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Comparison of Hydrodynamics and Mass Transfer in Airlift and Bubble Column Reactors Using CFD

โœ Scribed by J.M. van Baten; R. Krishna


Publisher
John Wiley and Sons
Year
2003
Tongue
English
Weight
133 KB
Volume
26
Category
Article
ISSN
0930-7516

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โœฆ Synopsis


Abstract

Computational Fluid Dynamics (CFD) is used to compare the hydrodynamics and mass transfer of an internal airlift reactor with that of a bubble column reactor, operating with an air/water system in the homogeneous bubble flow regime. The liquid circulation velocities are significantly higher in the airlift configuration than in bubble columns, leading to significantly lower gas holdups. Within the riser of the airlift, the gas and liquid phases are virtually in plug flow, whereas in bubble columns the gas and liquid phases follow parabolic velocity distributions. When compared at the same superficial gas velocity, the volumetric mass transfer coefficient, k~L~a, for an airlift is significantly lower than that for a bubble column. However, when the results are compared at the same values of gas holdup, the values of k__~L~__a are practically identical.


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