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Authors
Affiliations
1 Department of Food Technology and Biochemical Engineering, Jadavpur University, Calcutta 700032, IN
2 Department of Chemical Engineering, Judavpur University, Calcutta 700032, IN
Source
Journal of Surface Science and Technology, Vol 10, No 1-4 (1994), Pagination: 89-98
Abstract
Hydrodynamic characteristics of a liquid membrane permeation system for separation of toluene from a mixture of heptane and toluene were studied. The mass transfer coefficient was well correlated in terms of three dimensionless numbers: Sherwood, Schmidt and Reynolds. By using the correlation equation, a correction factor with respect to intrinsic permeation rate was evaluated from the experimental data under various non-ideal flow conditions.
Keywords
Liquid Surfactant Membrane, Hydrocarbon, Mass Transfer Coefficient, Intrinsic Permeation Rate.
