Verification of filtered two‐fluid models for gas‐particle flows in risers
- 3 November 2010
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 57 (10) , 2691-2707
Abstract
The effect of solid boundaries on the closure relationships for filtered two‐fluid models for riser flows was probed by filtering the results obtained through highly resolved kinetic theory‐based two‐fluid model simulations. The closures for the filtered drag coefficient and particle phase stress depended not only on particle volume fraction and the filter length but also on the distance from the wall. The wall corrections to the filtered closures are nearly independent of the filter length and particle volume fraction. Simulations of filtered model equations yielded grid length independent solutions when the grid length is ∼half the filter length or smaller. Coarse statistical results obtained by solving the filtered models with different filter lengths were the same and corresponded to those from highly resolved simulations of the kinetic theory model, which was used to construct the filtered models, thus verifying the fidelity of the filtered modeling approach. © 2010 American Institute of Chemical Engineers AIChE J, 2011Keywords
This publication has 45 references indexed in Scilit:
- High-resolution Eulerian simulation of RMS of solid volume fraction fluctuation and particle clustering characteristics in a CFB riserChemical Engineering Science, 2008
- The prediction of particle cluster properties in the near wall region of a vertical riser (200157)Powder Technology, 2002
- The role of meso-scale structures in rapid gas–solid flowsJournal of Fluid Mechanics, 2001
- Parametric effects of particle size and gas velocity on cluster characteristics in fast fluidized bedsPowder Technology, 2000
- Riser hydrodynamics: Simulation using kinetic theoryAIChE Journal, 2000
- Hydrodynamic modeling of gas/particle flows in riser reactorsAIChE Journal, 1996
- MFIX documentation theory guide1993
- GAS/SOLIDS FLOW PATTERNS IN A 30.5-CM-DIAMETER CIRCULATING FLUIDIZED BED1988
- Flow characterization in high-velocity fluidized beds using pressure fluctuationsChemical Engineering Science, 1988
- RADIAL VARIATION IN SOLID DENSITY IN HIGH VELOCITY FLUIDIZATION1986