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Electrochemical processes in recovering metals from ores

Journal Article · · JOM (1989); (USA)
DOI:https://doi.org/10.1007/BF03220927· OSTI ID:6712822
 [1];  [2]
  1. Hypalon Technical Polymer Product Dept., DuPont, Beaumont, TX (US)
  2. Nevada Univ., Reno, NV (USA). Dept. of Chemical and Metallurgical Engineering
Chalcopyrite (CuFeS{sub 2}) is one of the most abundant copper-bearing minerals in the U.S. Oxidative leaching and smelting and refining are the most common methods used for recovering copper from chalcopyrite. One of the problems associated with oxidative leaching is the formation of an elemental sulfur product layer around the unreacted chalcopyrite core. The sulfur coating slows the reaction by inhibiting both the diffusion of the oxidant to the unreacted core, and the diffusion of the copper and iron species to the bulk solution. Another problem with leaching is that the iron and copper are oxidized simultaneously. Both appear in the bulk solution in their most oxidized states. The direct electrodissolution of copper sulfide ore slurries could reduce the number of steps involved in the copper recovery process, possibly leading to significant reductions in energy consumption and operating costs. The potential application of electrodissolution processes in hydrometallurgy has been reviewed. This paper reviews investigations of the electrochemical dissolution of chalcopyrite, digenite (Cu{sub 1.8}S), chalcocite (Cu{sub 2}S) and covellite (CuS).
OSTI ID:
6712822
Journal Information:
JOM (1989); (USA), Journal Name: JOM (1989); (USA) Vol. 42:4; ISSN JOMME
Country of Publication:
United States
Language:
English

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