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Mass transfer in a stirred vessel extractor

✍ Scribed by M.J. Loosemore; A.P. Prosser


Publisher
Elsevier Science
Year
1963
Tongue
English
Weight
212 KB
Volume
18
Category
Article
ISSN
0009-2509

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πŸ“œ SIMILAR VOLUMES


A hydrodynamic model of mass transfer in
✍ D.R. Olander πŸ“‚ Article πŸ“… 1963 πŸ› Elsevier Science 🌐 English βš– 925 KB

The flow patterns generated by the rotation of stirrer bars in the two immiscible liquids in a stirred vessel extractor have been approximated by a simpliΓ­Γ¬ed model. Each phase was divided into two regions: the core region, whΓ­ch is the cylindrical volume swept out by the sthrer bars, and the outer

Mass transfer in stirred vessels
✍ R. B. Olney πŸ“‚ Article πŸ“… 1961 πŸ› American Institute of Chemical Engineers 🌐 English βš– 198 KB πŸ‘ 2 views
A modified model of stirred vessel mass
✍ D.R. Olander πŸ“‚ Article πŸ“… 1964 πŸ› Elsevier Science 🌐 English βš– 695 KB

The model of stirred vessel mass transfer previously presented [1] has been amended to account for transfer in the core region. In addition to the two-region picture, a modified single region model, in which the return flow to the interface occurs in a region close to the vessel wall, is also descri

Initial response analysis of mass transf
✍ L.G. Gibilaro; S.N. Davies; M. Cooke; P.M. Lynch; J.C. Middleton πŸ“‚ Article πŸ“… 1985 πŸ› Elsevier Science 🌐 English βš– 549 KB

A method for evaluating the mass transfer coefficient, kLa, in a gas sparged stirred vessel from the initial portion of the liquid dynamic response curve is described. The method assumes perfect liquid mixing but is independent of the gas mixing characteristics. Results obtained from two geometrica

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✍ Dipl.-Ing. Franz Otillinger; Prof. Dr.-Ing. Eckhart Blass πŸ“‚ Article πŸ“… 1988 πŸ› John Wiley and Sons 🌐 English βš– 809 KB