Development of Microbubble Generator and its Utilization to Enhance the Mass Transfer in the Bubble Plumes and Columns

Author(s):  
Akiko Kaneko ◽  
Xiaobo Gong ◽  
Shu Takagi ◽  
Yoichiro Matsumoto

Microbubble has characteristics of large surface area to unit volume and small buoyancy. We propose an effective technique to generate tiny bubbles less than 200 μm diameter utilizing a venturi tube at high void fraction. The mechanism of bubble breakup in the venturi tube is elucidated that the bubbles expanded after passing through the throat and then shrank rapidly. The tiny bubbles are generated due to the surface instability of shrinking bubbles. The effect of bubble diameter and plume structure on mass transfer efficiency in bubble plumes and columns are investigated numerically. In order to capture the detailed plume structure, the interaction between liquid and bubbles is treated by a two-way coupling Eulerian–Lagrangian method. The gas transfer from bubbles to liquid is computed by modeling the mass transfer rate of individual bubbles. The numerical results show that the dissolution efficiency changes rapidly when the initial bubble size reaches certain value. The effect of bubble-induced liquid velocity on the residence time of microbubbles increases with the decrease of initial bubble diameters, and also increases with the reduction of initial water depth. By comparing the concentrated and uniform bubble injections, the results suggest that the uniform injection provides much better mass transfer efficiency becasue the circulation of liquid induced by bubble is greatly suppressed.

Author(s):  
Xiaobo Gong ◽  
Shu Takagi ◽  
Yoichiro Matsumoto

The effect of the bubble-induced liquid velocity on the mass transfer performance in the bubble plume is analyzed quantitatively with numerical simulations. A two-way coupling Eulerian-Lagrangian approach is used in the modeling of the bubble plumes with mass transfer. The dissolution of oxygen in bubble plumes with the initial bubble diameters from 100μm to 1mm is simulated. The results show that when a single bubble generator is used with the gas flux rate equals 10−8 cubic meter per second, for the plume with 100μm bubbles inside a 0.1m height cubic tank the maximum of the bubble-induced liquid velocity is over 10 times larger than the bubble’s terminal velocity, and the averaged residence time of bubbles in the plume is around one-tenth of the rising period estimated with the terminal velocity of a single bubble. The result suggests that for bubble plumes in a shallow bulk of water, the benefits of using smaller bubbles for high mass transfer efficiency will be overestimated without considering the reduction of the residence time of bubbles because of the bubble-induced liquid velocity. The present simulation shows that the dissolution efficiency of oxygen for the bubble plume with 100μm bubbles in 0.1m tank is around 1/2 of the theoretical value estimated with a single bubble rising with negligible diameter shrink. Compared with a plume in a 0.1m tank, the shrink of bubble diameter and the scattering of bubbles from the center of plume during their rising in a 0.4m tank attenuate the reduction of the averaged residence time because of the acceleration process as shown in a 0.1m tank. The effect of bubble-induced liquid velocity on the mass transfer efficiency for plumes with initial bubble diameter smaller than 160μm does not present obviously in a 0.4m tank as it does in the shorter tank.


1987 ◽  
Vol 23 (9) ◽  
pp. 426-428
Author(s):  
K. F. Bogatykh ◽  
M. N. Minnullin ◽  
A. F. Artem'ev

2012 ◽  
Vol 47 (3) ◽  
pp. 432-439 ◽  
Author(s):  
Srestha Chaturabul ◽  
Pharannalak Wannachod ◽  
Bongkotch Rojanasiraprapa ◽  
Supat Summakasipong ◽  
Anchaleeporn W. Lothongkum ◽  
...  

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