Abstract In a process according to the present invention pre-reduced lateritic ores containing iron and nickel are leached with an aqueous sulphuric acid leach liquor containing or into which is introduced in the presence of the ore a peroxidant selected from hydrogen peroxide and peroxymonosulphuric acid. By so doing, the liquor is obtained with a lower concentration of iron than if the peroxidant had not been employed. In preferred embodiments the leaching is carried out at from 40° to 70° C. for a period of 1 to 5 hours; when hydrogen peroxide is used, it is preferably introduced continuously or progressively throughout the reaction period and when peroxymonosulphuric acid is used it is preferably introduced initially. The acidity of the liquor can be reduced at the end of the reaction to pH3 to 4 to further lower the content of iron in solution.
In a process for the extraction of nickel from a prereduced lateritic ore containing after reduction nickel in the zero oxidation state and iron, at least part of which is in the zero oxidation state comprising contacting the prereduced ore with an aqueous sulphuric acid leach liquor, the improvement consisting essentially of maintaining the prereduced ore and leach liquor in contact until at least some nickel has been brought into solution, at a temperature of from 30° to 70° C., the liquor containing peroxymonosulphuric acid or the same being introduced thereinto, in a mole ratio of from 0.3 to 1.0 moles per mole of sulphuric acid, and the sulphuric peroxymonosulphuric acids concentration in total being from 15 to 25 gpl.
Claim 2
Dependent Claim
120 words
In a process for the extraction of nickel from a prereduced lateritic ore containing after reduction nickel in the zero oxidation state and iron, at least part of which is in the zero oxidation state comprising contacting the prereduced ore with an aqueous sulphuric acid leach liquor, the improvement consisting essentially of maintaining the prereduced ore and leach liquor in contact until at least some nickel has been brought into solution, at a temperature of from 30° to 70° C., the liquor containing peroxymonosulphuric acid or the same being introduced thereinto, in a mole ratio of from 0.3 to 1.0 moles per mole of sulphuric acid, and the sulphuric peroxymonosulphuric acids concentration in total being from 15 to 25 gpl.
Claim 3
Dependent Claim
38 words
A process according to claim 1 wherein the leach liquor has an acid concentration of sulphuric and peroxy monosulphuric acids in total of from 15 to 20 gpl, of which the peroxymonosulphuric acid contributes 6 to 8 gpl.
Claim 4
Dependent Claim
55 words
A process as claimed in claim 1 wherein the pH of the leach liquor is raised to a pH in the range of 2.5 to 4.0 after the ore and liquor have been in contact for from 20 to 60 minutes or after the electropotential of the liquor has fallen to below its original value.