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Experimental and numerical study on convective boiling in a staggered array of micro pin-fin microgap

机译:微型针翅微间隙交错阵列中对流沸腾的实验和数值研究

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摘要

The flow patterns, heat transfer and pressure drop of convective boiling of dielectric fluid, FC-72, in a micro-gap are investigated experimentally. The surface of the microgap is enhanced with a staggered array of micro pin-fins. The enhanced surface of the microgap with the size of 10 × 10 mm~2 is subject to an electrical heat source. The micro-pin-fins are etched as cubic columns of 100 μm size and arranged in a staggered arrangement with 400 μm pitch in both transverse and longitudinal directions. The inside of the micro pin-fins is nucleated with a cavity of cylindrical shape with diameter of 60 μm and an opening with a size of either 15 μm or 45 μm width. The opening of the cavities of the micro-pin-fins is aligned toward the down-stream. For the case of single-phase flow, a numerical analysis is performed, and the pressure drop and velocity fields are investigated in the micro-gap. The experiments were performed for various mass fluxes ranging from 94 to 275 kg/m~2s and heat flux ranging from 0 to 10 W/cm~2, and at two saturation temperatures of 35 and 50 ℃. For the case of single-phase heat transfer, the experimental results are compared with the pin-fins having 45 μm cavity opening and found that the effect of cavity opening is significant when the mass flux is high. The surface-superheat at the onset of boiling is reduced by reducing the cavity opening-width from 45 to 15 μm. The microgap having nucleation cavity with cavity opening-width of 15 μm results in a 3.44 ℃ smaller surface-superheat than that of 45 μm opening-width. The convective heat transfer coefficient increases with the increase of mass flux, regardless of the flow type. Moreover, the variation of the pin-fin opening-widths does not influence the convection heat transfer rate. For single-phase flow, the heat flux shows a negligible effect on pressure drop, and the pressure drop increases with increasing mass flux. For two-phase flow, the pressure drop increases drastically with increasing heat flux. A smaller cavity opening-width results in a smaller pressure drop when the mass flux is high. The flow observation shows two distinct flow patterns in the microgap at the beginning of the bubble nucleation.
机译:实验研究了微间隙中FC-72介质对流沸腾的流动方式,传热和压降。微间隙的表面通过微细针状鳍片的交错阵列得到增强。尺寸为10×10 mm〜2的微间隙增强表面受到电热源的影响。将微针状鳍片蚀刻为100μm大小的立方柱,并在横向和纵向上以400μm的间距交错排列。微型针状翅片的内部成核为直径为60μm的圆柱形空腔和宽度为15μm或45μm的开口。微针状鳍片的空腔的开口朝向下游对齐。对于单相流,进行了数值分析,并在微间隙中研究了压降和速度场。分别在94和275 kg / m〜2s的各种质量通量和0〜10 W / cm〜2的热通量以及35和50℃的两个饱和温度下进行了实验。对于单相传热的情况,将实验结果与具有45μm空腔开口的针状翅片进行了比较,发现当质量通量较高时,空腔开口的效果显着。通过将腔的开口宽度从45μm减小到15μm,可以减少沸腾开始时的表面过热。具有成核腔的微间隙的开孔宽度为15μm,比起45μm的开孔产生的表面过热小3.44℃。对流传热系数随质量通量的增加而增加,与流动类型无关。而且,针翅开口宽度的变化不影响对流传热速率。对于单相流,热通量对压降的影响可忽略不计,并且压降随着质量通量的增加而增加。对于两相流,压降随着热通量的增加而急剧增加。当质量通量较高时,较小的腔体开口宽度会导致较小的压降。流动观察显示,在气泡成核开始时,微间隙中有两个不同的流动模式。

著录项

  • 来源
    《International Journal of Heat and Mass Transfer》 |2020年第3期|119203.1-119203.16|共16页
  • 作者

  • 作者单位

    Department of Energy and Refrigerating Air-Conditioning Engineering National Taipei University of Technology Taipei 10608 Taiwan Research Center of Energy Conservation for New Generation of Residential Commercial and Industrial Sectors National Taipei University of Technology Taipei 10608 Taiwan;

    Department for Management of Science and Technology Development Ton Duc Thang University Ho Chi Minh City Vietnam Faculty of Applied Sciences Ton Duc Thang University Ho Chi Minh City Vietnam;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Micro-pin-fin; Staggered array; Microgap; FC-72; Columnar nucleation pin-fin; Nucleate boiling heat transfer;

    机译:微针鳍;交错阵列;微间隙FC-72;柱状成核针翅;核沸腾传热;

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