折流板间距对管壳式换热器中水的动态和热行为的影响

IF 1 Q4 MATERIALS SCIENCE, COMPOSITES
A. Youcef, R. Saim
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引用次数: 1

摘要

对雷诺数为2432733562569的三个装有6、8、10节段挡板的管壳式换热器中的湍流进行了数值模拟。基于SIMPLE速度-压力耦合算法,采用有限体积法求解质量、动量和能量守恒方程,并在不同情况下使用Fluent软件中的数学模型k-ε。研究了三个挡板间距下的温度、速度、摩擦系数、传热系数、壳体压降、管与流体之间的总传热率、整体性能系数。这项工作在很大程度上有助于理解湍流,也显示了挡板数量对换热器传热的影响。壳体中的流速分别比参考速度增加了1.49%、1.62%和1.73%。结果表明,由于挡板数量的增加,出口温度、传热系数分别增加了1.09%和1.28%,压降分别增加了1.7%和2.82%,总传热率分别增加了1.0%和1.18%。本研究中获得的结果与文献中给出的结果一致。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effect of Spacing Between Baffles on the Dynamic and Thermal Behavior of Water in a Shell-and-Tube Heat Exchanger
A numerical simulation of a turbulent flow of water in three shell and tube heat exchangers equipped with 6, 8, 10 segmental baffles as the working fluid at Reynolds numbers ranging from 24327, 33356, 42569 are performed. The conservation equations of mass, momentum and energy are solved by the finite volume method based on the SIMPLE algorithm for coupling velocity-pressure, the mathematical model k-ε within the Fluent software is used in the different cases presented. The temperature, the velocity, the friction factor, the heat transfer coefficient, the pressure drop in the shell, the total heat transfer rate between the tubes and the fluid, the overall performance factor are studied for the three spacing between baffles. This work contributes largely to the understanding of turbulent flows and also shows the effect of the baffles number on the heat transfer in the heat exchangers. The velocity of flow in the shell increases by 1.49% and 1.62% and 1.73% of the reference velocity. The results show an increase in the outlet temperature, heat transfer coefficient 1.09% and 1.28%, pressure drop 1.7% and 2.82%, the total heat transfer rate 1.08% and 1.18% because of the increase in number of baffles. The results obtained in this study are in good agreement and correspond to the results given by the literature.
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来源期刊
CiteScore
1.90
自引率
25.00%
发文量
32
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