dc.creatorValdivia Hepp, Juan
dc.creatorRogan Castillo, José
dc.creatorMuñoz Gálvez, Víctor
dc.creatorGomberoff, L.
dc.creatorKlimas, A.
dc.creatorVassiliadis, D.
dc.creatorUritsky, V.
dc.creatorSharma, S.
dc.creatorToledo Cabrera, Benjamín
dc.creatorWastavino, L.
dc.date.accessioned2007-05-17T18:41:45Z
dc.date.available2007-05-17T18:41:45Z
dc.date.created2007-05-17T18:41:45Z
dc.date.issued2005-11
dc.identifierMINERALS ENGINEERING
dc.identifier0892-6875
dc.identifierhttps://repositorio.uchile.cl/handle/2250/118617
dc.description.abstractCopper was removed from an acidic mine drainage (AMD) using a liquid emulsion membrane contactor. The acidic drainage was a harmful natural acidic solution generated by bioleaching and chemical leaching of copper and iron sulfides, with average pH between 2 and 4. Normally the content of copper in AMD is low, which makes its recovery by SX uneconomical. The kinetics of copper removal in a stirred transfer cell was studied, using a salicylaldoxime as mobile carrier extractant and Span-80 as surfactant. It was found that the initial extraction rate of copper was affected by the carrier concentration in the liquid membrane and by the pH and metal content in the mine water. A minimum content of surfactant in the organic phase was required to stabilize the emulsion. A transport mechanism based on a diffusion model, which includes the extraction chemical reaction between the metal and the carrier extractant is discussed.
dc.languageen
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD
dc.subjectSURFACTANT MEMBRANES
dc.titleKinetics of copper removal from acidic mine drainage by a liquid emulsion membrane
dc.typeArtículo de revista


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