Estimation of bed expansions in a freely-bubbling three-dimensional gas-fluidized bed
โ Scribed by A. Hepbasli
- Publisher
- John Wiley and Sons
- Year
- 1998
- Tongue
- English
- Weight
- 178 KB
- Volume
- 22
- Category
- Article
- ISSN
- 0363-907X
No coin nor oath required. For personal study only.
โฆ Synopsis
Knowledge of bed expansions is important in the design and operation of gas-solid fluidized beds. This paper presents a study on the estimation of expanded bed height in a large three-dimensional gas-fluidized bed with a square section of 0)61;0)61 m. All experiments were performed at the freely bubbling mode and the bed expansions were recorded by a video camera. Bed materials were used 593 m raw perlite and 1233 m sand falling within the categories of Geldart's Groups B and D, respectively. The bed height at minimum fluidization ranged from 0)0398 to 0)3176 m, while the excess air velocity from 0)034 m s\ to 0)7453 m s. Equations related to the bed expansion were given using a modified form of two-phase theory of fluidization. A correlation for the average bed expansion (void fraction) was also presented that has been derived from the principal form found successful in gas-liquid systems as follows:
with an average deviation of less than 1%. The experimental findings were compared with previously reported results and were discussed in the light of available correlations.
๐ SIMILAR VOLUMES
Gas fluidization is generally associated with the formation of bubbles that critically influence the performance of fluidized bed processes (FBPs). Therefore, in the design, simulation and operation of FBPs, it is very essential to know the behaviour of the bubbles at the free surface. The size and
Bagasse, a by-product of sugar cane processing and an important potential energy resource, could be used as a fuel in fluidized bed combustors for energy generation. Bagasse can not be fluidized alone because of its nature, which has many fibrous, low density and high moisture content. These propert