Falling of a Spherical Particle in Fine-Bubble Plume and Fine-Bubble Behavior around the Particle

被引:0
作者
Takamure, K. [1 ]
Kawasaki, Y. [2 ]
Degawa, T. [1 ]
Uchiyama, T. [1 ]
机构
[1] Nagoya Univ, Inst Mat & Syst Sustainabil, Chikusa Ku, Furo Cho, Nagoya, Aichi 4648601, Japan
[2] Japan Tobacco Inc, Minato Ku, 4-1-1 Toranomon, Tokyo 1056927, Japan
关键词
three-phase gas-liquid-solid flow; microbubble plume; solid spherical particle; wake; PIV; DIRECT NUMERICAL SIMULATIONS; INDUCED CAVITATION BUBBLE; AIRLIFT PUMP; RISE; PERFORMANCE; SUSPENSION; DYNAMICS; VELOCITY; FLUID; WATER;
D O I
10.1134/S001546282105013X
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
In this study, the interaction between a spherical solid particle descending in a fine-bubble plume and the fine-bubbles around the particle is investigated experimentally. The fine-bubbles, which are formed by water electrolysis and have an average diameter of 0.037 mm, rise via buoyancy to form bubble plumes. The average bubble velocity in the conduit is 0.05 mm/s. A spherical solid particle with a diameter of 11.1 mm and a density of 1130 kg/m(3) is dropped into the fully-developed bubble plume. The particle falls in a meandering motion in the fine-bubble plume. In this process, the terminal velocity of the particles falling in the fine-bubble plume is almost identical to that of a particle falling in the quiescent water. Additionally, after the fine-bubbles have been separated from the particle surface, they flow into the wake of the particle, forming a stagnant region. The particle wake diameter increases threefold, as compared with its value in the downstream direction of the fine-bubble plume.
引用
收藏
页码:612 / 621
页数:10
相关论文
共 27 条
[1]   Numerical and Experimental Study of Bubble Dynamics in Contact with a Solid Surface [J].
Abramova, O. A. ;
Akhatov, I. Sh. ;
Gumerov, N. A. ;
Pityuk, Yu. A. ;
Sametov, S. P. .
FLUID DYNAMICS, 2018, 53 (03) :337-346
[2]   Unsteady rise of a bubble in a viscous fluid at small Reynolds numbers [J].
Arkhipov, V. A. ;
Vasenin, I. M. ;
Tkachenko, A. S. ;
Usanina, A. S. .
FLUID DYNAMICS, 2015, 50 (01) :79-86
[3]   Wall effects on the velocities of a single sphere settling in a stagnant and counter-current fluid and rising in a co-current fluid [J].
Arsenijevic, Z. Lj ;
Grbavcic, Z. B. ;
Garic-Grulovic, R. V. ;
Bakovic-Vragolovic, N. M. .
POWDER TECHNOLOGY, 2010, 203 (02) :237-242
[4]   SOLID LIQUID MASS-TRANSFER IN A GAS-LIQUID SOLID FLUIDIZED-BED [J].
ARTERS, DC ;
FAN, LS .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (01) :107-115
[5]   Direct Numerical Simulations of gas-liquid-solid three phase flows [J].
Baltussen, M. W. ;
Seelen, L. J. H. ;
Kuipers, J. A. M. ;
Deen, N. G. .
CHEMICAL ENGINEERING SCIENCE, 2013, 100 :293-299
[6]   FLOW VISUALIZATION IN WATER - A REVIEW OF TECHNIQUES [J].
CLAYTON, BR ;
MASSEY, BS .
JOURNAL OF SCIENTIFIC INSTRUMENTS, 1967, 44 (01) :2-&
[7]   ON THE DRAG COEFFICIENT OF A SPHERE [J].
FLEMMER, RLC ;
BANKS, CL .
POWDER TECHNOLOGY, 1986, 48 (03) :217-221
[8]   Operation performance of a small air-lift pump for conveying solid particles [J].
Fujimoto, H ;
Ogawa, S ;
Takuda, H ;
Hatta, N .
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2003, 125 (01) :17-25
[9]   Experimental and analytical investigations of airlift pumps operating in three-phase flow [J].
Kassab, S. Z. ;
Kandil, H. A. ;
Warda, H. A. ;
Ahmed, W. H. .
CHEMICAL ENGINEERING JOURNAL, 2007, 131 (1-3) :273-281
[10]   Numerical modeling of the free rise of an air bubble [J].
Kozelkov, A. S. ;
Kurkin, A. A. ;
Kurulin, V. V. ;
Lashkin, S. V. ;
Tarasova, N. V. ;
Tyatyushkina, E. S. .
FLUID DYNAMICS, 2016, 51 (06) :709-721