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Mass transfer between two phases was studied in an agitated vessel with a flat liquid-liquid interface for 30 systems, where physical properties varied in a wide range. The observed Sherwood numbers for the first-phase Sh1 were correlated in terms of the first-phase Reynolds number Re1, modified second-phase Reynolds number Re2'', Schmidt number Sc1, Capillary number Ca1 and a function of viscosity ratio Φ. The correlation obtained represents all the data with an average deviation of 12.7%: Sh1 = O.O119Sc11/3Ca16/13[Φ4Re13+Re2''8/3]1/4

Liquid-liquid mass transfer in an agitated vessel with a flat interface.