Article ID Journal Published Year Pages File Type
6584634 Chemical Engineering Journal 2015 9 Pages PDF
Abstract
In this study, the oxygen transfer rate (OTR), bubble size distribution, interfacial area per unit volume and liquid film mass transfer coefficient have all been measured in a 0.39 m diameter pilot-scale bubble column operated at industrially relevant superficial velocities between 0.14 and 0.28 m s−1 for which few data exist in the literature. The measured OTR ranged from 6.5 to 8.8 kg m−3 h−1, with values generally increasing with superficial velocity. The mean bubble size in the column was 3-5 mm, giving an interfacial area per unit volume for mass transfer of some 380-570 m2 m−3. Experimental data were used to validate a computational fluid dynamics (CFD) based model of the bubble column; it was found that this model could predict the experimentally measured OTR within 20% across the range of superficial velocities examined.
Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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