Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
6589476 | Chemical Engineering Science | 2015 | 11 Pages |
Abstract
Despite obvious shortcomings of the models for this application, some conclusions on the suitability of certain mixer designs for gas-liquid dispersion may be drawn already. The swirling flows created by the twist and turn of the helical mixer elements, which in turn pushes the lighter phase towards the center of the pipe is well predicted and validated. Further investigations have to consider the bubble size distribution e.g. by a population balance model to accurately predict the dispersion of the gas phase within and downstream the helical static mixer.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
F. Zidouni, E. Krepper, R. Rzehak, S. Rabha, M. Schubert, U. Hampel,