Abstract
An RPB (rotating packed bed) adsorption process was developed to remove emulsified dodecane from water under a centrifugal field. With activated carbon and sawdust as adsorbents, respectively, experimental results showed that the centrifugal force could enhance the rate of adsorption. Although an empirical pseudo-first-order model could describe the adsorption satisfactorily for both RPB and conventional packed bed, a mathematical analysis was provided to obtain mass transfer coefficient. It was shown that mass transfer coefficient increased with increasing rotational speed and liquid rate to the power of 0.81-0.86, and 0.34, respectively. These experimental results are consistent with the theoretical prediction of Munjal et al. (1989a, 1989b).
| Original language | English |
|---|---|
| Pages (from-to) | 531-538 |
| Number of pages | 8 |
| Journal | Journal of the Chinese Institute of Chemical Engineers |
| Volume | 35 |
| Issue number | 5 |
| State | Published - 09 2004 |
Keywords
- Adsorption
- Mass transfer coefficient
- Pseudo-first-order model
- Rotating packed bed