BUBBLE DYNAMICS AND ELUTRIATION STUDIES IN GAS-FLUID1ZED BEDS
- 1 August 1984
- journal article
- research article
- Published by Taylor & Francis in Chemical Engineering Communications
- Vol. 29 (1-6) , 35-61
- https://doi.org/10.1080/00986448408940148
Abstract
In order to adequately interpret the heat and mass transfer data taken in a gas-fluidized bed, it is essential to know the bubble dynamics and solids movement in the bed, and solids elutriation from the bed. To generate information on these aspects, an experimental facility has been designed, fabricated and successfully tested. This consists of a two-dimensional fluidized bed with its gas supply and cleanup system. The bubble dynamics and solids projection from the bed are recorded by a high-speed movie camera. The films are analyzed on a photo-optical data analyser and digitizer provided with an electronic graphics calculator connected to tape printer and a Teletype terminal interfaced with a computer. The analysis of recorded bed dynamics suggests that for large particles the bubbles grow to be non-spherical and these rise almost above the bed surface before bursting when the wake remains intact while the solids bulge at the bubble nose ruptures to release the bubble gas. It is concluded unambiguously that the solids projected in the freeboard originate from the bubble bulge, and not from the bubble wake as commonly believed. A series of experiments is proposed which will facilitate the development of a general quantitative theory for solids elutriation from industrial fluidized beds. In addition, a fairly complete review of the work done on bubble dynamics, solids movement in the bed, and solids projection from the bed surface in two- and three-dimensional fluidized beds is presented. Thus, on the whole the present work reviews the state-of-the-art of these three different fluid-bed aspects, and reports new data.Keywords
This publication has 39 references indexed in Scilit:
- THE EFFECT OF TEMPERATURE ON FLUIDIZED BED BEHAVIOURChemical Engineering Communications, 1982
- The effect of operating temperature on the velocity of minimum fluidization, bed voidage and general behaviourPowder Technology, 1982
- The effect of temperature upon minimum fluidization velocityPowder Technology, 1977
- Bubble sizes in a fluidized bed at elevated temperaturesChemical Engineering Science, 1976
- Particle ejection and entrainment from fluidised bedsPowder Technology, 1972
- The gas fluidisation of large particlesThe Chemical Engineering Journal, 1972
- On the mechanics of fluidized particle movementThe Chemical Engineering Journal, 1972
- The size and frequency of bubbles in two- and three-dimensional gas-fluidised bedsPowder Technology, 1970
- The behaviour of freely bubbling fluidised bedsChemical Engineering Science, 1969
- Flow patterns near a solid obstacle in a fluidized bedChemical Engineering Science, 1964