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Gas-liquid two-phase flow splitting at microchannel junctions with different branch angles

机译:气液两相分流在不同分支角的微通道交汇处

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摘要

In the present work, the phase split occurring at microchannel junctions with the square cross-section of 0.5 x 0.5 mm~2 was investigated experimentally under adiabatic condition. Microchannel junctions with five different branch angles varying from 30° to 150° were manufactured. Two different methods of controlling gas/liquid division from the run/the branch were employed, suitable for acquiring splitting data for a wide range of flow patterns covering slug flow, slug-annular flow and annular flow. The inlet superficial velocities varied from 0.8 to 21.3 m/s for gas phase (nitrogen), and from 0.019 to 0.356 m/s for liquid phase (pure water). The high speed recording technique was utilized to elucidate the fluid dynamics of two-phase flow splitting at microchannel junctions. Data analysis revealed that the phase splitting curves did not simply take on a transitional characteristic when the inlet flow pattern changed from slug flow to annular flow. Furthermore, the liquid taken off from the branch did not decrease with increasing branch angle for all kinds of inlet flow patterns. Finally, by comparing the present data with those of mini- and macro-scale research, it was found that more liquid was taken off from the branch at microchannel junctions.
机译:在目前的工作中,在绝热条件下实验研究了在横截面为0.5 x 0.5 mm〜2的微通道结处发生的相分离。制造了具有从30°到150°不等的五个不同分支角的微通道结。采用了两种从运行/支路控制气/液分配的方法,这些方法适用于获取涵盖段塞流,段塞环流和环形流的各种流动模式的分裂数据。气相(氮气)的入口表观速度从0.8到21.3 m / s,液相(纯水)的入口表观速度从0.019到0.356 m / s。高速记录技术被用来阐明在微通道连接处的两相流分裂的流体动力学。数据分析表明,当入口流型从团状流变为环形流时,相分离曲线不仅具有过渡特性。此外,对于所有类型的入口流型,从分支排出的液体都不会随着分支角的增加而减少。最后,通过将当前数据与微型和宏观研究的数据进行比较,发现在微通道连接处更多的液体从分支中排出。

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