XING Dian-chuan, SUN Li-cheng, YAN Chang-qi, TIAN Dao-gui. Experimental Investigation on Void Fraction Radial Distribution for Bubbly Flow in Vertical Circular Tube[J]. Atomic Energy Science and Technology, 2013, 47(2): 233-237. DOI: 10.7538/yzk.2013.47.02.0233
Citation: XING Dian-chuan, SUN Li-cheng, YAN Chang-qi, TIAN Dao-gui. Experimental Investigation on Void Fraction Radial Distribution for Bubbly Flow in Vertical Circular Tube[J]. Atomic Energy Science and Technology, 2013, 47(2): 233-237. DOI: 10.7538/yzk.2013.47.02.0233

Experimental Investigation on Void Fraction Radial Distribution for Bubbly Flow in Vertical Circular Tube

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  • The radial distribution of air-water two-phase upward bubbly flow in a vertical circular tube (ID 50 mm) was investigated experimentally by using the optical fiber probe under ambient temperature and pressure. The results show that the radial distribution of void fraction changes with different superficial gas and liquid velocities. The void fraction is almost invariable along radius except in the near wall region where it has a peak and then decreases sharply at high superficial liquid velocity which is called “wall peak”. In the case of stagnant liquid, the increasing rate for void fraction becomes slower as the radial position varies from the center to the wall with the increase of superficial gas velocity. When the superficial gas velocity increases, the void fraction decreases radially from the core to the wall location, namely “core peak”. When the liquid velocity is low, the void fraction distribution behaves as the transition pattern. The relative deviration of the probe measured area-weighted averaged void fraction against that based on pressure drop is less than 10%.
  • [1]
    SCHLEGEL J, HIBIKI T, ISHII M. Development of a comprehensive set of drift-flux constitutive models for pipes of various hydraulic diameters[J]. Progress in Nuclear Energy, 2010, 52(7): 666-677.
    [2]
    SCHLEGEL J P, SAWANT P, PARANJAPE S, et al. Void fraction and flow regime in adiabatic upward two-phase flow in large diameter vertical pipes[J]. Nuclear Engineering and Design, 2009, 239(12): 2864-2874.
    [3]
    周云龙,孙斌,赵鹏,等. 垂直上升管气液两相流截面含气率的理论模型[J]. 水动力学研究与进展:A辑,2003,18(6):783-785.ZHOU Yunlong, SUN Bin, ZHAO Peng, et al. The theoretical model for void fraction of gas-liquid two phase flow in vertical tubes[J]. Journal of Hydrodynamics: Ser A, 2003, 18(6): 783-785(in Chinese).
    [4]
    孙奇,赵华,杨瑞昌,等. 垂直上升两相流漂移流模型研究[J]. 核动力工程,2006,27(2):40-44.SUN Qi, ZHAO Hua, YANG Ruichang, et al. Drift flux model for vertical upward two-phase flow[J]. Nuclear Power Engineering, 2006, 27(2): 40-44(in Chinese).
    [5]
    SHEN X, MISHIMA K, NAKAMURA H. Two-phase phase distribution in a vertical large diameter pipe[J]. Int J Heat Mass Transfer, 2005, 48(1): 211-225.
    [6]
    郑荣钏,杨瑞昌,沈幼庭. 单纤光纤探针测量空泡份额的实验研究[J]. 工程热物理学报,1997,18(1):99-102.ZHENG Rongchuan, YANG Ruichang, SHEN Youting. Measurement of void fraction by an advanced single-fiber optical probe[J]. Journal of Engineering Themophysics, 1997, 18(1): 99-102(in Chinese).
    [7]
    陈听宽. 两相流与传热研究[M]. 西安:西安交通大学出版社,2004:364-371.
    [8]
    阎昌琪. 气液两相流[M]. 哈尔滨:哈尔滨工程大学出版社,2009:40-49.
    [9]
    LUCAS D, KREPPER E, PRASSER H M. Use of models for lift, wall and turbulent dispersion forces acting on bubbles for poly-disperse flows[J]. Chemical Engineering Science, 2007, 62(15): 4146-4157.
    [10]
    张立英,黄青山. 气升式环流反应器的理论研究进展[J]. 过程工程学报,2011,11(1):162-173.ZHANG Liying, HUANG Qingshan. Research progress in the modeling theory of airlift loop reactor[J]. The Chinese Journal of Process Engineering, 2011, 11(1): 162-173(in Chinese).

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