Abstract
Circulating Fluidized-Bed (CFB) Risers with Geldart Group B Particles Have Found Significant Application in Combustion Reactions. the Present Work Attempts to Study the Solids Flow Dynamics in a CFB Riser that is Operated with Group B Particles, using Computational Fluid Dynamics (CFD) Techniques. the Key Feature in the Present Study is that the Various Closure Schemes in the CFD Model Have Been Evaluated Against Data from Non-Invasive Experimental Techniques: Computer Automated Radioactive Particle Tracking (CARPT) for Solids Velocity Field and Computed Tomography (CT) for Solids Holdup. Since Solids Flow in a Riser is Multiscale in Character, in Addition to the Measured Averaged Solids Velocity Profiles and Solids' Fraction Profiles in the Experimental Section, Mean Granular Temperature Profiles Have Also Been Compared. Two Flow Regimes (Viz., Fast Fluidization and Dilute Phase Transport) Have Been Considered in This Study. © 2007 American Chemical Society.
Recommended Citation
S. Vaishali et al., "Numerical Simulation of Gas-Solid Dynamics in a Circulating Fluidized-Bed Riser with Geldart Group B Particles," Industrial and Engineering Chemistry Research, vol. 46, no. 25, pp. 8620 - 8628, American Chemical Society, Dec 2007.
The definitive version is available at https://doi.org/10.1021/ie0700819
Department(s)
Chemical and Biochemical Engineering
International Standard Serial Number (ISSN)
0888-5885
Document Type
Article - Conference proceedings
Document Version
Citation
File Type
text
Language(s)
English
Rights
© 2023 American Chemical Society, All rights reserved.
Publication Date
05 Dec 2007
