CFD Analysis of Various Design Aspects in Baffle Tube Heat Exchanger

A. Mishra, P. S. Daniel, Prof. Amit Kumar Asthana
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Abstract

To improve temperature difference, a computer simulation assessment for a rectangular duct with right angle confounds heat exchanger with small displacements and bewilder height was carried out. A total of 10 There were three separate two half Autocad models of rectangular shaped channel with bewilders spacing of 40 milimetre, 80 milimetre, and 120 milimetre and baffle heights of 10 mm, 12.5 milimetre, and 15 milimetre developed. The major goal of this study is to run computer simulations to see how Cu water nanoparticle affect the architecture and thermally hydrodynamic characteristics of a rectangular duct with baffles exchanger. The bottom walls of the canal, as well as the baffles, are regarded isothermal zones, whereas the sidewalls are termed regular zones. This approach employs a second derivative upwind mass and energy equation. The baffle pitch and height have a significant influence on the temperature distribution from the rectangle shaped channel  heating element, with a maximal temperature fluctuations of 9.831oC and a maximum heat transfer of 6.571 KW for baffle spacing 40 mm and height 15 mm for rectangle channel without opposite baffles. In comparison to the base design of rectangle shaped channels exchanger, the temperature difference increases nearly 1.5 times as even the width is decreased.
折流管换热器设计各方面的CFD分析
为了改善温差,对矩形直角小排量、导通高度的混流换热器进行了计算机模拟计算。共10个。有三个独立的两个半矩形通道的Autocad模型,挡板间距分别为40毫米、80毫米和120毫米,挡板高度分别为10毫米、12.5毫米和15毫米。本研究的主要目的是通过计算机模拟来观察铜水纳米粒子如何影响带折流板换热器矩形管道的结构和热流体动力特性。运河的底壁,以及挡板,被认为是等温区,而侧壁被称为规则区。这种方法采用了一种二阶导数迎风质量和能量方程。当挡板间距为40 mm,挡板高度为15 mm时,矩形通道的最大温度波动为9.831oC,最大换热量为6.571 KW。与矩形通道换热器的基础设计相比,即使宽度减小,温差也增加了近1.5倍。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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