Abstract
Abstract A model for copper permeation through liquid surfactant membranes in a continuously stirred vessel is presented in which mass transfer resistances both in and around W/O emulsion drops, interfacial reactions at aqueous-organic interfaces, and the residence time distribution of the W/O emulsion drops in the extraction vessel are taken into account. Extraction of copper using SME529 as a carrier was carried out with a continuously stirred vessel. It is shown that the experimental data can be satisfactorily interpreted by the proposed model.
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