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Pressure drops of single and two-phase flows through T-type microchannel mixers

机译:pressure drops of single and two-phase flows through T-type microchannel mixers

摘要

In this paper, preliminary experimental results are presented on pressure drop characteristics of single and two-phase flows through two T-type rectangular microchannel mixers with hydraulic diameters of 528 and 333 mum, respectively. It is shown that both N-2 and water single-phase laminar flows in microchannels, with consideration of experimental uncertainties, are consistent with classic theory, if additional effects, such as entrance effects that will interfere with the interpretation of experimental results, are eliminated by carefully designing the experiments. The obtained pressure drop data of N-2-water two-phase flow in micromixers are analyzed and compared with existing flow pattern-independent models. It is found that the Lockhart-Martinelli method generally underpredicts the frictional pressure drop. Thereafter, a modified correlation of C value in the Chisholm's equation based on linear regression of experimental data is proposed to provide a better prediction of the two-phase frictional pressure drop. Also among the homogeneous flow models investigated, the viscosity correlation of McAdams indicates the best performance in correlating the frictional pressure drop data (mean deviations within +/-20% for two micromixers both). Finally it is suggested that systematic studies are still required to accurately predict two-phase frictional performance in microchannels. (C) 2004 Elsevier B.V. All rights reserved.
机译:本文给出了通过两个分别为水力直径为528和333μm的T型矩形微通道混合器的单相和两相流压降特性的初步实验结果。结果表明,考虑到实验的不确定性,在微通道中的N-2和水单相层流均与经典理论相一致,如果消除了其他影响,例如会影响实验结果解释的入口效应,通过精心设计实验。分析了在微型混合器中获得的N-2-水两相流的压降数据,并将其与现有的与流型无关的模型进行了比较。发现,洛克哈特-马丁内利方法通常会低估摩擦压降。此后,基于实验数据的线性回归,提出了Chisholm方程中C值的修正相关性,以提供对两相摩擦压降的更好预测。同样在研究的均相流动模型中,McAdams的粘度相关性表明在关联摩擦压降数据方面的最佳性能(两个微型混合器的均值偏差均在+/- 20%之内)。最后,建议仍需要系统研究来准确预测微通道中的两相摩擦性能。 (C)2004 Elsevier B.V.保留所有权利。

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    Yue J; Chen GW; Yuan Q;

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