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- Publisher
- Wiley
- Copyright
- Copyright © 2002 Canadian Society for Chemical Engineering
- ISSN
- 0008-4034
- eISSN
- 1939-019X
- DOI
- 10.1002/cjce.5450800507
- Publisher site
- See Article on Publisher Site
Abstract
Volumetric gas—liquid mass transfer coefficient (kLa) data available in the literature for larger tanks (T = 0.39 m to 2.7 m) have been analyzed on the basis of relative dispersion parameter, N/Ncd. It was observed that at a given superficial gas velocity (VG), kLa values were approximately the same irrespective of geometric configuration (size of the tank, type and size of the impellers, type of the sparger, etc.) at a particular N/Ncd. A single correlation based on N/Ncd is presented which shows satisfactory agreement with the kLa data of different workers.
Journal
The Canadian Journal of Chemical Engineering – Wiley
Published: Oct 1, 2002