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Simultaneous Investigation of Entrained Liquid Fraction, Liquid Film Thickness and Pressure Drop in Vertical Annular Flow

机译:垂直环形流中夹带液体分数,液膜厚度和压降的同时研究

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摘要

The mechanism of atomization of part of the liquid film to form drops in annular two-phase flow is not entirely understood. It has been observed that drop creation only occurs when there are large disturbance waves present on the film interface. (Woodmansee and Har-rantty, 1969, "Mechanisms for the Removal of Droplets From a Liquid Surface by a Parallel Air Flow," Chem. Eng. Sci., 24, pp. 299-307) observed that ripples on these waves were precursors to drops. Though it has been reported that drops occur in bursts by (Azzopardi, Gas-Liquid Flows Begell House Inc., New York, 2006), all previous drop size or concentration measurements have always been time integrated to simplify data analysis. Dynamic time averaged drop size measurements are reported for the first time in annular flow. Experiments were carried out on a 19 mm internal diameter vertical pipe with air and water as fluids. Spraytec, a laser diffraction-based, drop size measurement instrument, was used in the drop related data acquisition. Simultaneous time-resolved measurements were carried out for drop, film thickness, and pressure drop. Film thickness has been measured using the conductance probes employing a pair of flush mounted rings as electrodes. Pressure drop was logged using differential pressure cell connected to two pressure taps located within the test section. The gas superficial velocity was varied systematically from 13 to 43 m/s at fixed liquid superficial velocities of 0.05 and 0.15 m/s, respectively. Additional tests were carried out with the gas velocity fixed at 14 m/s while the liquid superficial velocity was varied from 0.03 to 0.18 m/s. Signal acquired are presented in form of time series to permit data analysis at different levels. Based on signal analysis, interrelationships between liquid film where the drops are sourced and the contribution of the entrained liquid droplets to the overall pressure drop in the system has been elucidated. Though structures are not clearly visible in the signals acquired, the time series have been analyzed in amplitude space to yield probability density function (Pdf). Beyond gas superficial velocity of 30 m/s, Pdf of drop size distribution becomes monomodal or single-peaked marking transition to mist annular flow.
机译:尚不完全了解部分液膜雾化形成环形两相流液滴的机理。已经观察到,仅当在膜界面上存在大的干扰波时才产生液滴。 (Woodmansee and Har-rantty,1969,“通过平行气流从液体表面去除液滴的机理”,《化学工程学报》,24,pp。299-307)观察到这些波上的波纹是前兆。掉下来。尽管据报道(Azzopardi,Gas-Liquid Flows Begell House Inc.,纽约,2006年)突然出现液滴,但所有以前的液滴大小或浓度测量值始终经过时间积分以简化数据分析。动态时间平均液滴尺寸测量首次在环形流中报告。实验是在19毫米内径的垂直管上进行的,空气和水为流体。 Spraytec,一种基于激光衍射的液滴尺寸测量仪器,用于液滴相关数据的采集。同时进行了时间分辨的测量,以测定液滴,膜厚和压降。使用电导探针测量薄膜厚度,该电导探针使用一对齐平安装的环作为电极。使用连接到位于测试区域内的两个压力开关的差压传感器记录压降。气体表观速度在固定的液体表观速度分别为0.05和0.15 m / s时从13到43 m / s有系统地变化。气体速度固定为14 m / s时进行了其他测试,而液体表观速度从0.03变为0.18 m / s。采集的信号以时间序列的形式呈现,以允许在不同级别进行数据分析。基于信号分析,阐明了液滴来源的液膜与夹带液滴对系统中总压降的贡献之间的相互关系。尽管在所采集的信号中结构并不清晰可见,但已在幅度空间中分析了时间序列,以产生概率密度函数(Pdf)。超过30 m / s的气体表观速度,液滴尺寸分布的Pdf变为单峰或单峰标记过渡到雾状环形流。

著录项

  • 来源
    《Journal of Energy Resources Technology》 |2011年第2期|p.023103.1-023103.10|共10页
  • 作者

    M. B. Alamu; B. J. Azzopardi;

  • 作者单位

    Floxpat Petroleum and Energy Services, 145-157 St. John Street, London EC1V 4PW.UK;

    Chemical Engineering Department, University of Nottingham, University Park, Nottingham NG7 2RD, UK;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    gas; liquid; drops; entrained fraction; void fraction; annular;

    机译:加油站;液体;掉落夹带分数;空隙率环形的;
  • 入库时间 2022-08-18 00:30:15

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