Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
153051 | Chemical Engineering Journal | 2008 | 11 Pages |
Abstract
The hydrodynamic characteristics in the bottom region of circulating fluidized bed (CFB) risers with fluid catalytic cracking (FCC) particles were studied over a wide range of operating conditions. The results included radial solids concentration and corresponding radial profiles of standard deviation, particle velocity profiles, and probability density distributions. Comparisons were made between the flow structures in the riser bottom region and those in bubbling and turbulent fluidized beds.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Chemical Engineering (General)
Authors
Haiyan Zhu, Jesse Zhu,