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A study of heat transfer enhancement for electronic packaging.

机译:关于电子包装传热的研究。

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摘要

The fluid dynamic and heat transfer behavior of laminar non-Newtonian flow through non-circular ducts is of special interest because of their wide range of potential application in compact heat exchangers and in electronics cooling. The objectives of the present study were (1) to investigate the heat transfer characteristics for laminar forced convection of inelastic non-Newtonian fluids in a nonuniformly heated rectangular duct where the flow is hydrodynamically developed but thermally developing and (2) to investigate the influence of variable viscosity of temperature-dependent fluids on the laminar heat transfer and friction factors in a 2:1 rectangular duct. The governing equations were solved by a finite volume method. Second-order accurate differencing schemes were employed for both the diffusion and convective terms.;The effects of shear thinning, given by the Carreau equation, and the viscous dissipation, characterized by the Brinkman number, were examined via the friction factor, the Nusselt number, and the bulk fluid temperature. The results indicated that when viscous dissipation was present, the heat transfer from the heated surface of the duct was greatly enhanced with increased shear thinning of the fluid while the rate of increase of the bulk fluid temperature significantly decreased with axial distance. Consequently, the use of a shear-thinning non-Newtonian fluid for heat transfer enhancement appeared to be a very promising concept that is worthy of further study.;The present numerical results of local Nusselt numbers for oil (i.e., a temperature-dependent viscosity fluid) showed 70-80% enhancement over those of a constant property fluid and 40-50% enhancement over water, and gave excellent agreement with recent experimental results. The heat transfer enhancement from the heated top wall was due to an increased velocity gradient near the wall. A new correlation for local Nusselt numbers in the 2:1 rectangular duct was proposed which covered both thermally developing and thermally fully developed regions. Consequently, a temperature-dependent viscous fluid with a non-circular duct was proposed to be used in the design of a liquid cooling module for the computer industry.
机译:层流非牛顿流通过非圆形管道的流体动力学和传热特性因其在紧凑型换热器和电子冷却中的广泛应用而备受关注。本研究的目的是(1)研究非均匀加热的矩形管道中非弹性非牛顿流体的层流强迫对流的传热特性,该管道在流体动力作用下发展而在热力作用下发展;(2)研究流体的影响。在2:1矩形风管中,层流传热和摩擦系数上随温度变化的流体的可变粘度。控制方程通过有限体积法求解。对扩散项和对流项均采用了二阶精确差分方案。通过摩擦系数,努塞尔数检验了由Carreau方程给出的剪切稀化和以Brinkman数为特征的粘性耗散的影响。 ,以及散装流体的温度。结果表明,当存在粘性耗散时,管道受热面的传热随着流体剪切稀化的增加而大大增强,而整体流体温度的升高速率则随着轴向距离的增加而显着降低。因此,使用剪切稀化的非牛顿流体来增强传热似乎是一个非常有前途的概念,值得进一步研究。;油的局部Nusselt数值的当前数值结果(即与温度有关的粘度)流体)显示出比恒定性能的流体增强70-80%,并且比水增强40-50%,并且与最近的实验结果非常吻合。来自加热的顶壁的传热增强是由于壁附近的速度梯度增加。提出了在2:1矩形风管中局部Nusselt数的新相关性,该相关性涵盖了热发育区域和热充分发育区域。因此,提出了一种具有非圆形管道的随温度变化的粘性流体,用于设计用于计算机工业的液体冷却模块。

著录项

  • 作者

    Gingrich, William Kirk.;

  • 作者单位

    Drexel University.;

  • 授予单位 Drexel University.;
  • 学科 Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 1993
  • 页码 98 p.
  • 总页数 98
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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