi Gao , Jianfeng Yu , Jiejun Zhao , Huiyang Liu","doi":"10.1016/j.cherd.2025.07.052","DOIUrl":null,"url":null,"abstract":"<div><div>Ozonation degradation has attracted extensive attention due to its effectiveness in oxidizing organic pollutants. As a typical ozone (O<sub>3</sub>) 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 O<sub>3</sub>-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.</div></div>","PeriodicalId":10019,"journal":{"name":"Chemical Engineering Research & Design","volume":"221 ","pages":"Pages 1-10"},"PeriodicalIF":3.9000,"publicationDate":"2025-08-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Research & Design","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0263876225004101","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
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.
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.