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Investigation of fluid flow and heat transfer characteristics of parallel flow double-layer microchannel heat exchanger

机译:平行流动双层微通道热交换器流体流动和传热特性研究

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摘要

The fluid flow and heat transfer characteristics in parallel flow double-layer microchannel heat exchanger are investigated both numerically and experimentally. The effect of microchannel height, width and spacing on fluid flow and heat transfer performance is comprehensively studied. The numerical results are firstly validated by comparing the Nusselt number, pressure loss and friction factor with the experimental data. Subsequently, the velocity and temperature profiles from simulation results are obtained to study the fluid flow and heat transfer characteristics. The results show that the increasing height and width have an appreciable contribution to the velocity profile. The dimensionless hydrodynamic entrance length does not depend on microchannel size. Moreover, average Nusselt number increases with increasing width and decreasing height for simultaneously thermally and hydrodynamically developing flow. The friction factor is found to decrease slightly with increasing spacing and decreasing height and width. Taking the average Nusselt number, friction factor and the thermal performance index as an evaluation criterion, the heat exchanger with microchannels of 1-1.5 mm in height, 0.4-0.6 mm in width and 0.6-0.8 mm in spacing shows better heat exchange performance.
机译:在数值和实验上研究了平行流动双层微通道热交换器中的流体流动和传热特性。综合研究了微通道高度,宽度和间隔对流体流动和传热性能的影响。首先通过比较具有实验数据的泡沫数,压力损失和摩擦因子来验证数值结果。随后,获得了模拟结果的速度和温度分布,以研究流体流动和传热特性。结果表明,增加的高度和宽度对速度曲线具有明显的贡献。无量纲的流体动力学入口长度不依赖于微通道尺寸。此外,同时热和流体动力学显影的宽度和高度的宽度增加和高度的平均冲击数增加。发现摩擦系数随着间距和降低的高度和宽度而略微减小。以平均水果数量,摩擦因子和热性能指数作为评估标准,高度为1-1.5毫米的微通道,宽度为0.4-0.6毫米,间距为0.6-0.8毫米显示出更好的热交换性能。

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