The Influence of pH and Ferrous Ions on Chalcopyrite Dissolution in Chemical Leaching Chalcopyrite

Article Preview

Abstract:

This paper studied the influence of pH, temperature and particle size on the chemical leaching of chalcopyrite. The results show that H+ is not only responsible for the hydrolysis and precipitation of ferric ion as jarosite, but also related directly to chalcopyrite dissolution. The mechanism of chalcopyrite leaching is as follows: the first stage is H+ attacking valence band and electron transition during oxidation, which needs a great deal of the energy to the system. The second stage is the transport of electrons from the chalcopyrite surface to the dissolved oxygen. However, the limiting step changes into diffusion control from chemical control when the elemental sulphur film formed, which obstructs transport of electrons.

You might also be interested in these eBooks

Info:

Periodical:

Advanced Materials Research (Volumes 962-965)

Pages:

822-828

Citation:

Online since:

June 2014

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2014 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] Dutrizac J E: Hydrometallurgy, Vol. 23 (1990) No. 2, pp.153-176.

Google Scholar

[2] Rawlings D E, Dew D, and Plessis C: Trends in Biotechnology, Vol. 21 (2003) No. 1, pp.38-44.

Google Scholar

[3] Hiroyoshi N, Hirota M, Hirajima T, and Tsunekawa M: Hydrometallurgy, Vol. 47 (1997) No. 1, pp.37-45.

DOI: 10.1016/s0304-386x(97)00032-7

Google Scholar

[4] Hiroyoshi N, Arai M, Miki H, Tsunekawa M, and Hirajima T: Hydrometallurgy, Vol. 63 (2002) No. 3, pp.257-267.

DOI: 10.1016/s0304-386x(01)00228-6

Google Scholar

[5] Hiroyoshi N, Kuroiwa S, Miki H, Tsunekawa M, and Hirajima T: Hydrometallurgy, Vol. 87 (2007) No. 1-2, pp.1-10.

Google Scholar

[6] Córdoba E M, Muñoz J A, Blázquez M L, González F, and Ballester A: Hydrometallurgy, Vol. 93 (2008) No. 3-4, pp.81-87.

Google Scholar

[7] Córdoba E M, Muñoz J A, Blázquez M L, González F, and Ballester A: Hydrometallurgy, Vol. 93 (2008) No. 3-4, pp.88-96.

Google Scholar

[8] Córdoba E M, Muñoz J A, Blázquez M L, González F, and Ballester A: Hydrometallurgy, Vol. 93 (2008) No. 3-4, pp.97-105.

Google Scholar

[9] Córdoba E M, Muñoz J A, Blázquez M L, González F, and Ballester A: Minerals Engineering, Vol. 22 (2009) No. 3, pp.229-235.

Google Scholar

[10] Hiroyoshi N, Miki H, Hirajima T, and Tsunekawa M: Hydrometallurgy, Vol. 60 (2001) No. 3, pp.185-197.

DOI: 10.1016/s0304-386x(00)00155-9

Google Scholar

[11] Sohn H Y, Wadsworth M E: Rate Processes of Extractive Metallurgy (Springer Verlag, New York 1979).

Google Scholar

[12] Hiskey J B. Chalcopyrite semiconductor electrochemistry and dissolution, Queneau International Symposium, Extractive Metallurgy of Copper, Nickel and Cobalt, Volume I, pp.949-969 (1993).

Google Scholar

[13] Muñoz P B, Miller J D, and Wadsworth M E: Trans. B, Vol. 10 (1979) No. 2, pp.149-158.

Google Scholar

[14] Hackl R P, Dreisinger D B, Peters E, and King J A: Hydrometallurgy, Vol. 39 (1995) No. 1-3, pp.25-48.

Google Scholar

[15] Ammou C M, Cambazoglu M, and Steinmez D: Bulletin de la Société Française de Minéralogie et de Cristallographie, Vol. 100 (1977), pp.161-177.

DOI: 10.3406/bulmi.1977.7133

Google Scholar