| dc.contributor.author |
Asfour, Abdel Fattah A. |
en_US |
| dc.date.accessioned |
2009-11-25T13:03:12Z |
|
| dc.date.available |
2009-11-25T13:03:12Z |
|
| dc.date.issued |
1990 |
en_US |
| dc.identifier.citation |
Engineering Journal of Qatar University, 1990, Vol. 3, Pages 213-233. |
en_US |
| dc.identifier.uri |
http://hdl.handle.net/10576/7824 |
|
| dc.description.abstract |
A model for describing mass transfer in three-phase fluidized beds has been developed and tested using experimental data.
The presence of two distinguishable mass transfer zones in three-phase fluidized beds led to the idea of interfacing a plug flow model (PFM) with an axial dispersion model (ADM) at the separation boundary between these zones to yield the proposed model.
The model reported here has been valildated at a wide range of operating conditions and proved to perform better than other existing models. |
en_US |
| dc.language.iso |
en |
en_US |
| dc.publisher |
Qatar University |
en_US |
| dc.subject |
Engineering: Chemical Engineering |
en_US |
| dc.title |
An Improved Model Describing Mass Transfer In Three-Phase Fluidized Beds |
en_US |
| dc.type |
Article |
en_US |
| dc.identifier.pagination |
213-233 |
en_US |
| dc.identifier.volume |
3 |
en_US |