Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
9623839 | Chemical Engineering Journal | 2005 | 9 Pages |
Abstract
A low Reynolds number k-É computational fluid dynamics (CFD) model has been used for the description of flow pattern near the wall. An excellent agreement has been shown between the predicted and experimental hold-up and velocity profiles. The CFD model has been extended for the prediction of heat transfer for two-phase gas-liquid flows in bubble columns. A comparison has been presented between the predicted and the experimental data.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Mahesh T. Dhotre, Vivek S. Vitankar, Jyeshtharaj B. Joshi,