Porosity distributions in a fluidized bed with an immersed obstacle
- 1 June 1989
- journal article
- research article
- Published by Wiley in AIChE Journal
- Vol. 35 (6), 908-922
- https://doi.org/10.1002/aic.690350604
Abstract
Erosion in bubbling fluidized-bed combustors is a serious issue that may affect their reliability and economics. Available evidence suggests that the key to understanding this erosion is detailed knowledge of the coupled and complex phenomena of solids circulation and bubble motion. A thin transparent “two-dimensional” rectangular fluidized bed with an obstacle served as a rough model for a fluidized-bed combustor. This model was studied experimentally and computationally using two hydrodynamic equation sets. The computed hydrodynamic results agree reasonably well with experimental data. Bubble frequencies and sizes compare well with those obtained from analyzing a high-speed motion picture frame-by-frame. Time-averaged porosities computed from both models agree with time-averaged porosity distributions measured with a gamma-ray densitometer. The principal diferences between the data and the computations in this paper are due to asymmetries present in the experiment and to the simplified solids rheology used in the hydrodynamic models.Keywords
This publication has 22 references indexed in Scilit:
- A modification of the Kynch theory of sedimentationAIChE Journal, 1987
- Hydrodynamics of fluidization in a semicircular bed with a jetAIChE Journal, 1984
- Effects of pressure and type of gas on particle-particle interaction and the consequences for gas—solid fluidization behaviourPowder Technology, 1984
- Fluidization in two-dimensional beds with a jet. 2. Hydrodynamic modelingIndustrial & Engineering Chemistry Fundamentals, 1983
- Mechanisms for solids ejection from gas‐fluidized bedsAIChE Journal, 1983
- Fluidization in two-dimensional beds with a jet. 1. Experimental porosity distributionsIndustrial & Engineering Chemistry Fundamentals, 1983
- On the formation of bubbles in gas-particulate fluidized bedsJournal of Fluid Mechanics, 1979
- Particle and bubble behaviour and velocities in a large-particle fluidized bed with immersed obstaclesPowder Technology, 1979
- Theory of yield of cohesive powdersPowder Technology, 1975
- Vertical pneumatic conveying: A theoretical study of uniform and annular particle flow modelsThe Canadian Journal of Chemical Engineering, 1973