Metal sulphide extraction
AssigneeDuval Corporation
InventorsLeonard R. Ochs, Archibald W. Fletcher, Harald Weber, David Naden
Life of this patent
Estimating the term…
Loading patent…
AssigneeDuval Corporation
InventorsLeonard R. Ochs, Archibald W. Fletcher, Harald Weber, David Naden
Estimating the term…
A process is described for recovering metal values from a zinc-containing complex sulphide material comprising leaching the material in a first leaching stage under non-oxidative conditions with a controlled amount of an aqueous chloride lixiviant solution containing cupric chloride in an amount which is selected so as to solubilize at least a part of the zinc in the material and to precipitate a quantity of cupric sulphide substantially equivalent on a molar basis to the zinc leached from the material, the lixiviant solution further containing sufficient of a source of chloride ions other than cupric chloride to ensure solubilization of metal chlorides present, recovering from the first leaching stage a zinc chloride-containing leach liquor, recovering metal values from said leach liquor in a metal recovery section, treating solids from the first leaching stage under oxidizing conditions in a second leaching stage with a liquor containing hydrochloric acid and metal chlorides thereby to solubilize further metal values from the solids, to precipitate iron values and to regenerate cupric chloride-containing lixiviant solution for use in the first leaching stage, and recovering from the second leaching stage (a) a solids residue consisting essentially of (i) iron values in the form of ferric hydroxide and jarosite and (ii) sulphur and that is substantially free from non-ferrous metal values and (b) a cupric chloride-containing lixiviant solution for recycle to the first leaching stage.
A process for recovering metal values from a zinc-containing complex sulphide material, which sulphide material further contains copper in sulphide form, comprising leaching the material in a first leaching stage under non-oxidative conditions with a controlled amount of an aqueous chloride lixiviant solution containing cupric chloride in an amount which is selected so as to solubilize at least a part of the zinc in the material and to precipitate a quantity of cupric sulphide substantially equivalent on a molar basis to the zinc leached from the material, the lixiviant solution further containing sufficient of a source of chloride ions other than cupric chloride to ensure solubilization of metal chlorides present, recovering from the first leaching stage a zinc chloride-containing leach liquor, which further contains an amount of copper ions equivalent to the copper content of the zinc-containing complex sulphide material, recovering metal values from said leach liquor in a metal recovery section, treating solids containing copper in sulphide form from the first leaching stage under oxidizing conditions in a second leaching stage with a liquor containing (i) hydrochloric acid in an amount corresponding approximately to the stoichiometric quantity required for leaching the non-ferrous metal content of the copper sulphide-containing solids and (ii) metal chlorides thereby to solubilize substantially all the non-ferrous metal values in the solids, to precipitate iron values in the form of ferric hydroxide and jarosite and to regenerate cupric chloride-containing lixiviant solution for use in the first leaching stage, and recovering from the second leaching stage (a) a solids residue consisting essentially of (i) iron values in the form of ferric hydroxide and jarosite and (ii) sulphur, which solids residue is substantially free from non-ferrous metal values, and (b) a cupric chloride-containing lixiviant solution for recycle to the first leaching stage.
Dependencies are inferred from the claim text.