| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 155730 | Chemical Engineering Science | 2012 | 4 Pages |
Abstract
The mathematical model for a zero length column (ZLC) system has been extended to the practically important situation in which the sorption kinetics are controlled by the combined effect of intracrystalline diffusion and surface resistance to mass transfer. The validity of the new model is demonstrated by application to experimental data for diffusion of ethane in DDR zeolite.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Douglas M. Ruthven, Adam Vidoni,