| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 10263789 | Chemical Engineering Science | 2005 | 9 Pages |
Abstract
Gas-liquid mass transfer modelling assumed two mass transfer coefficients, one for the clean front of the bubble, the other for the stagnant cap. Adjusted values of these coefficients are consistent with theoretical predictions from Higbie's and Frössling's equations, respectively.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
S.S. Alves, S.P. Orvalho, J.M.T. Vasconcelos,