Treatment of water-containing ore beneficiation residues
US-2016318078-A1 · Nov 3, 2016 · US
US10023935B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10023935-B2 |
| Application number | US-201515509147-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 14, 2015 |
| Priority date | Sep 12, 2014 |
| Publication date | Jul 17, 2018 |
| Grant date | Jul 17, 2018 |
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A method of improving metal leach kinetics and recovery during atmospheric or substantially atmospheric leaching of a metal sulfide is disclosed. In some embodiments, the method may comprise the steps of: (a) producing a metal sulfide flotation concentrate; (b) processing the metal sulfide concentrate in a reductive activation circuit that operates at a first redox potential, to produce a reductively-activated metal sulfide concentrate; and, (c) subsequently processing the activated metal sulfide concentrate in an oxidative leach circuit to extract metal values. In some disclosed embodiments, reductive activation steps may be employed prior to oxidative leaching steps (including heap leap leaching or bio-leaching steps). In some embodiments, physico-chemical processing steps may be employed during reductive activation and/or oxidative leaching. Systems for practicing the aforementioned methods are also disclosed.
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What is claimed is: 1. A method of improving metal leach kinetics and recovery during atmospheric or substantially atmospheric leaching of a metal sulfide, the method comprising: (a) producing a metal sulfide concentrate comprising chalcopyrite, via flotation; (b) processing the metal sulfide concentrate in one or more reductive activation reactors which are held at a first redox potential, to produce a reductively-activated metal sulfide concentrate via a copper metathesis reaction; and, (c) subsequently processing the reductively-activated metal sulfide concentrate in an oxidative leach process to extract and recover metal values; wherein the reductively-activated metal sulfide concentrate comprises activated particles comprising chalcopyrite and a transitory, metastable non-stoichiometric binary metal sulfide phase with point defects substantially throughout the entirety of the activated particles. 2. A method of improving metal leach kinetics and recovery during atmospheric or substantially atmospheric leaching of a metal sulfide, the method comprising: (a) producing a metal sulfide concentrate comprising chalcopyrite particles via flotation; (b) processing the metal sulfide concentrate in one or more reductive activation reactors which are held at a first redox potential, to produce a reductively-activated metal sulfide concentrate via a copper metathesis reaction; and, (c) subsequently processing the reductively-activated metal sulfide concentrate in an oxidative leach process to extract and recover metal values; wherein the reductively-activated metal sulfide concentrate comprises converted chalcopyrite particles having a transitionary metastable non-stoichiometric binary metal sulfide mineral phase which differs from covellite. 3. A method of improving metal leach kinetics and recovery during atmospheric or substantially atmospheric leaching of a metal sulfide, the method comprising: (a) producing a metal sulfide concentrate via flotation; (b) processing the metal sulfide concentrate in one or more reductive activation reactors which are held at a first redox potential, to produce a reductively-activated metal sulfide concentrate via a copper metathesis reaction; and, (c) subsequently processing the reductively-activated metal sulfide concentrate in an oxidative leach process to extract and recover metal values; wherein step (c) comprises moving the reductively-activated metal sulfide concentrate from a plurality of oxidative stirred-tank reactors to one or more shear-tank reactors. 4. The method of claim 3 , wherein the plurality of oxidative stirred-tank reactors are in series with said one or more shear-tank reactors. 5. The method of claim 3 , wherein the plurality of oxidative stirred-tank reactors are in parallel with said one or more shear-tank reactors. 6. A method of improving metal leach kinetics and recovery during atmospheric or substantially atmospheric leaching of a metal sulfide, the method comprising: (a) producing a metal sulfide concentrate comprising chalcopyrite via flotation; (b) processing the metal sulfide concentrate in one or more reductive activation reactors which are held at a first redox potential, to produce a reductively-activated metal sulfide concentrate via a copper metathesis reaction; and, (c) subsequently processing the reductively-activated metal sulfide concentrate in an oxidative leach process to extract and recover metal values; wherein step (b) involves converting less than about 10 wt. % or less than about 10 vol. % of chalcopyrite within the metal sulfide concentrate, to a metastable non-stoichiometric binary metal sulfide mineral phase. 7. A method of extracting a metal from a metal sulfide particle, comprising: activating a metal sulfide particle comprising chalcopyrite, by changing a portion of the metal sulfide particle from chalcopyrite to a non-stoichiometric, metastable binary metal sulfide phase to introduce point defects substantially throughout the entirety of the activated metal sulfide particle; and extracting copper from the activated metal sulfide particle. 8. The method of claim 7 , wherein extracting copper from the activated metal sulfide particle comprises an oxidative leaching process. 9. The method of claim 7 , wherein the portion of the metal sulfide particle changed to a non-stoichiometric, metastable binary metal sulfide phase is less than about one tenth of the metal sulfide particle by weight or less than about one tenth by volume. 10. The method of claim 7 , wherein activating the metal sulfide particle is performed in a reductive environment ranging from about 200 to about 650 mV (Standard Hydrogen Electrode). 11. A method of leaching a metal sulfide concentrate, comprising: processing a metal sulfide concentrate in a reactor at a first redox potential to produce a reductively-processed metal sulfide concentrate comprising an activated particle having a non-stoichiometric metastable binary metal sulfide phase with point defects introduced substantially throughout the entirety of the activated particle; and leaching a metal from the reductively-processed metal sulfide concentrate via oxidative dissolution; wherein the oxidative dissolution occurs in an oxidative leach reactor at a second redox potential which is greater than a rest potential of the activated particle. 12. The method of claim 11 , wherein the non-stoichiometric metastable binary metal sulfide phase comprises less than about 10 wt. % or less than about 10 vol. % of the activated particle. 13. The method of claim 11 , wherein the first redox potential ranges from about 200 to about 650 mV (Standard Hydrogen Electrode). 14. The method of claim 11 , wherein the second redox potential ranges from about 600 to about 750 mV (Standard Hydrogen Electrode). 15. The method of claim 11 , wherein the metal sulfide concentrate comprises chalcopyrite. 16. The method of claim 11 , wherein the metal leached from the metal sulfide concentrate is copper. 17. A method of extracting a metal from a metal sulfide particle, comprising: activating a metal sulfide particle comprising chalcopyrite, by changing less than about 10 wt. % or less than about 10 vol. % of the metal sulfide particle from a primary metal sulfide to a binary metal sulfide phase; and extracting copper from the activated metal sulfide particle by an oxidative leach process. 18. The method of claim 17 , wherein the binary metal sulfide phase comprises a non-stoichiometric metastable binary metal sulfide phase with point defects substantially throughout the entirety of the activated metal sulfide particle. 19. A method of leaching a metal sulfide concentrate, comprising: processing a metal sulfide concentrate in a reactor at a first redox potential to produce a reductively-processed metal sulfide concentrate comprising an activated particle having a non-stoichiometric metastable binary metal sulfide phase with point defects introduced substantially throughout the entirety of the activated particle; and leaching a metal from the reductively-processed metal sulfide concentrate via oxidative dissolution; wherein the second redox potential ranges from about 600 to about 750 mV (Standard Hydrogen Electrode).
Leaching or slurrying (with organic compounds C22B3/16) · CPC title
by wet processes (by flotation B03D) · CPC title
by reducing in gaseous or solid state (slag reduction C22B15/0054) · CPC title
by leaching (C22B3/18 takes precedence) · CPC title
Preliminary treatment of ores or scrap · CPC title
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