"This study covers three Geldart groups, and includes state-of-the-art experimental measurements and first-principles prediction... The authors solved a longstanding problem in fluidization, namely extremely low Sherwood number of fine particles in fluidized beds... The authors showed that the well-known core-annulus profile reverses in slugging fluidization of Geldart D particles due to particle inertia effects... This new finding is a robust and important one since core-annulus behavior is not desired... These contributions to the field of particle technology are of high impact, and expected to be of lasting influence..." -Christine Hrenya, Professor of Chemical and Biological Engineering, University of Colorado at Boulder. "The authors have shown that we can eliminate the core-annular regime in risers... By directly computing the mass transfer coefficients, the need to include empirical parameters could be eliminated to obtain more accurate conversion rates..."-Reza Mostofi, Ph.D., UOP, A Honeywell Company.
| Autorius: | Mayank Kashyap, Dimitri Gidaspow, |
| Leidėjas: | LAP Lambert Academic Publishing |
| Išleidimo metai: | 2012 |
| Knygos puslapių skaičius: | 696 |
| ISBN-10: | 3659226637 |
| ISBN-13: | 9783659226632 |
| Formatas: | Knyga minkštu viršeliu |
| Kalba: | Anglų |
| Žanras: | Biochemical engineering |
Parašykite atsiliepimą apie „Dispersion and Mass Transfer Coefficients in Fluidized Beds: Experimental and Computational Fluid Dynamics Studies“
