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首页> 外文期刊>International communications in heat and mass transfer >Experimental study of boiling heat transfer in a microchannel with nucleated-shape columnar micro-pin-fins
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Experimental study of boiling heat transfer in a microchannel with nucleated-shape columnar micro-pin-fins

机译:带核形柱状微针鳍微通道中沸腾传热的实验研究

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The boiling regime and flow field patters of boiling heat transfer of FC-72 dielectric fluid in a microchannel are experimentally studied. The inner surface of the test section of the microchannel is covered with nucleated columnar fins of height 100 mu m. Each fin is nucleated with the core diameter of 60 mu m and opening of 45 mu m, which the fin openings is aligned opposite to the flow direction. The experiments are performed for two saturation temperatures of T-sat = 35 degrees C and T-sat = 50 degrees C. The heat flux and mass velocity are in the range of 0.67-4.5 W/cm(2), and 94-138 kg/m(2) s, respectively. The results are reported for the on boiling temperature difference and pressure drop. The flow-field behavior of formation of bubbles at the nucleated fins, single-pore nucleation, and boiling flow regime are addressed. The results reveal that the increase in the mass velocity increases the subcooled temperature difference. The flow-behavior images in the test-section show that cell flow, block flow, droplet/block flow, droplet flow, and annular flow patterns can be formed by the increase of the surface heat flux. The on boiling phase change induces about three-fold of pressure-drop in the microchannel, Besides, the rise of the working fluid saturation temperature raises the pressure-drop.
机译:实验研究了FC-72介质在微通道中沸腾传热的沸腾形式和流场模式。微通道测试部分的内表面覆盖有高度为100μm的有核柱状鳍。每个鳍成核,其核心直径为60μm,开口为45μm,这些鳍的开口与流向相反。在T-sat = 35摄氏度和T-sat = 50摄氏度的两个饱和温度下进行实验。热通量和质量速度在0.67-4.5 W / cm(2)和94-138的范围内kg / m(2)s。报告了沸腾温度差和压降的结果。解决了在有核鳍片处气泡形成,单孔成核和沸腾流态的流场行为。结果表明,质量速度的增加增加了过冷的温度差。测试区域中的流动行为图像显示,可以通过增加表面热通量来形成单元流动,块流动,液滴/块流动,液滴流动和环形流动模式。沸腾相变在微通道中引起大约三倍的压降,此外,工作流体饱和温度的升高也增加了压降。

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