Mass transfer in the flow of gases through shallow fluidized beds
β Scribed by Poong Yoon; George Thodos
- Publisher
- Elsevier Science
- Year
- 1972
- Tongue
- English
- Weight
- 553 KB
- Volume
- 27
- Category
- Article
- ISSN
- 0009-2509
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β¦ Synopsis
Concentration profiles within a fluidized bed have been measured using a hydrocarbon analyzer and have been utilized to establish from them mass transfer coefficients and the correspondingj,-factor relationship, s,J, = 0*947/Re I'*, for 100 < Re < 450. The experimental approach involved the evaporation of n-decane from the surface of Celite particles, ranging from 0.1215 to O-0721 in. dia. In addition, a model is presented which is based on the variation with bed height of a*, the interfacial area. This model predicts concentration profiles and actual mass transfer coefficients for a fluidized bed system.
π SIMILAR VOLUMES
## Abstract An experimental investigation has been conducted on the direct establishment of mass transfer driving forces for the vaporization of __n__βdecane from Celite particles fluidized by air. Ranges of particle sizes and reactor diameters were employed. Concentration profiles of __n__βdecane
The volumetric gas-liquid mass transfer coefficient (KLa) and axial dispersion coefficient (Dz) of liquid phase have been studied in air-oxygen saturated water fluidized beds of 0.52 to 0.755 mm glass spheres in a plexiglass column. The effects of liquid velocity, gas velocity, particle size and loa