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Extraction of copper from copper bearing sulfide ores (chalcopyrite) by oxidative chemical leaching

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dc.contributor.author Premaratne, W.A.P.J.
dc.contributor.author Dharmarathna, A.C.S.
dc.date.accessioned 2016-12-30T04:28:35Z
dc.date.available 2016-12-30T04:28:35Z
dc.date.issued 2016
dc.identifier.citation Premaratne, W.A.P.J. and Dharmarathna, A.C.S. 2016. Extraction of copper from copper bearing sulfide ores (chalcopyrite) by oxidative chemical leaching. In Proceedings of the International Research Symposium on Pure and Applied Sciences (IRSPAS 2016), Faculty of Science, University of Kelaniya, Sri Lanka. p 35. en_US
dc.identifier.isbn 978-955-704-008-0
dc.identifier.uri http://repository.kln.ac.lk/handle/123456789/15688
dc.description.abstract The extraction of copper from primary copper sulfide ores is much complicated and expensive. However, the successful metal extraction from natural mineral resources is very important, both environmentally and economically. The main objectives of this research work are to examine possible ways to increase the copper extraction from chalcopyrite (CuFeS2) using oxidative chemical leaching processes and to investigate oxidative leaching kinetics of chalcopyrite in sulfuric (H2SO4) acid medium. Chalcopyrite mineral sample was obtained from Geological Survey and Mines Bureau (GSMB) in Sri Lanka. Initial investigations characterized the chalcopyrite ore mineralogically and chemically. X-ray diffraction analysis of chalcopyrite ore reveled that only chalcopyrite (CuFeS2), azurite (Cu3(CO3)2(OH)2), pyrite (FeS2) and pyrrhotite (FeS) minerals were present. The copper content of the chalcopyrite ore sample was found to be 16.6% by weight according to the chemical analysis. The extraction of copper from chalcopyrite using hydrogen peroxide (H2O2), ferric sulphate (Fe2(SO4)3), potassium permanganate (KMnO4) and potassium dichromate (K2Cr2O7) oxidizing agents in acid solutions was studied using the 63-90 μm particle size fraction of chalcopyrite. The effect of temperature ranging from 30 ºC to 70 ºC, the effect of concentration of sulfuric acid ranging from 0.25 mol dm-3 to 5.0 mol dm-3 and the effect of pulp density ranging from 2% to 6% on the rate of dissolution of copper from chalcopyrite ore were also studied. The extraction rates are significantly influenced by the temperature and the concentration of the acid solutions. According to the oxidative chemical leaching results, the maximum extraction of copper was achieved with KMnO4 and then with K2Cr2O7, followed by H2O2 and Fe2(SO4)3. In this study maximum extraction of 70.2 % of copper was achieved at 0.1 mol dm-3 KMnO4 in 1.0 mol dm-3 H2SO4 acid. It was found that oxidizing agents improved the leaching kinetics of chalcopyrite in sulfuric acid medium saving both time and energy effectively and efficiently. A kinetic study showed that the dissolution of copper from chalcopyrite ore was controlled by chemical reaction process on the surface of particles. Based on the results obtained in this investigation, the apparent activation energy for the dissolution of copper using the Arrhenius expression was found to be 31.8 kJ mol-1. en_US
dc.language.iso en en_US
dc.publisher Faculty of Science, University of Kelaniya, Sri Lanka en_US
dc.subject Copper extraction en_US
dc.subject Chalcopyrite en_US
dc.subject Sulfuric acid en_US
dc.subject Oxidizing agents en_US
dc.subject Leaching kinetics en_US
dc.title Extraction of copper from copper bearing sulfide ores (chalcopyrite) by oxidative chemical leaching en_US
dc.type Article en_US


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