The Leaching of Dolomitic-Copper Ore Using Sulphuric Acid Under Controlled Conditions~!2010-03-15~!2010-06-17~!2010-07-21~!

Abstract

The leaching of dolomitic-copper ore using sulphuric acid under controlled conditions was studied with a view to evaluating the economic value and the effect of ore pulverisation, particle size, temperature and pH on the recovery of copper from chalcopyrite. The samples were ground and mixed with water and sulphuric acid to form an acid soluble copper content of 4.07 %, 8.14 % total copper and 22 % solids. The leaching was carried in duration of 0-6 hours. The sulphuric acid was found to be effective in recovering copper from chalcopyrite with efficiencies of 72 to 93 % for 75 micron particle size and 65 to 84% for the 212 micron sieve size at different pulverising times. The kinetics of dolomitic ore showed the reaction with H 2 SO 4 was second order with respect to chalcopyrite and first order with respect to dolomite and was consistent with the shrinking core model. The increase in temperature produced an increase in the recovery of copper from solids into the bulk solution. The leaching was favoured at low pH values (1.8<pH<3) than at high ones (pH >3). Profit levels for the reversed pH numbers, high to low (low to high pH), were higher than values for leaching from low to high pH numbers (high to low pH) particularly for acid sales. Since the economic evaluation showed positive profit levels for both acid and copper sales, the process was viable.

Chalcopyrite Leaching with Hydrogen Peroxide and Iodine Species in Acidic Chloride Media at Room Temperature: Technical and Economic Evaluation

“…This section presents a simplistic cost evaluation to support the discussion [52,53]. The operational costs of the leaching experiments depend on factors such as the concentration and price of the reagents used, as well the electricity and water consumption.…”

Kinetics of Hydrochloric Acid Leaching of Copper from its Ore

“…In another study, Demirkiran et al [19] found that copper leaching from a malachite ore in acetic acid solutions fits the mixed kinetic control model accounting for diffusion through the product layer at temperatures between 20 °C and 45 °C and a surface chemical reaction at temperatures between 45 °C and 60 °C. Using sulfuric acid under controlled conditions, the leaching of dolomitic-copper ore was studied by Ntengwe [20]. Copper recovery was found to be 72 to 93 % for 75 µm particle size and 65 to 84 % for the 212 µm particle size.…”