1997
DOI: 10.1016/s0304-386x(97)00032-7
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A case of ferrous sulfate addition enhancing chalcopyrite leaching

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Cited by 105 publications
(45 citation statements)
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“…The final copper recoveries were 21.9%, 39.6%, 44.6% and 46.2% for control test, ferric added medium, ferrous added medium and the medium with the initial redox potential of 420 mV, respectively. This result is in agreement with those obtained by Hiroyoshi et al [2] and Third et al [6] who reported that ferrous iron is more effective than ferric iron to dissolve chalcopyrite. Higher copper extraction rate in the first day of ferric added medium was related to the higher efficiency of chalcocite and covellite in ferric media.…”
Section: Effect Of Ferric and Ferrous Iron On Chemical Leachingsupporting
confidence: 83%
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“…The final copper recoveries were 21.9%, 39.6%, 44.6% and 46.2% for control test, ferric added medium, ferrous added medium and the medium with the initial redox potential of 420 mV, respectively. This result is in agreement with those obtained by Hiroyoshi et al [2] and Third et al [6] who reported that ferrous iron is more effective than ferric iron to dissolve chalcopyrite. Higher copper extraction rate in the first day of ferric added medium was related to the higher efficiency of chalcocite and covellite in ferric media.…”
Section: Effect Of Ferric and Ferrous Iron On Chemical Leachingsupporting
confidence: 83%
“…Third et al [6] also studied the effect of ferrous and ferric iron on the chemical and bacterial leaching of chalcopyrite at 37˚C and found that high ferric concentration inhibits the bioleaching of chalcopyrite. They also confirmed the results obtained by Hiroyoshi et al [2] and found that chemical leaching of chalcopyrite was increased 4-fold in the presence of 0.1 M ferrous iron compared with 0.1 M ferric iron. Cordoba et al [8] studied the influence of ferric iron on chalcopyrite dissolution at low and high solution potentials and found that although ferric iron was responsible for the oxidation of chalcopyrite, ferrous iron had an important role in controlling the precipitation and nucleation of jarosite (Equation (2)).…”
Section: Introductionsupporting
confidence: 81%
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“…Four candidates are most often proposed: metal deficient sulphides, elemental sulphur, polysulphides and jarosites (Cordoba et al, 2008a;Klauber, 2008;Rodriguez et al, 2003). From a process point of view, many authors agree on the fact that the dissolution rate of chalcopyrite is higher at redox potential of leach solution below a critical value (Hiroyoshi et al 1997(Hiroyoshi et al , 2000(Hiroyoshi et al , 2001. Tshilombo et al (2002) demonstrate that passivation of chalcopyrite occurs at low temperature within the potential range 450 -600 mV (vs. Ag/AgCl); Pinches et al (2000) advise potential between 380 mV and 480 mV and Cordoba et al (2008b) indicate a critical redox potential value of 413 mV above which chalcopyrite dissolution slows down.…”
Section: Discussionmentioning
confidence: 99%