CFD Modeling Of Turbulence in Channels Of Plate Heat Exchangers

D. Mandić
{"title":"CFD Modeling Of Turbulence in Channels Of Plate Heat Exchangers","authors":"D. Mandić","doi":"10.11159/ffhmt18.103","DOIUrl":null,"url":null,"abstract":"The subject of this paper is turbulence modeling of fluid flow in channels of plate heat exchangers for heating domestic hot water in heating substation in Belgrade. For testing of turbulence phenomena in the channels, this paper uses the standard K-ε model of turbulence. It is of particular importance that in this paper the modeling is made for different flow rates of fluids through channels, adopted in boundary conditions. The rate of flow in the input area of the channels was taken as the assumed average values of 0.01m / sec, and 0.1m / sec, which presupposed minimum and maximum values based on the measured values of these fluid velocities in the heat substations. On the basis of these assumed speeds, the values of the exchanged kinetic energy and the character of the change in the intensity of the projections of these velocities in the direction of all three axes are obtained. On the basis of these projections, we can determine the unsteadiness of the velocity and the return currents along these channels and in their contour surfaces as well as the \"dead spots\" in which there is no movement of the fluid. This work presents the calculated values of the Reynolds number of the streamline for the assumption velocity of fluid in channels. These phenomena can cause different problems in the transmission of heat and dirt in the channels of the plate heat exchangers where there is no circulation. Therefore, the obtained results can serve as a basis for dimensioning and selection of heat exchangers as well as for determining their optimal working conditions.","PeriodicalId":92806,"journal":{"name":"Journal of fluid flow, heat and mass transfer","volume":"86 1","pages":""},"PeriodicalIF":0.0000,"publicationDate":"2018-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of fluid flow, heat and mass transfer","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.11159/ffhmt18.103","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0

Abstract

The subject of this paper is turbulence modeling of fluid flow in channels of plate heat exchangers for heating domestic hot water in heating substation in Belgrade. For testing of turbulence phenomena in the channels, this paper uses the standard K-ε model of turbulence. It is of particular importance that in this paper the modeling is made for different flow rates of fluids through channels, adopted in boundary conditions. The rate of flow in the input area of the channels was taken as the assumed average values of 0.01m / sec, and 0.1m / sec, which presupposed minimum and maximum values based on the measured values of these fluid velocities in the heat substations. On the basis of these assumed speeds, the values of the exchanged kinetic energy and the character of the change in the intensity of the projections of these velocities in the direction of all three axes are obtained. On the basis of these projections, we can determine the unsteadiness of the velocity and the return currents along these channels and in their contour surfaces as well as the "dead spots" in which there is no movement of the fluid. This work presents the calculated values of the Reynolds number of the streamline for the assumption velocity of fluid in channels. These phenomena can cause different problems in the transmission of heat and dirt in the channels of the plate heat exchangers where there is no circulation. Therefore, the obtained results can serve as a basis for dimensioning and selection of heat exchangers as well as for determining their optimal working conditions.
板式换热器流道湍流的CFD模拟
本文的主题是贝尔格莱德供热站板式换热器加热生活热水通道内流体流动的湍流模拟。为了测试通道内的湍流现象,本文采用了标准的K-ε湍流模型。特别重要的是,本文对边界条件下流体通过通道的不同流速进行了建模。通道输入区的流速分别为0.01m / sec和0.1m / sec的假设平均值,并根据换热站中流体流速的实测值分别假设了最小值和最大值。在这些假设速度的基础上,得到了交换动能的值和这些速度在所有三个轴的方向上的投影强度变化的特征。在这些投影的基础上,我们可以确定沿着这些通道及其轮廓面的速度和回流的不稳定性,以及没有流体运动的“死点”。本文给出了流线雷诺数的计算值,用于假设流线中流体的流速。这些现象会在没有循环的板式换热器的通道中产生不同的传热和污垢问题。因此,所得结果可作为换热器尺寸和选型以及确定其最佳工作条件的依据。
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
CiteScore
0.90
自引率
0.00%
发文量
0
×
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:604180095
Book学术官方微信