Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
4768916 | Fuel Processing Technology | 2017 | 10 Pages |
Abstract
Results on axial mixing showed improved mixing with increasing fluidisation velocity and bed height. The lateral dispersion coefficients were in the order of 10â 3-10â 2 m2/s (on an up-scaled basis), increased with fluidisation velocity, and were only moderately influenced by the configuration of the gas distributor.
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Anna Köhler, David Pallarès, Filip Johnsson,