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TWO-PHASE FLOW CHARACTERISTICS IN A CO-FLOW INDUCED MICROCHANNEL WITH MICROBUBBLES GENERATION

机译:与微泡生成的混合诱导微通道中的两相流动特性

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This paper presents a micro-fluidic device which generates micro-bubbles, ranging from 70μm to 160μm in diameter, and two-phase flow characteristics in the device were tested. The device is composed of three sub-channels: a centered gas channel (10μm × 50μm) and two liquid channels (both with 85μm ×50μm) on each side of the gas channel. Micro-bubbles are generated by co-flow of gas and liquid at the exit of the gas channel when the drag force becomes larger than the surface tension force as bubbles grow. Methanol and a gas mixture of CO_2 and N_2 were used as the working fluid. Since the flow rate of gas was very small, the gas momentum effect was considered negligible. Thus, in the present case, the controlling parameters were the liquid superficial velocity and the inlet pressure of the gas. A high speed camera was used to record two-phase flow patterns and micro-bubbles of the device. To confine the ranges of the micro-bubbles generation, two-phase flow patterns in the device is observed at first. Four different flow patterns were observed: annular, annular-slug, slug, and bubbly flow. In bubbly flows, uniform-sized micro-bubbles were generated, and the operating ranges of the liquid superficial velocity and the gas pressure were below 0.132 m/s and 0.7 bar, respectively. Diameters of the micro-bubbles appeared smaller with the higher superficial liquid velocity and/or with a lower gas pressure. Experimental results showed that, with the gas pressure lower than a certain level, the sizes of micro-bubbles were almost insensitive to the gas pressure. In such a ranges, the micro-bubble diameters could be estimated from a drag coefficient correlation, C_(Dw) = 31330/Re~3, which is different from the correlations for macro-channels due to a larger wall effect with the micro-channels. In the latter part of the paper, as a potential of application of the micro-bubble generator to gas analysis, dissolution behavior of the gas components into the liquid flow was examined. The result shows that the micro-bubble generator can be adopted as a component of miniaturized gas analyzers if a proper improvement could be made in controlling the bubble sizes effectively.
机译:本文介绍了一种微气体器件,其产生微气泡,直径为70μm至160μm,测试装置中的两相流动特性。该器件由三个子通道组成:气体通道的每一侧是一个居中的气体通道(10μm×50μm)和两个液体通道(两侧,两者均以85μm×50μm)。当拖曳力变得大于气泡生长时,通过气体通道的出口处的气体和液体在气体通道的出口处产生微气泡而产生微气泡。甲醇和CO_2和N_2的气体混合物用作工作流体。由于气体的流速非常小,因此煤气效应被认为是可忽略的。因此,在当前情况下,控制参数是气体的液体浅表速度和入口压力。高速相机用于记录设备的两相流动模式和微气泡。为了限制微气泡产生的范围,首先观察到装置中的两相流动模式。观察到四种不同的流动模式:环形,环形块,块和起泡流动。在气泡流动中,产生均匀大小的微气泡,并且液体表面速度和气体压力的操作范围分别低于0.132m / s和0.7巴。微气泡的直径较小,具有较高的表面液体速度和/或气体压力较低。实验结果表明,随着低于一定水平的气体压力,微气泡的尺寸几乎对气体压力不敏感。在这样的范围内,可以从拖动系数相关性估计微气泡直径,C_(DW)= 31330 / Re〜3,这与由于微观的墙壁效应较大的墙壁效应而不同,这与宏通道的相关性不同渠道。在本文的后半部分中,作为将微气泡发生器施加到气体分析的潜力,检查气体组分的溶解行为进入液体流动。结果表明,如果可以在有效地控制气泡尺寸方面,可以采用微气泡发生器作为小型化气体分析仪的组件。

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