| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 9680943 | Desalination | 2005 | 12 Pages |
Abstract
A simplified mathematical model is developed to describe multicomponent mass transfer in the gas phases, in which a pseudo-binary diffusion approach is assumed; molecular diffusion is considered as the prevailing transport mechanism through the membrane. The results obtained are compared with the experiments and the validity range of the model is defined.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Filtration and Separation
Authors
Cristiana Boi, Serena Bandini, Giulio Cesare Sarti,