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dc.contributor.authorDorfling, C.
dc.contributor.authorAkdogan, G.
dc.contributor.authorBradshaw, S
dc.contributor.authorEksteen, Jacques
dc.contributor.editorNew Concept Information Systems Pvt Ltd
dc.date.accessioned2017-01-30T15:06:40Z
dc.date.available2017-01-30T15:06:40Z
dc.date.created2014-03-23T20:00:53Z
dc.date.issued2012
dc.identifier.citationDorfling, C. and Akdogan, G. and Bradshaw, S.M. and Eksteen, J.J. 2012. Kinetics of RH, RU, and IR dissolution during the Sulphuric Acid Pressure Leaching of First Stage Leach Residue, in Proceedings of the 26th International Mineral Processing Congress, IMPC 2012, Sep 23-28 2012, pp. 1196-1210. New Delhi, India: New Concept Information Systems.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/43326
dc.description.abstract

Experimental work was performed using a bench scale autoclave to evaluate the effects that leaching temperature, pressure, initial acid concentration, and the solid to liquid ratio have on the behaviour of base metals and platinum group metals in a high-pressure sulphuric acid oxygen leaching system. The concentrations of metals in the leach solution were measured over time at different leaching conditions. At the conditions investigated, the initial acid concentration had the largest influence on the copper leaching kinetics, while the leaching rates of the other precious metals (OPMs: rhodium, ruthenium, and iridium) were highly dependent on the leaching temperature. A set of chemical reactions that can be used to describe the leaching chemistry was proposed, and the associated reaction kinetics were quantified. As a first estimation, the rate expressions were considered first order, and the rate constants were determined using the method of least squares, considering the experimental and predicted concentrations obtained for the different leaching conditions. Of the OPM compounds, the sulphides showed the fastest dissolution rate, followed by OPM alloys, and finally the OPM oxides. During the initial leaching stages, base metals and OPMs competed for the available dissolved oxygen, with oxygen being preferentially used for copper leaching. Precipitation of OPMs during the initial leaching stages can be ascribed to copper and nickel dissolution according to exchange reactions between dissolved OPMs and copper present as digenite or nickel present as polydymite. Control of the autoclave residence time is of particular importance to enhance the selectivity of this leaching step, given the dependence of the PGM leaching rates on the extent of copper dissolution.

dc.publisherNew Concept Information Systems Pvt Ltd.
dc.subjectPlatinum group metals
dc.subjectPressure leaching
dc.subjectNickel-copper matte
dc.titleKinetics of RH, RU, and IR dissolution during the Sulphuric Acid Pressure Leaching of First Stage Leach Residue
dc.typeConference Paper
dcterms.source.startPage1196
dcterms.source.endPage1210
dcterms.source.titleInnovative Processing for Sustainable Growth - Conference Proceedings
dcterms.source.seriesInnovative Processing for Sustainable Growth - Conference Proceedings
dcterms.source.isbn8190171437
dcterms.source.conference26th International Mineral Processing Congress, IMPC 2012: Code 97654
dcterms.source.conference-start-dateSep 24 2012
dcterms.source.conferencelocationNew Delhi, India
dcterms.source.placeNew Delhi, India
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curtin.accessStatusFulltext not available


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