首页> 外文会议>International Conference on Nanochannels, Microchannels and Minichannels; 20070618-20; Puebla(MX) >TWO-PHASE FLOW CHARACTERISTICS IN A CO-FLOW INDUCED MICROCHANNEL WITH MICROBUBBLES GENERATION
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TWO-PHASE FLOW CHARACTERISTICS IN A CO-FLOW INDUCED MICROCHANNEL WITH MICROBUBBLES GENERATION

机译:带有微泡产生的共流诱导微通道中的两相流特性

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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:本文提出了一种微流体装置,该装置会产生直径范围为70μm至160μm的微气泡,并测试了该装置的两相流动特性。该设备由三个子通道组成:中心气体通道(10μm×50μm)和气体通道两侧的两个液体通道(均为85μm×50μm)。当阻力随着气泡的增长而变得大于表面张力时,微气泡是由气体和液体在气体通道出口处的共同流动产生的。使用甲醇以及CO_2和N_2的气体混合物作为工作流体。由于气体的流量非常小,因此认为气体动量效应可以忽略不计。因此,在当前情况下,控制参数是液体表观速度和气体的入口压力。使用高速相机记录设备的两相流模式和微气泡。为了限制微气泡的产生范围,首先观察装置中的两相流型。观察到四种不同的流动模式:环形,环形团状,团状和气泡状流动。在气泡流中,产生均匀尺寸的微气泡,并且液体表观速度和气体压力的操作范围分别低于0.132m / s和0.7bar。随着较高的表观液体速度和/或较低的气压,微气泡的直径显得较小。实验结果表明,当气压低于一定水平时,微气泡的大小几乎对气压不敏感。在这样的范围内,微气泡直径可以通过阻力系数相关系数C_(Dw)= 31330 / Re〜3来估算,这与宏通道的相关系数有所不同,因为微通道的壁效应更大。渠道。在本文的后半部分,作为将微气泡发生器应用于气体分析的潜力,研究了气体成分在液流中的溶解行为。结果表明,如果可以有效地控制气泡尺寸,可以进行适当的改进,则可以将微气泡发生器用作小型气体分析仪的组成部分。

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