Abstract A method for selectively recovering metals from generally sulphidic particulate materials containing metals selected from nickel, copper and precious metals in which the particulate material is preferentially leached in an agitated chloride solution containing cuprous ions by the action of chlorine. The redox potential of the solution increases upon feeding chlorine thereto and decreases upon feeding particulate material thereto, and the rate of feeding of chlorine is controlled relative to the rate of feeding of material to control the redox potential substantially at or below a selected potential at which the metal is leached preferentially with respect to other metals in the material. Nickel is leached preferentially with respect to copper and precious metals in a matte, for example, to produce a nickel-rich solution and to concentrate the precious metals in a nickel-depleted residue. The leach residue, or other concentrates containing copper and precious metals may also be treated by the method to selectively dissolve the copper values preferentially to the precious metal values. Dissolved copper in the nickel-bearing leach solutions may be precipitated in a separate tank by agitating the leach solution in the presence of elemental sulphur and nickel sulphide particles having an atomic ratio of nickel to sulphur greater than one, thereby producing copper sulphide and a substantially copper-free nickel-chloride solution which can be separated and the values recovered by conventional means.
Process for the recovery and separation of copper sulphide and nickel from aqueous nickeliferous solution containing dissolved copper comprising, i. feeding nickel sulphide having an atomic ratio of nickel to sulphur greater than one to the nickeliferous solution thereby establishing a selected redox potential in the range of 30-250 mV and forming an agitated slurry thereof, ii. reacting the nickel sulphide with dissolved copper in the solution in the presence of elemental sulphur at said selected redox potential, thereby precipitating copper sulphide and dissolving nickel in the nickeliferous solution, iii. withdrawing copper sulphide and copper-depleted solution from the slurry, iv. separating the copper sulphide from the copper-depleted solution, and v. recovering nickel from the copper-depleted solution.
Claim 2
Dependent Claim
116 words
Process for the recovery and separation of copper sulphide and nickel from aqueous nickeliferous solution containing dissolved copper comprising, i. feeding nickel sulphide having an atomic ratio of nickel to sulphur greater than one to the nickeliferous solution thereby establishing a selected redox potential in the range of 30-250 mV and forming an agitated slurry thereof, ii. reacting the nickel sulphide with dissolved copper in the solution in the presence of elemental sulphur at said selected redox potential, thereby precipitating copper sulphide and dissolving nickel in the nickeliferous solution, iii. withdrawing copper sulphide and copper-depleted solution from the slurry, iv. separating the copper sulphide from the copper-depleted solution, and v. recovering nickel from the copper-depleted solution.
Claim 3
Dependent Claim
21 words
Process according to claim 1 in which the solution is selected from the group consisting of chloride solutions and sulphate solutions.
Claim 4
Dependent Claim
29 words
Process according to claim 1 in which elemental sulphur is selected from the group consisting of sulphur flowers and sulpher-bearing particles resulting from the chlorine leaching of metal sulphides.
Claim 5
Dependent Claim
19 words
Process according to claim 1 in which the nickel sulphide is Ni 3 S 2 in a nickeliferous matte.
Claim 6
Dependent Claim
70 words
Process according to claim 1 in which the nickeliferous solution is a chloride solution resulting from chlorine leaching of nickeliferous matte, the elemental sulphur is sulphur-bearing particles resulting from the chlorine leach, the nickel sulphide is Ni 3 S 2 in nickeliferous matte, and the feed rate of nickeliferous matte to the slurry is controlled to establish said selected redox potential and thereby a selected residual copper concentration is solution.