TY - JOUR
T1 - Bubble formation in cocurrently upward flowing liquid
AU - Terasaka, Koichi
AU - Tsuge, Hideki
AU - Matsue, Hirokazu
PY - 1999/1/1
Y1 - 1999/1/1
N2 - The effects of liquid velocity, nozzle diameter, gas chamber volume and gas flow rate on volumes, shapes and growth curves of bubbles formed at a nozzle submerged in a cocurrently upward flowing liquid in a bubble column were experimentally investigated. The bubble volume decreases with increasing liquid flow velocity. The effect of liquid flow velocity on the volume of bubble increases with an increase in the gas flow rate. To simulate bubble formation at a nozzle submerged in cocurrently upward flowing liquid, a revised non-spherical bubble formation model was proposed. Bubble volumes, bubble growth curves and shapes experimentally obtained in this study, as well as in previous experimental studies, are well predicted by the present model.
AB - The effects of liquid velocity, nozzle diameter, gas chamber volume and gas flow rate on volumes, shapes and growth curves of bubbles formed at a nozzle submerged in a cocurrently upward flowing liquid in a bubble column were experimentally investigated. The bubble volume decreases with increasing liquid flow velocity. The effect of liquid flow velocity on the volume of bubble increases with an increase in the gas flow rate. To simulate bubble formation at a nozzle submerged in cocurrently upward flowing liquid, a revised non-spherical bubble formation model was proposed. Bubble volumes, bubble growth curves and shapes experimentally obtained in this study, as well as in previous experimental studies, are well predicted by the present model.
KW - Bubble
KW - Bubble column
KW - Bubble formation
KW - Bubble formation model
KW - Liquid flow
UR - http://www.scopus.com/inward/record.url?scp=0032827350&partnerID=8YFLogxK
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U2 - 10.1002/cjce.5450770304
DO - 10.1002/cjce.5450770304
M3 - Article
AN - SCOPUS:0032827350
SN - 0008-4034
VL - 77
SP - 458
EP - 464
JO - Canadian Journal of Chemical Engineering
JF - Canadian Journal of Chemical Engineering
IS - 3
ER -