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Hydrodynamics, heat transfer and flow boiling instabilities in microchannels

机译:微通道内的流体力学,传热和沸腾不稳定性

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摘要

Boiling in microchannels is a very efficient mode of heat transfer with high heat andudmass transfer coefficients achieved. Less pumping power is required for two-phaseudflows than for single-phase liquid flows to achieve a given heat removal.udApplications include electronics cooling such as cooling microchips in laptopudcomputers, and process intensification with compact evaporators and heatudexchangers.udEvaporation of the liquid meniscus is the main contributor to the high heat fluxesudachieved due to phase change at thin liquid films in a microchannel. The microscaleudhydrodynamic motion at the meniscus and the flow boiling heat transfer mechanismsudin microchannels are not fully understood and are very different from those inudmacroscale flows. Flow instability phenomena are noted as the bubble diameterudapproaches the channel diameter. These instabilities need to be well understood andudpredicted due to their adverse effects on the heat transfer.udA fundamental approach to the study of two-phase flow boiling in microchannels hasudbeen carried out. Simultaneous visualisation and hydrodynamic measurements wereudcarried out investigating flow boiling instabilities in microchannels using twouddifferent working fluids (n-Pentane and FC-72). Rectangular, borosilicateudmicrochannels of hydraulic diameter range 700-800 μm were used. The noveludheating method, via electrical resistance through a transparent, metallic deposit onudthe microchannel walls, has enabled simultaneous heating and visualisation to beudachieved. Images and video sequences have been recorded with both a high-speedudcamera and an IR camera.udBubble dynamics, bubble confinement and elongated bubble growth have beenudshown and correlated to the temporal pressure fluctuations. Both periodic and nonperiodicudinstabilities have been observed during flow boiling in the microchannel.udAnalysis of the IR images in conjunction with pressure drop readings, have allowedudthe correlation of the microchannel pressure drop to the wall temperature profile,udduring flow instabilities.udBubble size is an important parameter when understanding boiling characteristicsudand the dynamic bubble phenomena. In this thesis it has been demonstrated that theudflow passage geometry and microchannel confinement effects have a significantudimpact on boiling, bubble generation and bubble growth during flow boiling inudmicrochannels.
机译:微通道中的沸腾是一种非常有效的传热模式,具有很高的热量和传质系数。要实现给定的散热,两相流所需的泵送功率要比单相液流所需的泵送功率要少。ud的应用包括电子制冷,例如笔记本电脑,ud计算机中的微芯片冷却,以及紧凑型蒸发器和换热器的过程强化。液体弯月面的蒸发是导致高热通量的主要因素,这是由于微通道中液体薄膜的相变而导致的。弯月面的微尺度 udhydrodynamic运动和沸腾传热机理 udin微通道尚未完全了解,并且与那些在 udscale尺度上的流体有很大的不同。当气泡直径接近通道直径时,注意到流动不稳定现象。由于这些不稳定性会对传热产生不利影响,因此需要很好地理解和预测。 ud已经开始研究微通道中两相流沸腾的基本方法。同时使用两种不同的工作流体(正戊烷和FC-72)进行了可视化和流体力学测量,以研究微通道中的沸腾不稳定性。使用水力直径范围为700-800μm的矩形硼硅酸盐/微通道。通过在微通道壁上的透明金属沉积物的电阻,这种新颖的加热方法已实现了同时加热和可视化。图像和视频序列已用高速 udcamera和IR相机记录。 ud显示了气泡动力学,气泡限制和细长气泡增长,并与时间压力波动相关。在微通道内的沸腾过程中,观察到周期性和非周期性的不稳定性。 ud对红外图像与压降读数的结合分析,已经使微通道压降与壁温曲线之间具有相关性,导致了流体的不稳定性。 ud气泡大小是了解沸腾特性和动态气泡现象时的重要参数。在本文中,已经证明了溢流通道的几何形状和微通道限制效应对溢流在微通道中的沸腾,气泡的产生和气泡的生长具有显着的影响。

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  • 作者

    Barber Jacqueline Claire;

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  • 年度 2010
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  • 原文格式 PDF
  • 正文语种 {"code":"en","name":"English","id":9}
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