dc.creatorValdés, H.
dc.creatorRomero, J.
dc.creatorSanchez, J.
dc.creatorBocquet, S.
dc.creatorRios, G. M.
dc.creatorValenzuela, F. J.
dc.date.accessioned2018-12-20T15:10:07Z
dc.date.available2018-12-20T15:10:07Z
dc.date.created2018-12-20T15:10:07Z
dc.date.issued2009
dc.identifierChemical Engineering Journal, Volumen 151, Issue 1-3, 2018, Pages 333-341
dc.identifier13858947
dc.identifier10.1016/j.cej.2009.04.012
dc.identifierhttps://repositorio.uchile.cl/handle/2250/158147
dc.description.abstractThis study aims to describe the mass transfer in a membrane-based solvent extraction system for the extraction of molybdenum(VI) from aqueous solutions, identifying chemical kinetics of the complex formation at the interface. The analyzed process is the membrane-based solvent extraction of molybdenum(VI) from aqueous solutions with n-hexane containing Alamine 336 as extraction phase using a hollow fiber contactor. This extraction process has been described through a resistances-in-series model, taking into account transport and thermodynamic relationships. In this work, the model has been used to identify an effective reaction rate expression and to describe the mass transfer by complex formation at the interface. The reaction rate expression has been estimated from experimental data obtained in a previous work [F. Valenzuela, H. Aravena, C. Basualto, J. Sapag, C. Tapia, Separation of Cu2+ and molybdenum(VI) from mine waters using two microporous extraction systems, Separation Science
dc.languageen
dc.rightshttp://creativecommons.org/licenses/by-nc-nd/3.0/cl/
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Chile
dc.sourceChemical Engineering Journal
dc.subjectLiquid-liquid extraction
dc.subjectMass transfer
dc.subjectMembrane contactor
dc.subjectModelling
dc.subjectMolybdenum
dc.titleCharacterization of chemical kinetics in membrane-based liquid-liquid extraction of molybdenum(VI) from aqueous solutions
dc.typeArtículo de revista


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