矩形微通道内强制对流换热的实验与数值研究

D. Kamble, B. Gawali
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引用次数: 2

摘要

对五组矩形微通道中水的换热特性进行了实验和数值分析。对雷诺数为2.1 ~ 48时液压微通道直径分别为222 μm、267 μm、323 μm、330 μm和343 μm的微通道进行了分析。在输入热量为10 W ~ 100 W、进口流体温度为29℃、质量流量为0.0167 kg/sec ~ 0.116 kg/sec的条件下进行了数值分析和实验。随着雷诺数的增加,努塞尔数呈线性增加的趋势。此外,流动微通道入口和出口之间的区域存在较高的温度梯度。当水力直径为222 μm时,换热系数高于其他水力直径配置。数值计算结果与实验结果吻合较好,误差在4-5%之间。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Experimental and Numerical Investigation of Forced Convection Heat Transfer in Rectangular Microchannels
Experimental and numerical analysis were performed to evaluate heat transfer characteristics of water through five sets of rectangular microchannels. Microchannels of hydraulic diameter of 222 μm, 267 μm, 323 μm, 330 μm and 343 μm respectively for Re number between 2.1 to 48 were analysed. Numerical analysis and experiments were conducted under a input heat of 10 W to 100 W, inlet fluid temperature 29°C and mass flow rates of 0.0167 kg/sec to 0.116 kg/sec. Nusselt number tends to be linear increasing as Reynolds number increases. Besides high temperature gradient exist in the region between inlet and exit of flow microchannel. For hydraulic diameter 222 μm, heat transfer coefficient seems to be higher as compare to other configurations of hydraulic diameters. Numerical results showed reasonably good agreement within 4-5% with experimental results.
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