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The Study of Copper Leaching from Conichalcite and Chalcopyrite Using Alternative Lixiviants

  • Junmo Ahn
  • Isabel F. Barton
  • Doyun Shin
  • Jaeheon LeeEmail author
Conference paper
Part of the The Minerals, Metals & Materials Series book series (MMMS)

Abstract

This project investigated alternative lixiviants for leaching copper from chalcopyrite and conichalcite, two highly refractory Cu ore minerals. Chalcopyrite (CuFeS2) is the most abundant of the copper sulfide minerals; conichalcite (CaCuAsO4OH) is less well known but contributes to supergene Cu inventory in high-As deposits. Neither leaches well in sulfuric acid. Sulfurous acid, glycine, methanesulfonic acid (MSA), and thiourea (for conichalcite leaching test) were tested as lixiviants for chalcopyrite- and conichalcite-bearing ores with ferric sulfate or hydrogen peroxide as oxidant. The highest Cu extraction from chalcopyrite was obtained by MSA (47% Cu recovery in 30 g/L of MSA with 5 g/L Fe3+ at 75 ℃ within 96 h; nearly 100% Cu extraction in 30 g/L MSA with 3% hydrogen peroxide at 75 ℃ within 72 h). Glycine recovered 20.7% of copper from chalcopyrite at room temperature within 96 h. All these compare favorably to the results of sulfuric acid leaching of chalcopyrite (1.5% recovery at 96 h). Conichalcite proved less refractory to sulfuric acid (46–71% extraction in 10 g/L H2SO4 with 3 g/L Fe3+ in 24 h) and leached almost as well in MSA (45–67% extraction in 20 g/L MSA with 3 g/L Fe3+ in 24 h), but glycine, thiourea, and sulfurous acid did not effectively leach conichalcite.

Keywords

Copper Chalcopyrite Conichalcite Alternative lixiviants Sulfurous acid Methanesulfonic acid Glycine 

References

  1. 1.
    Córdoba E, Muñoz J, Blázquez M, González F, Ballester A (2008) Leaching of chalcopyrite with ferric ion. Part I: General aspects. Hydrometallurgy 93(3):81–87Google Scholar
  2. 2.
    Klauber C (2008) A critical review of the surface chemistry of acidic ferric sulphate dissolution of chalcopyrite with regards to hindered dissolution. Int J Min Process 86(1):1–17CrossRefGoogle Scholar
  3. 3.
    Reddy BJ, Frost RL, Martens WN (2005) Characterization of conichalcite by SEM, FTIR, Raman and electronic reflectance spectroscopy. J Miner Sci 69(2):155–167Google Scholar
  4. 4.
    Sato T, Lawson F (1983) Differential leaching of some lead smelter slags with sulfurous acid and oxygen. Hydrometallurgy 11(3):371–388CrossRefGoogle Scholar
  5. 5.
    Youzbashi A, Dixit S (1993) Leaching of Cu2O with aqueous solution of sulfur dioxide. Metall Mater Trans B 24(4):563–570CrossRefGoogle Scholar
  6. 6.
    Zhang W, Singh P, Muir D (2000) SO2/O2 as an oxidant in hydrometallurgy. Miner Eng 13(13):1319–1328CrossRefGoogle Scholar
  7. 7.
    Ahmed IB, Gbor PK, Jia CQ (2000) Aqueous sulphur dioxide leaching of Cu, Ni Co, Zn and Fe from smelter slag in absence of oxygen. Can J Chem Eng 78(4):694–703CrossRefGoogle Scholar
  8. 8.
    Gernon M (1999) Environmental benefits of methanesulfonic acid. Comparative properties and advantages. Green Chem 1(3):127–140Google Scholar
  9. 9.
    Feng Q, Wen S, Zhao W, Lv C, Bai X (2015) Leaching of copper from malachite with methane-sulfonic acid. Solvent Extr Res Dev 22(2):159–168CrossRefGoogle Scholar
  10. 10.
    Oraby E, Eksteen J (2014) The selective leaching of copper from a gold–copper concentrate in glycine solutions. Hydrometallurgy 150:14–19CrossRefGoogle Scholar
  11. 11.
    Oraby E, Eksteen J (2015) The leaching of gold, silver and their alloys in alkaline glycine–peroxide solutions and their adsorption on carbon. Hydrometallurgy 152:199–203CrossRefGoogle Scholar

Copyright information

© The Minerals, Metals & Materials Society 2018

Authors and Affiliations

  • Junmo Ahn
    • 1
  • Isabel F. Barton
    • 1
    • 2
  • Doyun Shin
    • 1
  • Jaeheon Lee
    • 1
    Email author
  1. 1.Department of Mining and Geological EngineeringUniversity of ArizonaTucsonUSA
  2. 2.Lowell Institute for Mineral Resources, University of ArizonaTucsonUSA

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