Solid-state catalysts for low or moderate temperature leach applications and methods thereof

Patent metadata

Field	Value
Publication number	US-11124858-B2
Application number	US-201917272437-A
Country	US
Kind code	B2
Filing date	Aug 27, 2019
Priority date	Aug 27, 2018
Publication date	Sep 21, 2021
Grant date	Sep 21, 2021

Abstract

A method for removing sulfate iron-containing compounds from a low- to moderate-temperature metal sulfide leach circuit (1) is disclosed. A reactor (6) within a chloride leach circuit (5) and which is preferably maintained at a temperature between 20 and 150 degrees Celsius may be provided with a catalyst (4) comprising a material selected from the group consisting of: colloidal hematite, colloidal goethite, particulate containing FeOOH, particulate containing α-FeOOH, particulate containing γ-FeOOH, particulate containing Fe2O3, particulate containing α-Fe2O3, particulate containing γ-Fe2O3, particulate containing Fe3O4, particulate containing Fe(OH)SO4, and a combination thereof. The catalyst (4) may also be used with heap leach and/or dump leach circuits (22), without limitation. Methods for using and generating the catalyst (4) are also disclosed. In some embodiments, the catalyst (4) may be used as an anti-frothing agent (e.g., for zinc leaching, without limitation).

First claim

What is claimed is:

1. A method for removing a sulfate iron-containing compound from a metal sulfide leaching circuit ( 1 ) comprising:
providing a reactor ( 6 ) within a chloride leach circuit ( 5 );
providing a pressure vessel ( 12 ) downstream of the reactor ( 6 );
providing an upstream solid/liquid separation device ( 8 ) between the reactor ( 6 ) and the pressure vessel ( 12 );
providing a solids feed ( 2 ) containing metal sulfide particles to the reactor ( 6 );
leaching the metal sulfide particles in the reactor ( 6 );
dewatering leach residue ( 7 ) leaving the chloride leach circuit ( 5 ) using the upstream solid/liquid separation device ( 8 );
providing a downstream solid/liquid separation device ( 14 ) downstream of the pressure vessel ( 12 ) for receiving product ( 13 ) leaving the pressure vessel ( 12 );
precipitating a sulfate iron-containing compound out of solution in the pressure vessel ( 12 );
removing said sulfate iron-containing compound using the downstream solid/liquid separation device ( 14 );
providing a catalyst ( 4 ) comprising a material selected from the group consisting of: colloidal hematite, colloidal goethite, particulate containing FeOOH, particulate containing α-FeOOH, particulate containing γ-FeOOH, particulate containing Fe 2 O 3 , particulate containing α-Fe 2 O 3 , particulate containing γ-Fe 2 O 3 , particulate containing Fe 3 O 4 , particulate containing Fe(OH)SO 4 , and a combination thereof;
providing the catalyst ( 4 ) to the reactor ( 6 ); and
optionally providing the catalyst ( 4 ) to the pressure vessel ( 12 ).

2. The method according to claim 1 , further comprising maintaining the reactor ( 6 ) at a temperature between 20 and 150 degrees Celsius.

3. The method according to claim 1 , further comprising maintaining the reactor ( 6 ) at a temperature between 20 and 100 degrees Celsius and maintaining the reactor ( 6 ) at atmospheric pressure.

4. The method according to claim 1 , further comprising maintaining the reactor ( 6 ) at a temperature between 40 and 150 degrees Celsius and maintaining the reactor ( 6 ) at above-atmospheric pressure.

5. The method according to claim 1 , wherein the catalyst ( 4 ) is a solid-state catalyst.

6. The method according to claim 1 , wherein the metal sulfide particles of the solids feed ( 2 ) comprise pyrite, pyrrhotite, and/or marcasite.

7. The method according to claim 1 , further comprising delivering a liquids fraction ( 16 ) from the downstream solid/liquid separation device ( 14 ) to the reactor ( 6 ); wherein the liquids fraction ( 16 ) comprises a chloride salt solution comprising ferric chloride.

8. The method according to claim 1 , further comprising leaching a solids fraction ( 9 ) of the leach residue ( 7 ) from the chloride leach circuit ( 5 ), in a cyanide leach circuit ( 10 ), to recover a precious metal therefrom.

9. The method according to claim 8 , wherein the precious metal is selected from the group consisting of: gold, silver, a platinum group metal, and a combination thereof.

10. The method according to claim 1 , further comprising delivering a liquids fraction ( 11 ) of the leach residue ( 7 ) from the chloride leach circuit ( 5 ), to the pressurized vessel ( 12 ).

11. The method according to claim 1 , further comprising maintaining the pressurized vessel ( 12 ) at a pressure between 1 and 15 bar.

12. The method according to claim 1 , further comprising the step of doping material of the catalyst ( 4 ) with Al 3+ , Ti 3+ , or a combination thereof.

13. The method according to claim 1 , wherein the catalyst ( 4 ) is colloidal and the method further comprises supporting the material of the catalyst ( 4 ) on a particle or particulate.

14. The method according to claim 1 , further comprising binding the catalyst ( 4 ) to a surface of a component within the reactor ( 6 ) and/or the pressure vessel ( 12 ); or forming a porous or non-porous film or coating comprising the catalyst ( 4 ) on a surface of a component within the reactor ( 6 ) and/or the pressure vessel ( 12 ).

15. The method according to claim 1 , further comprising promoting high oxidation and promoting one of the following in the reactor ( 6 ): rapid conversion of sulfide to sulfate; rapid conversion of arsenic III to arsenic V.

16. The method according to claim 1 , further comprising promoting rapid conversion of ferrous to ferric in the pressure vessel ( 12 ).

17. The method according to claim 1 , further comprising mitigating froth formation in the leach reactor ( 6 ) by virtue of the steps of: providing the catalyst ( 4 ) to the reactor ( 6 ) and optionally providing the catalyst ( 4 ) to the pressure vessel ( 12 ).

18. The method according to claim 1 , wherein the metal sulfide particles in the solids feed ( 2 ) comprises sphalerite, the method comprising leaching zinc (Zn) into solution in the reactor ( 6 ).

Assignees

• Smidth As F L

Inventors

• Chaiko David J

Classifications

• C22B3/02

  Apparatus therefor · CPC title

• C22B3/44

  by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title

• C22B3/08 Primary

  Sulfuric acid {, other sulfurated acids or salts thereof} · CPC title

• C22B3/06

  in inorganic acid solutions {, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions} · CPC title

• B01J23/745

  Iron · CPC title