Control of the redox potential by oxygen limitation improves bacterial leaching of chalcopyrite.

Shake flask and stirred tank bioleaching experiments showed that the dissolution of chalcopyrite is inhibited by ferric ion concentrations as low as 200 mg L(-1) and redox potentials >420 mV (vs. Ag/AgCl). Chemical leaching of chalcopyrite (4% suspension, surface area 2.3 m2 g(-1)) was enhanced fourfold in the presence of 0.1 M ferrous sulphate compared with 0.1 M ferric sulphate. A computer-controlled reactor was designed to function as a "potentiostat"-bioreactor by arresting the air supply to the reactor when the redox potential in solution was greater than a designated setpoint. Leaching at a low, constant redox potential (380 mV vs. Ag/AgCl) achieved final copper recoveries of 52%-61%, which was twice that achieved with a continuous supply of oxygen (<30% extraction). The bacterial populations were observed to continue growing under oxygen limitation but in a controlled manner that was found to improve chalcopyrite dissolution. As the control mechanism is easily established and is likely to decrease production cost, the use of this technology may find application in industry.

[1]  R. Cord-Ruwisch,et al.  The role of iron-oxidizing bacteria in stimulation or inhibition of chalcopyrite bioleaching , 2000 .

[2]  M. Tsunekawa,et al.  A model for ferrous-promoted chalcopyrite leaching , 2000 .

[3]  Hirota,et al.  Inhibitory effect of iron-oxidizing bacteria on ferrous-promoted chalcopyrite leaching , 1999, Biotechnology and bioengineering.

[4]  F. Carranza,et al.  Silver catalyzed IBES process: application to a Spanish copper–zinc sulphide concentrate: Part 3. Selection of the operational parameters for a continuous pilot plant , 1998 .

[5]  M. Tsunekawa,et al.  A case of ferrous sulfate addition enhancing chalcopyrite leaching , 1997 .

[6]  J. Modak,et al.  Estimation of mineral-adhered biomass of Thiobacillus ferrooxidans by protein assay — some problems and remedies , 1996 .

[7]  J. A. King,et al.  Passivation of chalcopyrite during oxidative leaching in sulfate media , 1995 .

[8]  J. E. Dutrizac,et al.  Elemental Sulphur Formation During the Ferric Sulphate Leaching of Chalcopyrite , 1989 .

[9]  T. Hirato,et al.  The leaching of chalcopyrite with ferric sulfate , 1987 .

[10]  H. Kametani,et al.  Effect of suspension potential on the oxidation rate of copper concentrate in a sulfuric acid solution , 1985 .

[11]  T. Biegler,et al.  The Electrochemistry of Surface Oxidation of Chalcopyrite , 1985 .

[12]  M. Wadsworth,et al.  Passive and transpassive anodic behavior of chalcopyrite in acid solutions , 1982 .

[13]  R. Mcmillan,et al.  Anodic dissolution of n-type and p-type chalcopyrite , 1982 .

[14]  J. E. Dutrizac,et al.  The dissolution of chalcopyrite in ferric sulfate and ferric chloride media , 1981 .

[15]  C. Reid The association of twinning and fracture in bcc metals , 1981 .

[16]  G. Power,et al.  Electrochemical aspects of leaching copper from chalcopyrite in ferric and cupric salt solutions , 1981 .

[17]  J. E. Dutrizac,et al.  The kinetics of dissolution of chalcopyrite in ferric ion media , 1978 .

[18]  M. M. Bradford A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. , 1976, Analytical biochemistry.