System and method for enhanced metal recovery during atmospheric leaching of metal sulfides

Patent metadata

Field	Value
Publication number	US-2017283908-A1
Application number	US-201515509147-A
Country	US
Kind code	A1
Filing date	Sep 14, 2015
Priority date	Sep 12, 2014
Publication date	Oct 5, 2017
Grant date	—

Abstract

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.

First claim

What is claimed is:

1 . (canceled)

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 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-processed metal sulfide concentrate comprises activated particles composed of chalcopyrite and a transitory, metastable non-stoichiometric binary metal sulfide phase with point defects substantially throughout the entirety of the activated particles.

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 the metal sulfide concentrate comprises chalcopyrite particles and wherein the reductively-processed metal sulfide concentrate comprises converted chalcopyrite particles having a transitionary metastable non-stoichiometric binary metal sulfide mineral phase which differs from covellite.

4 . (canceled)

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9 . (canceled)

10 . 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 the step of processing the reductively-processed metal sulfide concentrate within a plurality oxidative leach reactors to extract a metal from said reductively-activated concentrate via dissolution further comprises moving the reductively-processed metal sulfide concentrate from a plurality of oxidative, stirred-tank reactors to one or more shear-tank reactors.

11 . The method of claim 10 , wherein the plurality of oxidative stirred-tank reactors are in series with said one or more shear-tank reactors.

12 . The method of claim 10 , wherein the plurality of oxidative stirred-tank reactors are in parallel with said one or more shear-tank reactors.

13 . 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; further comprising converting an outer portion of a metal sulfide within the metal sulfide concentrate to a metastable non-stoichiometric binary metal sulfide mineral phase within the one or more reductive activation reactors so as to introduce point defects substantially throughout the entirety of the activated particle.

14 . A method of extracting a metal from a metal sulfide particle, comprising:
activating a metal sulfide particle by changing a portion of the metal sulfide particle from a primary metal sulfide to a non-stoichiometric, metastable binary metal sulfide phase to introduce point defects substantially throughout the entirety of the activated particle; and extracting a metal from the activated metal sulfide particle.

15 . The method of claim 14 , wherein extracting the metal from the activated metal sulfide particle comprises an oxidative leaching process.

16 . (canceled)

17 . (canceled)

18 . The method of claim 14 , 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.

19 . The method of claim 14 , wherein activating the metal sulfide particle is performed in a reductive environment ranging from about 200 to about 650 mV (SHE).

20 . (canceled)

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28 . (canceled)

29 . The method of claim 14 , wherein the primary metal sulfide phase comprises chalcopyrite.

30 . 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.

31 . (canceled)

32 . (canceled)

33 . The method of claim 30 , 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.

34 . The method of claim 30 , wherein the oxidative dissolution occurs in an oxidative leach reactor at a second redox potential greater than a rest potential of the activated particle.

35 . The method of claim 30 , wherein the first redox potential ranges from about 200 to about 650 mV (SHE).

36 . The method of claim 30 , wherein the second redox potential ranges from about 600 to about 750 mV (SHE).

37 . The method of claim 30 , wherein the metal sulfide concentrate comprises chalcopyrite.

38 . The method of claim 30 , wherein the metal leached from the metal sulfide concentrate is copper.

39 . A method of extracting a metal from a metal sulfide particle, comprising:
activating a metal sulfide particle by changing a portion of the metal sulfide particle from a primary metal sulfide to a binary metal sulfide phase; and if there is a sufficient amount of activated binary metal sulfide present, extracting a metal from the metal sulfide by an oxidative leach process.

40 . The method of claim 39 , w

Assignees

• Chaiko David J
• Smidth As F L

Inventors

• Chaiko David J
• Baczek Frank
• Walters Tom
• Rocks Sarah (Sally)
• Eyzaguirre Carlos

Classifications

• C22B3/02

  Apparatus therefor · CPC title

• C22B1/00 Primary

  Preliminary treatment of ores or scrap · CPC title

• C22B3/04

  by leaching (C22B3/18 takes precedence) · CPC title

• C22B15/0021

  by reducing in gaseous or solid state (slag reduction C22B15/0054) · CPC title

• C22B15/0008

  by wet processes (by flotation B03D) · CPC title