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6. Performance Characteristics o f F e r m e n t e r s Containing Microbial Flocs . . . . . . 1 Mass Transfer between Fluid and Flocs . . . . . . . . . . . . . . 2 Batch Fermenters . . . . . . . . . . . . . . . . . . . . 3 C o n t i n u o u s Fermenters . . . . . . . . . . . . . . . . . . 7. Process Applications . . . . . . . . . . . . . . . . . . . . . 1 Reaction Processes . . . . . . .
1944) for sulfite oxidation with a vaned-disk agitator. It is also less than the value of unity obtained for sulfite oxidation with flat paddle agitators (Friedman and Lightfoot, 1957). In order to obtain more general correlations between mass transfer and the design and operation variables, kL should be separated from the interfacial area per unit volume, a, because kL and a are each influenced by different factors. Calderbank et aI. tL )2/3 = 0 . 13[(Pg/V)PL]I/4 PLDL P2 (65) where Pg = power consumption accompanied by aeration, kg mZ/hr 3.
Birukov, V. : Proceedings of the 4th International Fermentation Symposium, Page 105, Kyoto (1972). Calderbank, P. : Trans, Inst. Chem. Engrs. 36,443 (1958). Calderbank, P. : Trans. Inst. Chem. Engrs. 37, 173 (1959b). Calderbank, P. , Moo-Young, M. : Trans. Inst. Chem. Engrs. 37, 26 (1959a). Calderbank, P. , Moo-Young, M. : Chem. Eng. Sci. 16, 39 (1961). Cooper, C. , Fernstrom, G. , Miller, S. : Ind. Eng. Chem. 36, 504 (1944). Friedman, A. , Lightfoot, E. : Ind. Eng. Chem. 49, 1227 (1957). : J.