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Pressure drop characteristics of large length-to-diameter two-phase micro-channel heat sinks

机译:大口径两相微通道散热器的压降特性

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摘要

Unlike prior published two-phase micro-channel studies that concern mostly miniature heat sinks, the present study addresses transport characteristics of a heat sink containing large length-to-diameter micro-channels. The copper heat sink has a 609.6-mm long by 203.2-mm wide base area, and contains 100 parallel micro-channels having a 1×1 mm~2 cross-section, and a length-to-diameter ratio of 609.6 to 1. The study addresses pressure drop characteristics of R134a for subcooled inlet conditions with inlet pressures of 689.4-731.3 kPa, mass velocities of 75.92-208.79 kg/m~2 s, and base heat fluxes of 4036-28,255 W/m~2. The data are compared to predictions of the Homogeneous Equilibrium Model (HEM) in conjunction with six different two-phase mixture viscosity relations, correlations based on the Separated Flow Model (SFM) and intended for macro-channels, and correlations based on SFM and intended for micro-channels. Overall, fairly good predictions are achieved with HEM, compared to poor predictions with the macro-channel SFM correlations. The micro-channel SFM correlations fared better, yielding mean absolute error values as low as 6.66%. Flow visualization results show appreciable periodic fluctuations in two-phase flow patterns, which include four primary patterns: bubblyjslug, slug, transition, and annular, along with two other patterns associated specifically with downstream dryout: transition and annular. These observations point to the need for more research to address the role of flow instabilities and fluctuations in flow pattern development.
机译:与先前发布的主要涉及微型散热器的两阶段微通道研究不同,本研究针对的是包含大直径直径微通道的散热器的传输特性。铜散热器的底面积为609.6毫米(长)乘以203.2毫米(宽),并包含100个平行微通道,这些微通道的横截面为1×1 mm〜2,长径比为609.6:1。研究针对过冷进气条件下R134a的压降特性,进气压力为689.4-731.3 kPa,质量速度为75.92-208.79 kg / m〜2 s,基础热通量为4036-28,255 W / m〜2。将数据与均相平衡模型(HEM)的预测,六种不同的两相混合物粘度关系,基于分离流模型(SFM)的相关性和用于宏通道的相关性以及基于SFM和预期的相关性进行了比较用于微渠道。总体而言,与宏信道SFM相关性较差的预测相比,HEM可以实现相当好的预测。微通道SFM相关性更好,产生的平均绝对误差值低至6.66%。流量可视化结果显示出两相流模式中明显的周期性波动,其中包括四个主要模式:气泡状,段塞状,过渡型和环形,以及另外两个与下游干燥有关的模式:过渡型和环形。这些观察结果表明,需要进行更多的研究来解决流动不稳定性和波动在流动模式发展中的作用。

著录项

  • 来源
    《International Journal of Heat and Mass Transfer》 |2017年第ptab期|1258-1275|共18页
  • 作者单位

    Purdue University Boiling and Two-Phase Flow Laboratory (PU-BTPFL), Mechanical Engineering Building, 585 Purdue Mall, West Lafayette, IN 47907, USA;

    Purdue University Boiling and Two-Phase Flow Laboratory (PU-BTPFL), Mechanical Engineering Building, 585 Purdue Mall, West Lafayette, IN 47907, USA;

    Purdue University Boiling and Two-Phase Flow Laboratory (PU-BTPFL), Mechanical Engineering Building, 585 Purdue Mall, West Lafayette, IN 47907, USA;

  • 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-channel; Heat sink; Flow boiling; Pressure drop; Flow patterns; Flow oscillations;

    机译:微信;散热器;流沸腾;压力下降;流型;流动振荡;
  • 入库时间 2022-08-18 00:18:05

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