Abstract
The present state of the art in the experimental determination of mass transfer coefficient in Air Lift Reactors is reviewed. A Criterion which allows to decide whether the assumption of perfect mixing of the liquid phase is valid was experimentally verified. For the cases where such assumption does not hold, a new method that renders local values of KLa in each of the regions of the reactor (riser, downcomer and gas separator) is presented. The model is based on a fluid dynamic structred model of the system.
Original language | English |
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Pages (from-to) | 2221-2226 |
Number of pages | 6 |
Journal | Chemical Engineering Science |
Volume | 47 |
Issue number | 9-11 |
DOIs | |
State | Published - 8 Jun 1992 |
Keywords
- Air Lift
- Mass Transfer rate
- Structured Model
ASJC Scopus subject areas
- General Chemistry
- General Chemical Engineering
- Industrial and Manufacturing Engineering