NOTATION a quantity, detìned in Eq. (3) B quantity, defined in Eq. (3) C, concentration of the tracer in the mobile tluid Cz concentration of the tracer in the stagnant zones D coefficient of axial dispersion E quantity, defined in Eqs. (8-11) f(x) arbitrary function F quantity, defined in Eqs. (8-1
Dispersion of gas in the track of tracer bubbles injected into a two-dimensional fluidised bed
β Scribed by T.J. Evans; P.N. Rowe
- Publisher
- Elsevier Science
- Year
- 1974
- Tongue
- English
- Weight
- 177 KB
- Volume
- 29
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
The rising velocity of an isolated bubble in a "two-dimensional" air-fluidised bed has been measured and found to be wel1 described by the relation, ub= 15'9Abf cm/sec, where Ab is the area of the bubble measured in cm\*. This predicts a smaller rising velocity than the corresponding @avies and Tayl
Based on the observed pattern of coalescence of bubble pairs in vertical alignment in a two-dimensional bed, a theory is developed which describes how bubble size and frequency changes with height in a gas fluidised bed. It is confirmed by comparison with the reported data from 10 separate investiga
An improved electroresistivity probe has been used in a freely bubbling gas-fluidised bed of carbon particles to give the distributions of velocitj and size of bubbles therein. Bubble properties agree with previous observations but the significant influence of macro-circulation patterns on bubble ve