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dc.contributor.authorMoon, G.
dc.contributor.authorYoo, Kyoungkeun
dc.date.accessioned2017-06-23T02:59:04Z
dc.date.available2017-06-23T02:59:04Z
dc.date.created2017-06-19T03:39:42Z
dc.date.issued2017
dc.identifier.citationMoon, G. and Yoo, K. 2017. Separation of Cu, Sn, Pb from photovoltaic ribbon by hydrochloric acid leaching with stannic ion followed by solvent extraction. Hydrometallurgy. 171: pp. 123-127.
dc.identifier.urihttp://hdl.handle.net/20.500.11937/53213
dc.identifier.doi10.1016/j.hydromet.2017.05.003
dc.description.abstract

A recycling process consisting of HCl leaching with Sn4 + followed by solvent extraction is proposed to recover Cu, Sn and Pb from photovoltaic (PV) ribbon. During HCl leaching with Sn4 +, Sn and Pb were removed from PV ribbon whereas Cu remained as plate. The leaching efficiency of Sn increased with increasing temperature, initial Sn4 + concentration or decreasing pulp density. In the case of leaching test performed in the 1 M HCl solution at 400 rpm and 70 °C with 5% pulp density and 5000 mg/L Sn4 +, the leaching efficiency of Sn increased to > 99% within 60 min, whereas 71.9% of Pb was recovered as PbCl2 powder after settling the leach solution for 24 h at room temperature. A solvent extraction with tri-butyl phosphate (TBP) was performed to extract selectively Sn from leach solution. The extraction efficiency of Sn increased with increasing the contents of TBP in kerosene, and < 1% of Pb was extracted. Therefore, the separation of Sn, Cu, Pb was achieved successfully by the recycling process.

dc.publisherElsevier
dc.titleSeparation of Cu, Sn, Pb from photovoltaic ribbon by hydrochloric acid leaching with stannic ion followed by solvent extraction
dc.typeJournal Article
dcterms.source.volume171
dcterms.source.startPage123
dcterms.source.endPage127
dcterms.source.issn0304-386X
dcterms.source.titleHydrometallurgy
curtin.departmentDept of Mining Eng & Metallurgical Eng
curtin.accessStatusFulltext not available


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