In the absence of halide ion, Hg2+ is the predominant species in water and can be effectively extracted using oleic acid. The organic phase complex that is formed is HgRi2(RH). The presence of polar modifiers in the organic phase facilitates the formation of a complex dimer, [HgR2'2(RH)12. Kinetics of the extraction reaction have been studied as a function of pH, Hg2+ concentration, oleic acid concentration, and mixing rate in a stirred cell reactor. Extraction kinetics are first order in mercury concentration and zero order with respect to oleic acid concentration and pH. This is consistent with f i l m theory predictions for an instantaneous reaction that is mass transfer controlled. A diffusion/ reaction model for mercury extraction in a batch stirred tank reactor has been developed that incorporates this information, and includes mass transfer of mercuric ion from the bulk solution to the droplet surface, equilibrium between aqueous mercury and organic mercury complex at the droplet interface, and diffusion and dimer formation of the complex within the organic phase droplet. Without the use of adjustable parameters, this model successfully predicts mercury extraction rate and equilibrium.