A model for describing mass transfer in three-uhase fluid&d beds has been develoDed and tested using experimental data. The presence of two distinct mass transfer zones led to the idea o> interfacing a plug flow model (PFM) with an axial dispersion model (ADM) at the separation boundary between thes
Three-phase mass transfer: Improved pseudo-homogeneous model
β Scribed by Endre Nagy; Anton Moser
- Publisher
- American Institute of Chemical Engineers
- Year
- 1995
- Tongue
- English
- Weight
- 915 KB
- Volume
- 41
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
Abstraet--A new one-dimensional heterogeneous model has been developed to describe the mass transfer rate for a three-phase system which contains larger particles, i.e. particles larger than or in the same order of magnitude as the gas-liquid boundary layer. The diffusion of the absorbed component i
In Part I a two-scale thermomechanical theory of expansive compacted clays composed of adsorbed water and clay platelets was derived using a mixture-theoretic approach and the Coleman and Noll method of exploitation of the entropy inequality. This approach led to a two-scale model which describes th
## Abstract The mass transfer rates of a gaseous reactant into a liquid where the reactions are catalyzed by homogeneous catalysts have been evaluated by the numerical solution of the diffusionβreaction equations according to Higbie's penetration theory. The concentration profiles as well as enhanc