Abstraet--A new approach to the modelling of gross gas-solids flow through the riser in a circulating fluidized-bed system is proposed in this paper. This approach differs from the previous ones, which are found to be theoretically incorrect based on a fundamental analysis of the riser process hydro
Factors affecting solids segregation in circulating fluidized-bed riser
β Scribed by B. Hirschberg; J. Werther
- Publisher
- American Institute of Chemical Engineers
- Year
- 1998
- Tongue
- English
- Weight
- 1014 KB
- Volume
- 44
- Category
- Article
- ISSN
- 0001-1541
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β¦ Synopsis
Axial and radial segregation effects due to differences in particle sizes and solids densities were studied in a 0.2-m-dia. riser at gas velocities between 3.5 and 7 m/s and solids circulation rates between 8 and 40 kg/(m2.s). Two bed materials (a quartz sand/iron powder mixture and a quartz sand with a broad size distribution) with identical terminal velocity distributions were used. Local mean particle sizes and local mass fractions of the iron powder (for the mixture) decreased with height. Measurements of the solids streams revealed that the downflowing solids consist preferentially of large and/or hea y particles, while the reverse happens in the upward solids flow. The single particle terminal velocity is the decisive parameter affecting solids segregation. The comparison of both bed materials indicates that two bed materials will exhibit the same segregation patterns only i f the distributions of the particles' terminal uelocities in both materials are the same.
π SIMILAR VOLUMES
Results of detailed experimental measurements of solids mass flux profiles in circulating tfuidized-bed risers of internal diameter 0.152 and 0.305 m are described. The ranges of superficial gas velocity and mean solids mass flux used were 3-5 m s-1 and 2-111 kg m ' s I, respectively, and the solids