{"title":"Mass transfer for droplets and bubbles with a stagnant surfactant cap - an analytical solution of the advection-diffusion equation","authors":"Marcel minor","doi":"10.1016/j.ces.2025.121948","DOIUrl":null,"url":null,"abstract":"The mass transfer rate to a liquid droplet or bubble, in motion in another immiscible fluid, is studied when the interface is partly covered by a stagnant surfactant cap. We present an analytical solution by solving the equations for advection diffusion under conditions of creeping flow and a thin concentration boundary layer. The empirical relation between the Sherwood number and drag coefficient for partly coated bubbles proposed in literature that accurately describes both experiments and numerical simulations of CO<span><span style=\"\"><math><msub is=\"true\"><mrow is=\"true\"></mrow><mn is=\"true\">2</mn></msub></math></span><span style=\"font-size: 90%; display: inline-block;\" tabindex=\"0\"></span><script type=\"math/mml\"><math><msub is=\"true\"><mrow is=\"true\"></mrow><mn is=\"true\">2</mn></msub></math></script></span>-release from a rising bubble follows from our analytical solution. Mass transfer and drag force are interrelated as demonstrated mathematically.This study improves the understanding of mass transfer to partly covered droplets and bubbles at time scales where these are created such as in processing equipment or microfluidic devices as well as for semi-stationary situations where partly covered bubbles or droplets exist as in froth flotation, bubble columns or extraction processes.","PeriodicalId":271,"journal":{"name":"Chemical Engineering Science","volume":"14 1","pages":""},"PeriodicalIF":4.1000,"publicationDate":"2025-05-30","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Science","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1016/j.ces.2025.121948","RegionNum":2,"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
The mass transfer rate to a liquid droplet or bubble, in motion in another immiscible fluid, is studied when the interface is partly covered by a stagnant surfactant cap. We present an analytical solution by solving the equations for advection diffusion under conditions of creeping flow and a thin concentration boundary layer. The empirical relation between the Sherwood number and drag coefficient for partly coated bubbles proposed in literature that accurately describes both experiments and numerical simulations of CO-release from a rising bubble follows from our analytical solution. Mass transfer and drag force are interrelated as demonstrated mathematically.This study improves the understanding of mass transfer to partly covered droplets and bubbles at time scales where these are created such as in processing equipment or microfluidic devices as well as for semi-stationary situations where partly covered bubbles or droplets exist as in froth flotation, bubble columns or extraction processes.
期刊介绍:
Chemical engineering enables the transformation of natural resources and energy into useful products for society. It draws on and applies natural sciences, mathematics and economics, and has developed fundamental engineering science that underpins the discipline.
Chemical Engineering Science (CES) has been publishing papers on the fundamentals of chemical engineering since 1951. CES is the platform where the most significant advances in the discipline have ever since been published. Chemical Engineering Science has accompanied and sustained chemical engineering through its development into the vibrant and broad scientific discipline it is today.