{"title":"非线性拉伸流中圆柱体周围的传质","authors":"Moshe Favelukis","doi":"10.1002/cjce.25553","DOIUrl":null,"url":null,"abstract":"<p>In this theoretical report, we explored the transfer of mass around an infinite cylinder in a nonlinear extensional creeping flow, and at large Peclet numbers. First, we inspected the fluid mechanics problem, which is governed by a single dimensionless parameter: the nonlinear intensity of the flow (<i>E</i>). The fluid motion in the presence of the cylinder suggests interesting features such as closed circulations (<i>E</i> > 2/3) and separating surfaces (<i>E</i> < 0), both phenomena which are absent in the linear case (<i>E</i> = 0). Next, we examined the transfer of mass, where three different regions have been distinguished. In the first one (−2/9 < <i>E</i> < 2/3), which also includes the linear case, the thin concentration boundary layer, at each quarter, covers the entire cylinder surface. In the next one (<i>E</i> > 2/3), the closed circulation, which is in contact with the cylinder surface, reduces the length of the concentration boundary layer. In the last one (<i>E</i> < −2/9), separating surfaces touching the surface of the cylinder and creating, at each quarter, two concentration boundary layers flowing in opposite directions. There is a range (−0.340 < <i>E</i> < 0), where the mass transfer is lower than the linear case, with a minimum at <i>E</i> = −2/9 = −0.222. From this point, and in both directions, as |<i>E</i>| increases, the rate of mass transfer also increases.</p>","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"103 7","pages":"3444-3453"},"PeriodicalIF":1.6000,"publicationDate":"2024-11-20","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Mass transfer around a cylinder in a nonlinear extensional flow\",\"authors\":\"Moshe Favelukis\",\"doi\":\"10.1002/cjce.25553\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p>In this theoretical report, we explored the transfer of mass around an infinite cylinder in a nonlinear extensional creeping flow, and at large Peclet numbers. First, we inspected the fluid mechanics problem, which is governed by a single dimensionless parameter: the nonlinear intensity of the flow (<i>E</i>). The fluid motion in the presence of the cylinder suggests interesting features such as closed circulations (<i>E</i> > 2/3) and separating surfaces (<i>E</i> < 0), both phenomena which are absent in the linear case (<i>E</i> = 0). Next, we examined the transfer of mass, where three different regions have been distinguished. In the first one (−2/9 < <i>E</i> < 2/3), which also includes the linear case, the thin concentration boundary layer, at each quarter, covers the entire cylinder surface. In the next one (<i>E</i> > 2/3), the closed circulation, which is in contact with the cylinder surface, reduces the length of the concentration boundary layer. In the last one (<i>E</i> < −2/9), separating surfaces touching the surface of the cylinder and creating, at each quarter, two concentration boundary layers flowing in opposite directions. There is a range (−0.340 < <i>E</i> < 0), where the mass transfer is lower than the linear case, with a minimum at <i>E</i> = −2/9 = −0.222. From this point, and in both directions, as |<i>E</i>| increases, the rate of mass transfer also increases.</p>\",\"PeriodicalId\":9400,\"journal\":{\"name\":\"Canadian Journal of Chemical Engineering\",\"volume\":\"103 7\",\"pages\":\"3444-3453\"},\"PeriodicalIF\":1.6000,\"publicationDate\":\"2024-11-20\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Canadian Journal of Chemical Engineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://onlinelibrary.wiley.com/doi/10.1002/cjce.25553\",\"RegionNum\":4,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Canadian Journal of Chemical Engineering","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/cjce.25553","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Mass transfer around a cylinder in a nonlinear extensional flow
In this theoretical report, we explored the transfer of mass around an infinite cylinder in a nonlinear extensional creeping flow, and at large Peclet numbers. First, we inspected the fluid mechanics problem, which is governed by a single dimensionless parameter: the nonlinear intensity of the flow (E). The fluid motion in the presence of the cylinder suggests interesting features such as closed circulations (E > 2/3) and separating surfaces (E < 0), both phenomena which are absent in the linear case (E = 0). Next, we examined the transfer of mass, where three different regions have been distinguished. In the first one (−2/9 < E < 2/3), which also includes the linear case, the thin concentration boundary layer, at each quarter, covers the entire cylinder surface. In the next one (E > 2/3), the closed circulation, which is in contact with the cylinder surface, reduces the length of the concentration boundary layer. In the last one (E < −2/9), separating surfaces touching the surface of the cylinder and creating, at each quarter, two concentration boundary layers flowing in opposite directions. There is a range (−0.340 < E < 0), where the mass transfer is lower than the linear case, with a minimum at E = −2/9 = −0.222. From this point, and in both directions, as |E| increases, the rate of mass transfer also increases.
期刊介绍:
The Canadian Journal of Chemical Engineering (CJChE) publishes original research articles, new theoretical interpretation or experimental findings and critical reviews in the science or industrial practice of chemical and biochemical processes. Preference is given to papers having a clearly indicated scope and applicability in any of the following areas: Fluid mechanics, heat and mass transfer, multiphase flows, separations processes, thermodynamics, process systems engineering, reactors and reaction kinetics, catalysis, interfacial phenomena, electrochemical phenomena, bioengineering, minerals processing and natural products and environmental and energy engineering. Papers that merely describe or present a conventional or routine analysis of existing processes will not be considered.