不同相移正弦波型微通道散热器的传热与流动特性

Abdul Aziz Shuvo, Md. Omarsany Bappy, Amitav Tikadar, T. C. Paul, A. Morshed
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摘要

微通道散热片(MCHS)在去除微电子器件的大热流通量方面具有广阔的应用前景。而在直线微通道中,速度边界层和热边界层是连续增长的。因此,微通道的性能下降。破坏边界层的形成可以提高MCHS的性能。实现这一目标的一种方法是开发波浪通道而不是直线微通道(s-MCHS),后者由于其波浪性而阻碍了边界层的持续增长。大量研究表明,波幅的增加和波长的减少增强了混沌平流和更好的冷却剂混合。从而增加了MCHS内的换热和压降。虽然波浪型MCHS的波长和波幅(w-MCHS)对传热性能有显著影响,但两波壁之间的相移(θp)也会影响MCHS的流动和传热特性。当上下正弦壁处于不同相位时,MCHS的横截面积会发生变化。因此,横截流面积的变化在MCHS中产生了逆压梯度。这导致更多的流动逆转和更好的冷却剂混合,从而改善热性能。本研究旨在研究层流条件下w-MCHS在θp = 0, π/2, π三种不同相移情况下的流动和换热特性。在研究中,Re在300到800之间。有相移的w-MCHS, θp = π/2, π总是比s-MCHS和有相移的w-MCHS表现出更高的努塞尔数(Nu), θp = 0。波浪形MCHS中θp = π/2和θp = π相移引起的表面积增加可以忽略不计,相移w-MCHS的传热增强是由边界层的中断、重新初始化和重新附着引起的。在目前的数值研究中,Nu随着相移而增加,在相移时Nu比s-MCHS高7倍,θp = π,波长(λ) = 3.5 mm。除了换热效果好、冷却剂混合效果好外,相移引起的剪切应力和压降增大,主要是由于混沌流动造成的。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Heat Transfer and Flow Characteristic of Sinusoidal Wavy Microchannel Heat Sink With Different Phase Shift
Microchannel heat sinks (MCHS) are promisingly utilized to remove large heat flux from microelectronic devices. However, the velocity and thermal boundary layers grow continually in a straight microchannel. As a result, the performance of the microchannel degrades. Disrupting the formation of the boundary layer can enhance the performance of MCHS. One approach to achieve that goal is to develop a wavy channel rather than a straight microchannel (s-MCHS) which hinders the continual growth of boundary layers due to its waviness. Numerous researches suggested that wave amplitude increment and wavelength decrement enhanced the chaotic advection and better coolant mixing. Thus, heat transfer and pressure drop were increased in the MCHS. Although wavelength and wave amplitude in a wavy MCHS (w-MCHS) significantly impact heat transfer performance, the phase shift (θp) between two wavy walls in an MCHS also affects the flow and heat transfer characteristics. When the upper and lower sinusoidal walls are in different phases, the cross-sectional area of the MCHS varies. So, the cross-sectional flow area variation creates an adverse pressure gradient in the MCHS. which causes more flow reversal and better coolant mixing, resulting in improved thermal performance. The current study aims to study the flow and heat transfer characteristics in w-MCHS for three different phase shifts, θp = 0, π/2, π, under laminar flow conditions. Re ranges from 300 to 800 in the study. w-MCHS with phase shift, θp = π/2, π always shows higher Nusselt number (Nu) than s-MCHS and w-MCHS with phase shift, θp = 0. An increase in surface area due to phase shifts, θp = π/2 and θp = π in wavy MCHS, is negligible and the enhancement in heat transfer of phase-shifted w-MCHS is caused by interruption, reinitialization, and reattachment of boundary layers. In the current numerical study, Nu was found to increase with the phase shift and found 7 times higher than s-MCHS at phase shift, θp = π for wavelength (λ) = 3.5 mm. Besides higher heat transfer and better coolant mixing, the phase shift in wavy MCHS causes increased shear stress and pressure drop due to chaotic flow in wavy MCHS.
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