Characteristics of flow fields in the gas-liquid mini-bubble columns with particle image velocimetry measurements

被引:11
作者
Li, Chen [1 ]
Ma, Yongli [1 ]
Liu, Mingyan [1 ,2 ]
Wang, Kaiyue [1 ]
机构
[1] Tianjin Univ, Sch Chem Engn & Technol, Tianjin 300350, Peoples R China
[2] Tianjin Univ, State Key Lab Chem Engn, Tianjin, Peoples R China
基金
中国国家自然科学基金;
关键词
bubble column; microfluidics; multiphase flow; particle measurements; particle technology; MICRO-FLUIDIZED-BEDS; SMALL AIR BUBBLES; MASS-TRANSFER; HEAT-TRANSFER; BEHAVIOR; HOLDUP; PHASE; PIV; HYDRODYNAMICS; DIAMETER;
D O I
10.1002/aic.17798
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
As a new type of gas-liquid microreactors, the gas-liquid mini-bubble column has potential applications. However, few studies on the flow fields in the mini-bubble column can be found at present. In this work, particle image velocimetry (PIV) was used to visually study the velocity fields, vorticity fields and bubble dynamics in the gas-liquid mini-bubble columns with column inner diameters of 1-3 mm and mini-bubble diameters ranged from 0.7 to 1.3 mm. It is found that with the increase of superficial liquid velocity, bubbles rose from almost straight line to Z-shaped or S-shaped trajectory, and the bubble trajectory changed from one-dimension to three-dimension; when the bubble velocity changed, the bubble size and gas holdup decreased; bubble terminal velocity was controlled by bubble buoyancy and flow resistance, and increased slightly with bubble coalescence. These findings may provide basic reference for the design and scale-up of such a mini-bubble column reactor.
引用
收藏
页数:16
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