dc.creatorValenzuela, F. J.
dc.creatorCabrera, J.
dc.creatorBasualto, C.
dc.creatorSapag, J.
dc.creatorRomero, J.
dc.creatorSánchez, J.
dc.creatorRios, G.
dc.date.accessioned2018-12-20T15:09:58Z
dc.date.available2018-12-20T15:09:58Z
dc.date.created2018-12-20T15:09:58Z
dc.date.issued2007
dc.identifierSeparation Science and Technology, Volumen 42, Issue 2, 2018, Pages 363-377
dc.identifier01496395
dc.identifier15205754
dc.identifier10.1080/01496390601069887
dc.identifierhttps://repositorio.uchile.cl/handle/2250/158085
dc.description.abstractThis is a report on the separation and recovery of zinc ions from an acidic mine drainage using a stirred transfer cell-type emulsion liquid membrane contactor. Di(2-ethylhexyl) phosphoric acid was used as a highly selective carrier for the transport of zinc ions through the emulsified liquid membrane. A study was made of the effect on the extraction extent and initial extraction rate of the following variables: pH and initial metal concentration of the feed phase, carrier content in the organic solution, a stripping agent concentration in the receiving phase, and stirring speed in the transfer cell. The content of sulfuric acid as a stripping agent did not show in the studied range any significant influence on metal permeation through the SLM, although a minimum hydrogen ion concentration of 100 g/L is suggested in the internal aqueous solution to ensure an acidity gradient between both aqueous phases to promote the permeation of metal ions toward the strip liquor. Results show that u
dc.languageen
dc.rightshttp://creativecommons.org/licenses/by-nc-nd/3.0/cl/
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Chile
dc.sourceSeparation Science and Technology
dc.subjectAcid drainage
dc.subjectLiquid membrane
dc.subjectSeparation
dc.subjectZinc
dc.titleSeparation of zinc ions from an acidic mine drainage using a stirred transfer cell-type emulsion liquid membrane contactor
dc.typeArtículo de revista


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