Characteristics of Bubble Dispersion under Nonuniform Electric Field in an Up-Flow Bubbling System: From Charged Bubble to Charged Bubble Cluster

IF 3.8 3区 工程技术 Q2 ENGINEERING, CHEMICAL Industrial & Engineering Chemistry Research Pub Date : 2024-10-24 DOI:10.1021/acs.iecr.4c02627
Xiaojiang Liang, Jianan Luo, Weiwei Chen, Haotian Fei, Xuelei Ye, Wenhao Li, Yong Nie
{"title":"Characteristics of Bubble Dispersion under Nonuniform Electric Field in an Up-Flow Bubbling System: From Charged Bubble to Charged Bubble Cluster","authors":"Xiaojiang Liang, Jianan Luo, Weiwei Chen, Haotian Fei, Xuelei Ye, Wenhao Li, Yong Nie","doi":"10.1021/acs.iecr.4c02627","DOIUrl":null,"url":null,"abstract":"Electric dispersion is a novel and promising method for bubble dispersion. In this study, the laboratory scale bubbling reactor with a nonuniform electric field was established. A high-speed camera was used to observe and investigate the electric dispersion in a nitrogen biodiesel up-flow system. The results showed that dynamic characteristics of the bubble dispersion, including bubble volume, shape, and rising velocity, were strongly correlated with the electric field strength. The bubble could be controllably dispersed into numerous charged bubbles through electric dispersion, with the equivalent diameter decreasing from 1.88 to 0.64 mm. As a result, the charged bubble cluster was obtained with a Gaussian distribution. The number of the charged bubble cluster per cubic meter increased from 5.01 × 10<sup>5</sup> to 5.40 × 10<sup>7</sup>, which significantly improved the gas–liquid mass transfer area. Moreover, changes in gas and liquid velocities had little effect on the charged bubble cluster. Both the size and number density of the charged bubble cluster could be regulated by adjusting the electric field strength. Additionally, a model was developed to predict the mean size of the charged bubble cluster, with an average relative error of 6.37%. Overall, the results would provide a reference for the application of electric dispersion in bubbling reactors.","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"211 1","pages":""},"PeriodicalIF":3.8000,"publicationDate":"2024-10-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1021/acs.iecr.4c02627","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

Electric dispersion is a novel and promising method for bubble dispersion. In this study, the laboratory scale bubbling reactor with a nonuniform electric field was established. A high-speed camera was used to observe and investigate the electric dispersion in a nitrogen biodiesel up-flow system. The results showed that dynamic characteristics of the bubble dispersion, including bubble volume, shape, and rising velocity, were strongly correlated with the electric field strength. The bubble could be controllably dispersed into numerous charged bubbles through electric dispersion, with the equivalent diameter decreasing from 1.88 to 0.64 mm. As a result, the charged bubble cluster was obtained with a Gaussian distribution. The number of the charged bubble cluster per cubic meter increased from 5.01 × 105 to 5.40 × 107, which significantly improved the gas–liquid mass transfer area. Moreover, changes in gas and liquid velocities had little effect on the charged bubble cluster. Both the size and number density of the charged bubble cluster could be regulated by adjusting the electric field strength. Additionally, a model was developed to predict the mean size of the charged bubble cluster, with an average relative error of 6.37%. Overall, the results would provide a reference for the application of electric dispersion in bubbling reactors.

Abstract Image

查看原文
分享 分享
微信好友 朋友圈 QQ好友 复制链接
本刊更多论文
气泡在上流式气泡系统中的非均匀电场下的分散特性:从带电气泡到带电气泡簇
电分散是一种新颖而有前途的气泡分散方法。本研究建立了实验室规模的非均匀电场鼓泡反应器。使用高速相机观察和研究了氮气生物柴油上流式系统中的电分散情况。结果表明,气泡分散的动态特性,包括气泡体积、形状和上升速度,与电场强度密切相关。通过电分散,气泡可以可控地分散成许多带电气泡,等效直径从 1.88 毫米减小到 0.64 毫米。因此,得到的带电气泡簇呈高斯分布。每立方米带电气泡簇的数量从 5.01 × 105 增加到 5.40 × 107,从而显著提高了气液传质面积。此外,气体和液体速度的变化对带电气泡簇的影响很小。带电气泡簇的大小和数量密度都可以通过调节电场强度来调节。此外,还建立了一个模型来预测带电气泡簇的平均大小,平均相对误差为 6.37%。总之,研究结果将为起泡反应器中电分散的应用提供参考。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 去求助
来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.
期刊最新文献
Issue Publication Information Issue Editorial Masthead Magnesium-Promoted Catalytic Stability of the Cu/ZnO/ZrO2/Al2O3-MgO Catalyst in CO2 Hydrogenation to Methanol Nucleation Thermodynamics and Nucleation Kinetics of Ammonium Sulfate under the Synergistic Action of Ammonium Chloride and Ammonium Fluoride Quercetin–Copper Complexation-Based Porous Polymer for Chromium, Mercury, and Cadmium Metal Ion Adsorption: Experimental and Computational Study
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
现在去查看 取消
×
提示
确定
0
微信
客服QQ
Book学术公众号 扫码关注我们
反馈
×
意见反馈
请填写您的意见或建议
请填写您的手机或邮箱
已复制链接
已复制链接
快去分享给好友吧!
我知道了
×
扫码分享
扫码分享
Book学术官方微信
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术
文献互助 智能选刊 最新文献 互助须知 联系我们:info@booksci.cn
Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。
Copyright © 2023 Book学术 All rights reserved.
ghs 京公网安备 11010802042870号 京ICP备2023020795号-1