Rise velocity of an air bubble in porous media: Theoretical studies

被引:48
|
作者
Corapcioglu, MY [1 ]
Cihan, A [1 ]
Drazenovic, M [1 ]
机构
[1] Middle E Tech Univ, Dept Geol Engn, TR-06531 Ankara, Turkey
关键词
air bubble; bubbly flow; discrete airflow; granular media;
D O I
10.1029/2003WR002618
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
[1] The rise velocity of injected air phase from the injection point toward the vadose zone is a critical factor in in-situ air sparging operations. It has been reported in the literature that air injected into saturated gravel rises as discrete air bubbles in bubbly flow of air phase. The objective of this study is to develop a quantitative technique to estimate the rise velocity of an air bubble in coarse porous media. The model is based on the macroscopic balance equation for forces acting on a bubble rising in a porous medium. The governing equation incorporates inertial force, added mass force, buoyant force, surface tension and drag force that results from the momentum transfer between the phases. The momentum transfer terms take into account the viscous as well as the kinetic energy losses at high velocities. Analytical solutions are obtained for steady, quasi-steady, and accelerated bubble rise velocities. Results show that air bubbles moving up through a porous medium equilibrate after a short travel time and very short distances of rise. It is determined that the terminal rise velocity of a single air bubble in an otherwise water saturated porous medium cannot exceed 18.5 cm/s. The theoretical model results compared favorably with the experimental data reported in the literature. A dimensional analysis conducted to study the effect of individual forces indicates that the buoyant force is largely balanced by the drag force for bubbles with an equivalent radius of 0.2-0.5 cm. With increasing bubble radius, the dimensionless number representing the effect of the surface tension force decreases rapidly. Since the total inertial force is quite small, the accelerated bubble rise velocity can be approximated by the terminal velocity.
引用
收藏
页码:W042141 / W042149
页数:9
相关论文
共 50 条
  • [21] Bubble swarm rise velocity in fluidized beds
    Puncochar, Miroslav
    Ruzicka, Marek C.
    Simcik, Miroslav
    CHEMICAL ENGINEERING SCIENCE, 2016, 152 : 84 - 94
  • [22] The formation method and velocity rise of bubble cluster
    Usanina, A. S.
    Basalaev, S. A.
    Perfilieva, K. G.
    ALL-RUSSIAN CONFERENCE XXXIV SIBERIAN THERMOPHYSICAL SEMINAR, DEDICATED TO THE 85TH ANNIVERSARY OF ACADEMICIAN A. K. REBROV, 2018, 1105
  • [23] Capillary rise in porous media
    Lago, M
    Araujo, M
    PHYSICA A, 2001, 289 (1-2): : 1 - 17
  • [24] Capillary rise in porous media
    Lago, M
    Araujo, M
    JOURNAL OF COLLOID AND INTERFACE SCIENCE, 2001, 234 (01) : 35 - 43
  • [25] Theoretical modeling of squeezing flow in porous media under arbitrary boundary velocity
    Lang, Ji
    Wang, Qianqian
    TRIBOLOGY INTERNATIONAL, 2024, 191
  • [26] Theoretical and Experimental Studies of Hydrodynamics and Heat Exchange in Porous Media
    Direktor, L. B.
    Zaichenko, V. M.
    Maikov, I. L.
    Kosov, V. F.
    Sinel'shchikov, V. A.
    Torchinskii, V. M.
    HIGH TEMPERATURE, 2010, 48 (06) : 887 - 895
  • [27] Theoretical and experimental studies of hydrodynamics and heat exchange in porous media
    L. B. Direktor
    V. M. Zaichenko
    I. L. Maikov
    V. F. Kosov
    V. A. Sinel’shchikov
    V. M. Torchinskii
    High Temperature, 2010, 48 : 887 - 895
  • [28] Bubble formation on porous media surfaces
    Teppner, R
    Schaflinger, U
    DROP-SURFACE INTERACTIONS, 2002, (456): : 291 - 294
  • [29] Bubble Coarsening Kinetics in Porous Media
    Yu, Yuehongjiang
    Wang, Chuanxi
    Liu, Junning
    Mao, Sheng
    Mehmani, Yashar
    Xu, Ke
    GEOPHYSICAL RESEARCH LETTERS, 2023, 50 (01)
  • [30] Visualization of Bubble Formation in Porous Media
    Zhang, Hui
    Frey, Steffen
    Steeb, Holger
    Uribe, David
    Ertl, Thomas
    Wang, Wenping
    IEEE TRANSACTIONS ON VISUALIZATION AND COMPUTER GRAPHICS, 2019, 25 (01) : 1060 - 1069