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Mass Transfer Studies on Hydrocarbon Permeation Through Liquid Surfactant Membrane
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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.
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