System and method for parallel solution extraction of one or more metal values from metal-bearing materials
US-2015361527-A1 · Dec 17, 2015 · US
US2023128925A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023128925-A1 |
| Application number | US-202117776448-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 16, 2021 |
| Priority date | Jul 16, 2020 |
| Publication date | Apr 27, 2023 |
| Grant date | — |
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Alkaline oxidation process for treating refractory sulfide ore or concentrate particles enriched in a metal to be recovered comprising stages in which refractory ore or concentrate particles are surface-oxidized in an alkaline oxidation step in alkaline liquid phase with calcium hydroxide forming an alkaline slurry, which slurry is thereafter mechanically activated to remove passivating coatings from the surface oxidized refractory ore particles.
Opening claim text (preview).
1 : Alkaline oxidation process for treating refractory sulfide ore particles enriched in a metal to be recovered wherein refractory sulfide ore particles are submitted to at least 3 stages in each of which said refractory sulfide ore particles are surface-oxidized by an oxidizing agent in an alkaline oxidation step (CSTR) in alkaline liquid phase and form an alkaline slurry containing surface oxidized refractory sulfide ore particles and in each of which said alkaline slurry is thereafter submitted to a mechanical activation step (MA) for at least partly removing a surface layer containing oxidized matter from the surface-oxidized refractory sulfide ore particles, said mechanical activation forming a mechanically activated slurry containing oxidized matter, refractory sulfide ore particles from which oxidized matter has been removed, alkaline liquid phase and liberated metal to be recovered by further processing or returned to a next or a previous alkaline oxidation step, said alkaline liquid phase containing calcium hydroxide as an alkaline agent and said refractory sulfide ore being a refractory sulfide ore or concentrate enriched in a metal selected from the group consisting of gold, silver, platinum, palladium, coper, nickel, zinc, cobalt and combinations thereof, said at least 3 stages comprising: a series of n alkaline oxidation steps in a series of n reactors (CSTR), each n th alkaline oxidation forming a n th alkaline slurry, where n is an integer comprised between 3 and 10, a series of x mechanical activation steps (MR), each mechanical activation step being a mechanical activation of said n th alkaline slurry, where x is an integer, equal or lower than n, and comprised between 3 and 10, wherein said series of n alkaline oxidation steps comprises at least: a first alkaline oxidation step wherein said refractory ore particles enriched in a metal to be recovered are fed into an agitated reactor and form a first alkaline slurry, at least one intermediate alkaline oxidation step fed with one alkaline slurry from a previous alkaline oxidation step, a last alkaline oxidation step being said n th alkaline oxidation step fed with one alkaline slurry from a previous alkaline oxidation step, said series of x mechanical activation steps comprising at least: a first mechanical activation step of said first alkaline slurry in a first mechanical activation means to form a first mechanically activated slurry, at least one intermediate mechanical activation step of a n th alkaline slurry with said n th alkaline slurry being comprised between a 2 nd alkaline slurry and a (x−1) th alkaline slurry in a y th mechanical activation means to form a y th mechanically activated slurry, a last mechanical activation step of said last alkaline slurry being said x th mechanical activation step in a x th mechanical activation means to form an x th mechanically activated slurry. 2 - 3 . (canceled) 4 : Alkaline oxidation process according to claim 1 , wherein said oxidizing agent is an oxidizing liquid, an oxidizing powder or an oxidizing gas. 5 : Alkaline oxidation process according to claim 1 , wherein said calcium hydroxide of said alkaline liquid phase is obtained by one or more addition of dry quicklime CaO, hydrated lime Ca(OH) 2 , or milk of lime, said one or more addition being selected from the group consisting of an addition upstream one n th reactor, in one n th reactor, upstream a x th mechanical activation means, in a x th mechanical activation means and a combination thereof. 6 : Alkaline oxidation process according to claim 1 , wherein each intermediate alkaline oxidation step is fed by a previous alkaline oxidation step, via a mechanical activation step. 7 : Alkaline oxidation process according to claim 1 , wherein at least one alkaline oxidation step of said series of n alkaline oxidation steps is performed at atmospheric pressure. 8 : Alkaline oxidation process according to claim 1 , wherein at least one alkaline oxidation step of said series of n alkaline oxidation steps is performed at a temperature comprised between 70 and 100° C. 9 : Alkaline oxidation process according to claim 1 , wherein at least one alkaline oxidation step of said series of n alkaline oxidation steps is performed with a dissolved oxygen content comprised between 1 and 30 mg/dm 3 of liquid phase. 10 : Alkaline oxidation process according to claim 9 , wherein at least one alkaline oxidation step of said series of n alkaline oxidation steps is performed with a dissolved oxygen content comprised between 1 and 5 mg/dm 3 of liquid phase. 11 : Alkaline oxidation process according to claim 1 , wherein at least one alkaline oxidation step of said series of n alkaline oxidation steps is performed at a pH comprised between 10 and 12.5, said pH being controlled with a controlled addition of said alkaline agent. 12 : Alkaline oxidation process according to claim 1 , wherein at least one alkaline oxidation step of said series of n alkaline oxidation steps is performed with solid content in the agitated reactor comprised between 10 and 70 wt % with respect to the total weight contained in said agitated reactor. 13 : Alkaline oxidation process according to claim 1 , wherein at least one of said series of x mechanical activation steps is performed in one of a vertical mill, a vertical stirred mill, a horizontal mill, an attritor, a stirred ball mill or a horizontal stirred mill. 14 : Alkaline oxidation process according to claim 1 , wherein said refractory sulfide ore particles fed to said first alkaline oxidation step are obtained by a previous crushing and grinding, down to having 80% of the particles with a diameter in the range between 25 and 200 μm. 15 : Alkaline oxidation process according to claim 14 , wherein said crushed and ground refractory sulfide ore particles are subjected to mineral flotation to produce a concentrate of refractory sulfide ore particles fed to said first alkaline oxidation step. 16 - 22 . (canceled)
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