The hydrodynamics and mass transfer, specifically the effects of gas velocity and the presence and type of solids on the gas hold-up and volumetric mass transfer coefficient, were studied on a lab-scale airlift reactor with internal draft tube. Basalt particles and biofilmcoated particles were used
Comparison of Hydrodynamics and Mass Transfer in Airlift and Bubble Column Reactors Using CFD
โ 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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โฆ 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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