Enhancing the overall heat transfer coefficient through tube rotation of a heat exchanger: An analytical approach

Q3 Chemical Engineering
D. Pal, N. Subrahmanyam, Jayadeekshitha M, K. Raj, Mahesh Nallamothu
{"title":"Enhancing the overall heat transfer coefficient through tube rotation of a heat exchanger: An analytical approach","authors":"D. Pal, N. Subrahmanyam, Jayadeekshitha M, K. Raj, Mahesh Nallamothu","doi":"10.2174/2405520416666230102114948","DOIUrl":null,"url":null,"abstract":"\n\nFlow in an annulus between two concentric cylinders or pipes is very often observed, ranging its applications in many streams, namely, in steam generators, condensers, petroleum science and engineering, and various flow devices in chemical processing industries. The objective is to prove or understand the essence of parameters like heat transfer coefficient, mass transfer coefficient, etc., depending on such flow regimes. One such piece of equipment found in industry is a heat exchanger, where heat transfer occurs from one medium to another.\n\n\n\nThe present study majorly discusses increasing the heat transfer coefficient in the case of shell and tube heat exchangers with rotation of tubes and is restricted to a single tube inside a shell.\n\n\n\nThe methodology section can be broadly divided into two categories. First, the theoretical solution (obtained under certain assumptions) of the flow between two concentric cylinders, which includes both the rotation case and no rotation case. And second, ANSYS Fluent simulations have been presented at a steady state for both cases. All required conditions, dimensions of the chosen geometry, and assumptions have been clearly mentioned before getting into the discussion or along the way. Moreover, this study is a kind of comparative study between the conventional method of operating and rotation of tubes inside the shell and tube heat exchangers.\n\n\n\nThe results were positive from both the ways – theoretical and ANSYS, that there was a certain increase in the heat transfer coefficient. The overall heat transfer coefficient increased at varying flow rates (0.25kg/s, 0.5kg/s, and 1kg/s) at different speeds of rotation (100 RPM, 200 RPM, and 300 RPM).\n\n\n\nOne of the most common equipment in industries is heat exchanger. Parameters like heat transfer coefficient can be increased by rotating tube(s) of heat exchanger. This was presented using two approaches- analytical and simulation techniques. On varying RPM from 0 to 300, heat transfer coefficient increased by 69.1% for 1 kg/s, 124.7% for 0.5 kg/s, and 172.3% for 0.25 kg/s.\n","PeriodicalId":38021,"journal":{"name":"Recent Innovations in Chemical Engineering","volume":" ","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2023-01-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Recent Innovations in Chemical Engineering","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.2174/2405520416666230102114948","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"Chemical Engineering","Score":null,"Total":0}
引用次数: 0

Abstract

Flow in an annulus between two concentric cylinders or pipes is very often observed, ranging its applications in many streams, namely, in steam generators, condensers, petroleum science and engineering, and various flow devices in chemical processing industries. The objective is to prove or understand the essence of parameters like heat transfer coefficient, mass transfer coefficient, etc., depending on such flow regimes. One such piece of equipment found in industry is a heat exchanger, where heat transfer occurs from one medium to another. The present study majorly discusses increasing the heat transfer coefficient in the case of shell and tube heat exchangers with rotation of tubes and is restricted to a single tube inside a shell. The methodology section can be broadly divided into two categories. First, the theoretical solution (obtained under certain assumptions) of the flow between two concentric cylinders, which includes both the rotation case and no rotation case. And second, ANSYS Fluent simulations have been presented at a steady state for both cases. All required conditions, dimensions of the chosen geometry, and assumptions have been clearly mentioned before getting into the discussion or along the way. Moreover, this study is a kind of comparative study between the conventional method of operating and rotation of tubes inside the shell and tube heat exchangers. The results were positive from both the ways – theoretical and ANSYS, that there was a certain increase in the heat transfer coefficient. The overall heat transfer coefficient increased at varying flow rates (0.25kg/s, 0.5kg/s, and 1kg/s) at different speeds of rotation (100 RPM, 200 RPM, and 300 RPM). One of the most common equipment in industries is heat exchanger. Parameters like heat transfer coefficient can be increased by rotating tube(s) of heat exchanger. This was presented using two approaches- analytical and simulation techniques. On varying RPM from 0 to 300, heat transfer coefficient increased by 69.1% for 1 kg/s, 124.7% for 0.5 kg/s, and 172.3% for 0.25 kg/s.
通过换热器的管旋转提高整体传热系数:一种分析方法
经常观察到两个同心圆柱体或管道之间的环形空间中的流动,其应用范围广泛,包括蒸汽发生器、冷凝器、石油科学与工程以及化学加工行业中的各种流动装置。目的是证明或理解传热系数、传质系数等参数的本质,这些参数取决于这些流态。工业中发现的一种设备是热交换器,在热交换器中,热从一种介质传递到另一种介质。本研究主要讨论了在管壳式换热器中随着管的旋转而增加传热系数的问题,并且仅限于壳体内的单管。方法论部分大致可分为两类。首先,两个同心圆柱体之间流动的理论解(在某些假设下获得),包括旋转情况和无旋转情况。其次,ANSYS Fluent对这两种情况都进行了稳态模拟。在进入讨论之前或讨论过程中,已经明确提到了所有所需的条件、所选几何形状的尺寸和假设。此外,本研究是对管壳式换热器内管的传统操作和旋转方法的一种比较研究。从理论和ANSYS两种方法得到的结果都是积极的,即传热系数有一定的增加。总传热系数在不同流速(0.25kg/s、0.5kg/s和1kg/s)和不同转速(100RPM、200RPM和300RPM)下增加。工业中最常见的设备之一是热交换器。通过旋转换热器的管子可以增加传热系数等参数。这是使用两种方法提出的——分析和模拟技术。在从0到300的不同转速下,1 kg/s时传热系数增加了69.1%,0.5 kg/s时增加了124.7%,0.25 kg/s时提高了172.3%。
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 求助全文
来源期刊
Recent Innovations in Chemical Engineering
Recent Innovations in Chemical Engineering Chemical Engineering-Chemical Engineering (all)
CiteScore
2.10
自引率
0.00%
发文量
20
×
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
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
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 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术官方微信