Numerical Investigation of the Mixing Efficiency in Square-Wave Passive Micromixers for Microfluidic Device Applications

V. Ionescu
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Abstract

This numerical study investigated the mixing efficiency and pressure drop characteristics of water-based liquid flow through five different serpentine-type microchannel structures with a square cross-section, for Reynolds numbers Re between 0.5 and 40. The cost of mixing was also evaluated here in terms of pressure drop and input power required to transport the fluid through the channel. The passive micromixer models were characterized by a constant hydraulic diameter of 200 μm, with the height H and pitch Pi of the microchannel modified at the values from 0.6 to 1 mm and 1.2 to 2 mm, respectively, maintaining a constant Pi/H ratio of 2. At Re = 2, Re = 10 and Re =30, the mixing efficiency for the model with Pi = 2 mm and H = 1 mm was 1.27, 1.1 and 1.26 times the mixing indexes of the model with Pi = 1.2 mm and H = 0.6 mm, respectively. This enhanced mixing quality was obtained with the sacrifice of a lower mixing index to pressure drop ratio (1.18, 1.32 and 1.13 times lower) and a higher mixing cost in terms of input power (1.18, 1.49 and 1.15 times higher).
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用于微流控器件的方波无源微混合器混合效率的数值研究
本文研究了在雷诺数Re为0.5 ~ 40的条件下,水基液体通过5种不同的方形截面蛇纹石微通道结构时的混合效率和压降特性。混合成本也根据压降和输送流体通过通道所需的输入功率进行了评估。无源微混合器模型的水力直径为200 μm,微通道的高度H和节距Pi分别在0.6 ~ 1 mm和1.2 ~ 2 mm范围内调整,Pi/H比值为2。在Re = 2、Re = 10和Re =30时,Pi = 2 mm和H = 1 mm模型的混合效率分别是Pi = 1.2 mm和H = 0.6 mm模型混合指数的1.27倍、1.1倍和1.26倍。这种混合质量的提高是以较低的压降比为代价(分别降低1.18、1.32和1.13倍),较高的输入功率为代价(分别提高1.18、1.49和1.15倍)。
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