Flow Boiling in Silicon Microchannel Heat Sinks

T. Harirchian, S. Garimella
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引用次数: 7

Abstract

The local flow boiling heat transfer and pressure drop in microchannel heat sinks are investigated with a dielectric fluid, Fluorinert FC-77. The effect of channel size on flow boiling is studied for mass fluxes ranging from 250 to 1600 kg/m2s for seven different test pieces consisting of parallel microchannels with nominal widths ranging from 100 to 5850 mum, all with a depth of 400 mum. High-speed visualizations are performed simultaneously with the local measurements of the temperature and pressure drop to investigate the flow boiling patterns and the conditions for transition between different regimes. The results of this study show that for microchannels of width 400 mum and greater, the heat transfer coefficients corresponding to a fixed wall heat flux as well as the boiling curves are independent of channel size, and have a weak dependence on channel width for smaller microchannels. This is consistent with the visualizations which show that flow regimes in microchannels of width 400 mum and larger are similar, while those in the 100 mum wide microchannels are distinctly different. Also, unlike the 100 mum wide microchannels, in which bubble nucleation at the walls is suppressed at a relatively low heat flux, nucleate boiling is dominant over a wide range of heat fluxes for microchannels of width 400 mum and larger.
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硅微通道散热器中的流动沸腾
用氟化FC-77介质研究了微通道散热器的局部流动沸腾换热和压降。在质量通量为250 ~ 1600 kg/m2s的条件下,研究了通道尺寸对流动沸腾的影响,七个不同的试件由平行微通道组成,公称宽度为100 ~ 5850 μ m,深度均为400 μ m。高速可视化与局部温度和压降测量同时进行,以研究流动沸腾模式和不同状态之间转换的条件。研究结果表明,对于宽度为400 μ m及以上的微通道,固定壁面热流密度对应的换热系数和沸腾曲线与通道尺寸无关,对于较小的微通道,与通道宽度的相关性较弱。这与可视化结果一致,显示宽度为400 μ m及更大的微通道内的流动形式相似,而宽度为100 μ m的微通道内的流动形式明显不同。此外,与100 μ m宽的微通道不同,在相对较低的热流密度下,气泡在壁上的成核受到抑制,而在400 μ m及更宽的微通道中,成核沸腾在很宽的热流密度范围内占主导地位。
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