The recovery of copper from a pregnant sulphuric acid bioleach solution with developmental resin Dow XUS43605

dc.contributor.authorLiebenberg, C. J.en_ZA
dc.contributor.authorDorfling, C.en_ZA
dc.contributor.authorBradshaw, S. M.en_ZA
dc.contributor.authorAkdogan, G. A.en_ZA
dc.contributor.authorEksteen, J. J.en_ZA
dc.date.accessioned2014-07-07T12:35:10Z
dc.date.available2014-07-07T12:35:10Z
dc.date.issued2013-04
dc.descriptionCITATION: Liebenberg, C. J. et al. 2013. The recovery of copper from a pregnant sulphuric acid bioleach solution with developmental resin Dow XUS43605. Journal of the Southern African Institute of Mining and Metallurgy, 113(5):389-397.
dc.descriptionThe original publication is available at https://www.saimm.co.za
dc.description.abstractENGLISH ABSTRACT: This paper focuses on the application of ion exchange technology for the recovery of copper from a leach solution originating from a heap bioleach in which base metals are leached from a low-grade ore that bears platinum group metals. Screening tests indicated that Dow XUS43605 has high selectivity for copper over the other metals in the solution, namely nickel, iron, cobalt, zinc, manganese, and aluminium. Batch adsorption kinetic experiments showed that copper adsorption equilibrium is attained at a fast rate. The kinetics of adsorption increased as the temperature was increased from 25°C to 60°C due to the decrease in solution viscosity and the subsequent improved intra-particle mass diffusion. Single-component Langmuir and Freundlich isotherm models were fitted to the batch copper adsorption equilibrium data, and a maximum copper capacity of 26 g/l was observed for Dow XUS43605. The effects of flow rate, temperature, pH, and initial metal concentration on the dynamic recovery of copper were investigated in fixed-bed columns, and it was determined that temperature and flow rate had the most significant impacts on the loading of copper on the resin at copper breakthrough. A 36% increase in copper loading at breakthrough was observed when the temperature was increased from 25°C to 60°C. Finally, it was determined that a split elution is possible by using different concentrations of H2SO4 to first elute co-loaded nickel from the resin, followed by the elution of copper.en_ZA
dc.description.versionPublisher's version
dc.format.extent9 pages : illustrationsen_ZA
dc.identifier.citationLiebenberg, C. J. et al. 2013. The recovery of copper from a pregnant sulphuric acid bioleach solution with developmental resin Dow XUS43605. Journal of the Southern African Institute of Mining and Metallurgy, 113(5):389-397.
dc.identifier.issn2411-9717 (online)
dc.identifier.issn2225-6253 (print)
dc.identifier.urihttp://hdl.handle.net/10019.1/95211
dc.language.isoen_ZAen_ZA
dc.publisherSouthern African Institute of Mining and Metallurgyen_ZA
dc.rights.holderAuthors retain copyrighten_ZA
dc.subjectSulfuric aciden_ZA
dc.subjectSolution miningen_ZA
dc.subjectTransition metalsen_ZA
dc.subjectIon exchangeen_ZA
dc.subjectHydrometallurgyen_ZA
dc.titleThe recovery of copper from a pregnant sulphuric acid bioleach solution with developmental resin Dow XUS43605en_ZA
dc.typeArticle
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