Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
4992777 | Experimental Thermal and Fluid Science | 2017 | 8 Pages |
Abstract
Experiments on the total gas holdup, αG, in air-water cylindrical bubble columns were carried out to investigate effects of the column diameter, DH, and the initial liquid height, H0, on αG. Ranges of DH and H0 were 160 ⩽ DH ⩽ 2000 mm and 400 ⩽ H0 ⩽ 4000 mm, respectively. The superficial gas velocity, JG, was varied from 0.025 to 0.35 m/s. The characteristics of gas holdup showed that all the flows in the present experiments were pure heterogeneous. The following conclusions were obtained for αG in air-water bubble columns: (1) the effects of DH and H0 on αG are negligible when scaling up from small to large bubble columns, provided that αG in the small columns are obtained for DH ⩾ 200 mm and H0 â³Â 2200 mm. The height-to-diameter ratio is useless in evaluation of the critical height, above which αG does not depend on H0, (2) for the above ranges of DH and H0, Akita-Yoshida's and Koide's correlations can give good evaluations of αG for a wide range of JG by tuning the model constants, (3) for DH < 200 mm, the decrease in DH increases the population of large bubbles, which results in the decrease in αG, and (4) for H0 â²Â 2200 mm and DH ⩾ 200 mm, αG at a constant JG decreases with increasing H0 and approaches an asymptotic value, and the Froude number using JG and H0 as the characteristic scales well correlates αG in this regime.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
Shohei Sasaki, Kengo Uchida, Kosuke Hayashi, Akio Tomiyama,