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Heat transfer enhancement through periodic flow area variations in microchannels

机译:通过微通道中的周期性流动面积变化来增强传热

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In this study, annular microchannels with a microscale gap of 300 μm were implemented through the concentric superposition of two macro-sized cylinders. Flow area variations along the streamwise direction were created by introducing sinusoidal wave profiles on either the inner or outer wall of the annular gap while keeping the other wall flat. These variations introduced re-entrant effects along the flow direction. Numerical studies using the finite volume method were performed to elucidate the single-phase, steady-state thermal and hydrodynamic performances of the wavy channels, using water as the fluid medium, with an operating Reynolds number range of 800-2200. The predicted results were validated using the available measured data and classical correlations. This study demonstrated the viability of attaining enhanced heat transfer rates of up to 360% of the original straight channel through the inducement of flow area variations with single wavy-walled channels. Despite magnifications of the friction factors, the single wavy-walled channels attained a 120% increment in heat transfer coefficient when evaluated at the same pumping power. Overall, single-walled wavy passages were deemed suitable for heat exchanger designs demanding very high heat removal rates and efficiencies while the conventional serpentine channels were apt for moderately enhancing heat transfer while requiring low pumping power.
机译:在这项研究中,通过两个大尺寸圆柱体的同心叠加实现了具有300μm微米级间隙的环形微通道。通过在环形间隙的内壁或外壁上引入正弦波波形,同时保持另一壁平坦,可以沿流向产生流动面积变化。这些变化沿流动方向引入了折返效应。使用有限体积方法进行了数值研究,以阐明使用水作为流体介质,工作雷诺数范围为800-2200的波浪通道的单相,稳态热和流体力学性能。使用可用的测量数据和经典相关性验证了预测结果。这项研究表明,通过诱导单个波浪壁通道的流动面积变化,可以获得高达原始直通道360%的增强传热率的可行性。尽管摩擦系数得到了放大,但在相同的泵浦功率下进行评估时,单个波状通道的传热系数却增加了120%。总的来说,单壁波浪通道被认为适合于要求很高的除热率和效率的换热器设计,而常规的蛇形通道易于适度地增强传热而又需要低的泵送功率。

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