Thermo-fluid performance of axially perforated multiple rectangular flow deflector-type baffle plate in an tubular heat exchanger

IF 2.2 Q2 ENGINEERING, MULTIDISCIPLINARY
Md Atiqur Rahman
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Abstract

The study investigated an unconventional heat exchanger design that utilizes swirling airflow to enhance heat transfer over heated tubes. This innovative system incorporates a perforated round baffle plate, accompanied by multiple rectangular air deflectors oriented in opposite directions at varying inclination angles. These deflectors are symmetrically arranged at different pitch ratios alongside consistently spaced tubes forming a circular configuration, all subject to a uniform heat flux. Enclosed within a circular duct with longitudinal airflow, the combined baffle plate and tube assembly bring forth efficient heat transfer. The air-side turbulence intensified by the deflectors induces a chaotic motion, contributing to enhanced surface heat transfer. Each baffle plate has twelve opposite-oriented deflectors, resulting in opposing swirl flows that further promote flow recirculation and augment surface heat transfer. The performance of this heat exchanger was evaluated by considering different pitch ratios and inclination angles across a Reynolds number range of 16000-30000. The findings demonstrate that the heat exchanger with rectangular flow deflectors on the baffle plate exhibits significant improvements in thermo-fluid performance. Notably, an average enhancement of 1.88 was observed at an inclination angle of 50 degrees and a pitch ratio of 1.2 when compared to an exchanger without baffle plates, emphasizing the considerable impact of these design aspects.
管式热交换器中轴向穿孔多矩形导流板式挡板的热流体性能
该研究调查了一种非常规的热交换器设计,它利用漩涡气流来增强加热管的热传递。这种创新系统包括一个穿孔圆形挡板,以及多个矩形空气导流板,这些导流板以不同的倾斜角度朝相反的方向排列。这些导流板以不同的间距比对称地排列在间距一致的管子旁边,形成一个圆形结构,所有管子都受到均匀的热通量影响。在纵向气流的圆形管道内,挡板和管子的组合实现了高效的热传递。导流板加强了空气侧的湍流,诱发了混沌运动,从而增强了表面传热。每块折流板上都有十二个方向相反的导流板,从而形成相反的漩涡流,进一步促进流体再循环,增强表面传热。在 16000-30000 雷诺数范围内,通过考虑不同的间距比和倾角,对该热交换器的性能进行了评估。研究结果表明,在挡板上安装矩形导流板的热交换器在热流体性能方面有显著改善。值得注意的是,与不带折流板的热交换器相比,在倾角为 50 度、间距比为 1.2 时,平均提高了 1.88,这强调了这些设计方面的重大影响。
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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来源期刊
Applications in engineering science
Applications in engineering science Mechanical Engineering
CiteScore
3.60
自引率
0.00%
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0
审稿时长
68 days
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