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Experimental Investigation on Thermo-Hydraulic Performance of Heat Exchanger Tube with Solid and Perforated Circular Disk Along with Twisted Tape Insert

机译:实心多孔圆盘与扭曲带插入物的换热器管的热工水力实验研究

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摘要

Heat transfer enhancement in heat exchanger by using passive approach has become a very versatile area of research for the researchers. Although very significant results has been achieved in the thermal performance of heat exchangers, especially in the range of lower Reynolds number, but still these passive approaches of heat transfer enhancement is not effective for the range of higher Reynolds number. In the present work the effect of 'perforated circular disk turbulators with and without twisted tape', on heat transfer, friction factor and thermal performance of heat exchanger is evaluated experimentally. The different geometrical parameters used for the experiment include fixed diameter ratio (0. 8), pitch ratios (1, 2, and 3), perforation index (0%, 8%, 16%, and 24%), fixed twist ratio (2) and fixed width ratio (0.4). The experiment is done in the range of Reynolds number lying from 6,500 to 26,500. On the basis of experimental observation, there is 2.2-3.54 times improvement in heat transfer and around 1.18-1.64 times improvement in thermal performance factor over smooth tube heat exchanger.
机译:通过使用被动方法增强热交换器中的传热,已成为研究人员非常广泛的研究领域。尽管已在热交换器的热性能方面取得了非常显着的结果,尤其是在较低的雷诺数范围内,但是这些被动的传热增强方法对于较高的雷诺数范围仍然无效。在本工作中,实验评估了“带或不带扭曲带的多孔圆盘湍流器”对换热器的传热,摩擦系数和热性能的影响。用于实验的不同几何参数包括固定直径比(0. 8),螺距比(1、2和3),穿孔指数(0%,8%,16%和24%),固定扭曲比( 2)和固定宽度比(0.4)。实验在雷诺数范围从6,500到26,500的范围内完成。根据实验观察,与光滑管式换热器相比,传热提高了2.2-3.54倍,热性能系数提高了约1.18-1.64倍。

著录项

  • 来源
    《Heat Transfer Engineering》 |2019年第8期|616-626|共11页
  • 作者单位

    Uttarakhand Tech Univ, Tulas Inst, Mech Engn Dept, Dehra Dun, India;

    Uttarakhand Tech Univ, BTKIT Dwarahat, Dept Mech Engn, Dehra Dun, India;

    DIT Univ, Dept Mech Engn, Dehra Dun, India;

    DIT Univ, Dept Mech Engn, Dehra Dun, India;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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