Pilot scale production of yellowcake from the Kintyre uranium deposit using a direct precipitation process

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dc.contributor.authorMachaughton, SJen_AU
dc.contributor.authorCollier, DEen_AU
dc.contributor.authorTapsell, GJen_AU
dc.contributor.authorRing, RJen_AU
dc.contributor.authorHawley, Ben_AU
dc.contributor.authorBellingham, Aen_AU
dc.date.accessioned2024-04-08T02:45:41Zen_AU
dc.date.available2024-04-08T02:45:41Zen_AU
dc.date.issued1998-09-28en_AU
dc.date.statistics2024-04-04en_AU
dc.descriptionPhysical copy held at DDC: 660.20994/13en_AU
dc.description.abstractKintyre is a high grade uranium deposit located in the north west of Western Australia 90 km south of Telfer. Two bulk samples of upgraded ore from the deposit were processed in a pilot plant to produce a saleable uranium oxide concentrate. The pilot plant was operated continuously for 42 days at a throughput of 15 kg h-1. This paper describes the direct precipitation processing route that was employed and the performance of the plant under a range of operating conditions. Ground ore was leached at 56% solids using sulphuric acid and hydrogen peroxide as an oxidant. The leach liquor was recovered using a high rate thickener followed by belt filtration. The resulting leach liquor had a tenor of 6 to 8 g L-1 U3O8 and was treated with hydrogen peroxide to oxidise any ferrous iron to the ferric state. The ferric iron was then removed by precipitation with lime. The iron precipitate was leached with sulphuric acid to recover uranium before disposal with the primary leach tailings. Yellowcake was precipitated from the clarified iron-free liquor using hydrogen peroxide and sodium hydroxide for pH control. The simplicity of the circuit – a leaching stage followed by two precipitation stages – is in marked contrast to conventional uranium circuits which utilise solvent extraction or ion exchange to recover uranium from leach liquors. Operation of the pilot plant successfully demonstrated the technical feasibility of the direct precipitation processing route. In both precipitation circuits the overall efficiency was found to be dependent on the distribution of reagents within each circuit. Optimisation of these variables resulted in high precipitation efficiencies (>99.9%). The design criteria that were established in the pilot plant were generally more favourable than predictions based on laboratory testwork.en_AU
dc.identifier.booktitleChemeca 98 Proceedings, Port Douglas, 28-30 September 1998en_AU
dc.identifier.citationMacnaughton, S. J., Collier, D., Tapsell, G., Ring, R. J., Hawley, B., & Bellingham. A. (1998). Pilot scale production of yellowcake from the Kintyre uranium deposit using a direct precipitation process. Paper presented to Chemeca 98 : creating competetive resources : the 26th Australasian Chemical Engineering conference, Port Douglas, Queensland, Australia, 28-30 September 1998. In Chemeca 98 Proceedings, Port Douglas, 28-30 September 1998.en_AU
dc.identifier.conferenceenddate1998-09-30en_AU
dc.identifier.conferencenameChemeca 98 : creating competetive resources : the 26th Australasian Chemical Engineering conferenceen_AU
dc.identifier.conferenceplacePort Douglas, Queenslanden_AU
dc.identifier.conferencestartdate1998-09-28en_AU
dc.identifier.issn1858256835en_AU
dc.identifier.urihttps://apo.ansto.gov.au/handle/10238/15551en_AU
dc.language.isoenen_AU
dc.publisherInstitution of Engineers Australiaen_AU
dc.subjectUraniumen_AU
dc.subjectDepositsen_AU
dc.subjectWestern Australiaen_AU
dc.subjectAustraliaen_AU
dc.subjectPrecipitationen_AU
dc.subjectPilot plantsen_AU
dc.subjectOresen_AU
dc.subjectHydrogen peroxideen_AU
dc.subjectLeachingen_AU
dc.titlePilot scale production of yellowcake from the Kintyre uranium deposit using a direct precipitation processen_AU
dc.typeConference Paperen_AU
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