Mi. Bouaifi et M. Roustan, BUBBLE-SIZE AND MASS-TRANSFER COEFFICIENTS IN DUAL-IMPELLER AGITATED REACTORS, Canadian journal of chemical engineering, 76(3), 1998, pp. 390-397
The study relates to the mass transfer and the bubble size in a non st
andard vessel equipped with various dual-impeller combinations. The ef
fects of the rotational speed, gas flow rate, impeller type and diamet
er are investigated. The volumetric mass transfer coefficient k(L)a an
d the bubble size d(bs) were studied. The liquid side mass transfer co
efficient k(L) and the volumetric interfacial area a were estimated se
parately. A comparison has been made with some existing correlations.