Liquid phase mass transfer coefficients for fihns in wave motion are considerably larger than predicted by previous theory. The increase in interfacial area due to waves cannot explain the discrepancy satisfactorily. A model for the absorption process has been proposed which takes into account eddie
Mass transfer to falling liquid films at low reynolds numbers
β Scribed by E. Ruckenstein; C. Berbente
- Publisher
- Elsevier Science
- Year
- 1968
- Tongue
- English
- Weight
- 835 KB
- Volume
- 11
- Category
- Article
- ISSN
- 0017-9310
No coin nor oath required. For personal study only.
π SIMILAR VOLUMES
The mass transfer data measured m the hqmd flmd& beds of ion exchange resms m the Reynolds number range 0 22-6 4 are presented A comparison was made between the experunental results and the values predlcted by the recent theory of Nelson and Galloway and by the moddied theory proposed by Rowe The ob
Mass transfer coefficients for packed beds of Raschii rings were measured by the electrochemical technique in the low Reynolds number range, where both, free and forced convection are important. From the analysis of the governing basic equations the parameters controlling the combined Bee and force
A low-speed water-tunnel is described to enable dissolution rates of pelleted organic acid spheres to be measured. Results are obtained for the overall aud local mass-transfer rates from 2 in. diameter benzoic acid spheres to water at 3O.O"C between Reynolds numbers of 2.3 and 255. Comparison with s