A comprehensive study on co2‐interphase mass transfer in vertical cocurrent and countercurrent gas‐liquid flow
作者:
W.‐D. Deckwer,
I. Adler,
A. Zaidi,
期刊:
The Canadian Journal of Chemical Engineering
(WILEY Available online 1978)
卷期:
Volume 56,
issue 1
页码: 43-55
ISSN:0008-4034
年代: 1978
DOI:10.1002/cjce.5450560107
出版商: Wiley Subscription Services, Inc., A Wiley Company
数据来源: WILEY
摘要:
AbstractCocurrent and countercurrent absorption and desorption of CO2in water was investigated in tall bubble columns (length 440 and 720 cm, diameter 15 and 20 cm, respectively). Operating conditions were applied which provided for high interphase mass transfer rates. Under these circumstances the relative gas holdup varies considerably with axial position whereas the mean bubble diameter measured at two points was found to be approximately constant. The measured data permit the calculation of local values of interfacial areas, superficial gas velocities, and frequency factors for bubble coalescence and break up.A dispersion model which takes into account the hydrostatic head and a variable gas velocity was applied to describe the measured concentration profiles in both phases. If increased mass transfer coefficients at the column bottom and measured local values of the hold up were used a striking agreement between experimental and predicted profiles could be obtained. The findings lead to a more sophisticated picture of the complex behaviour of gas‐liquid dispersions at high interphase mass transfer rate
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