IP Library Granted Patent US 6,890,371
Granted Patent B2
US 6,890,371 · App. 10/328,633 · Granted May 10, 2005

Method for processing elemental sulfur-bearing materials using high temperature pressure leaching

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Quick Facts
Patent No.
US 6,890,371
App. No.
10/328,633
Granted
May 10, 2005
Kind
B2
Abstract

The present invention relates generally to a process for the production of sulfuric acid and liberation of precious metal values from materials containing sulfur through pressure leaching operations. In accordance with various aspects of the present invention, the sulfur-bearing materials may comprise residues from pressure leaching operations, such as those carried out at medium temperatures. The process of the present invention can be advantageously used to convert such sulfur-bearing materials to sulfuric acid by means of pressure leaching. The sulfuric acid so produced can be used beneficially in other mineral processing operations, for example those at the site where it is produced. Metals, such as precious metals, that are contained within the sulfur-bearing materials advantageously may be recovered from processing products by established precious metals recovery technology.

Claims (37)

1. A treatment process comprising the steps of:

a) providing a feed stream comprising an elemental sulfur-bearing material and a dispersant, wherein said elemental sulfur-bearing material comprises an elemental sulfur-containing residue from a pressure leaching operation;

b) pressure leaching at least a portion of said feed stream at a temperature in the range of about 220° C. to about 275° C. in an oxygen-containing atmosphere in an agitated multiple-compartment pressure leaching vessel to form a product slurry comprising a sulfuric acid solution;

c) separating at least a portion of said sulfuric acid solution from said product slurry to yield a residue;

d) recovering at least one metal value from said residue.

2. The process of claim 1 , wherein said elemental sulfur-bearing material comprises an elemental sulfur-containing residue from a pressure leaching operation carried out at a temperature in the range of about 140° C. to about 180° C.

3. The process of claim 1 wherein said step of recovering metal values from said residue comprises recovering at least one precious metal from said residue.

4. The process of claim 1 wherein said step of pressure leaching at least a portion of said feed stream comprises pressure leaching at temperatures above about 235° C.

5. The process of claim 1 wherein said step of providing a feed stream comprising an elemental sulfur-bearing material and a dispersant comprises providing a feed stream comprising an elemental sulfur-bearing material and a sufficient amount of ground sand or mineral processing tailings.

6. A treatment process comprising the steps of:

a) providing a feed stream comprising an elemental sulfur-bearing material, wherein said elemental sulfur-bearing material comprises an elemental sulfur-containing residue from a pressure leaching operation;

b) pressure leaching at least a portion of said feed stream in the presence of a dispersant at a temperature in the range of about 220° C. to about 275° C. in an oxygen-containing atmosphere in an agitated multiple-compartment pressure leaching vessel to form a product slurry comprising a sulfuric acid solution;

c) separating at least a portion of said sulfuric acid solution from said product slurry to yield a residue;

d) recovering at least one metal value from said residue.

7. The process of claim 6 , wherein said elemental sulfur-bearing material comprises an elemental sulfur-containing residue from a pressure leaching operation carried out at a temperature in the range of about 140° C. to about 180° C.

8. The process of claim 6 wherein said step of recovering metal values from said residue comprises recovering at least one precious metal from said residue.

9. The process of claim 6 wherein said step of pressure leaching at least a portion of said feed stream in the presence of a dispersant comprises pressure leaching at least a portion of said feed stream in the presence of a sufficient amount of ground sand or mineral processing tailings.

10. A process for recovering metal values from an elemental sulfur-bearing solid residue of a pressure leaching process carried out at a temperature in the range of about 140° C. to about 180° C., the process comprising the steps of:

a) comminuting the elemental sulfur-bearing solid residue from the pressure leaching process carried out at a temperature in the range of about 140° C. to about 180° C. to produce a feed material;

b) forming a feed slurry by combining said feed material with a dispersant and a sufficient amount of fluid medium;

c) pressure leaching at least a portion of said feed slurry at a temperature in the range of about 220° C. to about 275° C. in an oxygen-containing atmosphere to yield a pressure leach product slurry comprising a sulfuric acid solution;

d) reducing the temperature and pressure of said product slurry;

e) separating at least a portion of said sulfuric acid solution from said product slurry to yield a solid residue;

f) recovering at least one metal value from said solid residue.

11. The process of claim 10 wherein said step of recovering at least one metal value from said solid residue comprises recovering one or more precious metals contained in said residue.

12. The process of claim 10 wherein said step of reducing the temperature and pressure of said product slurry comprises flashing said product slurry.

13. The process of claim 10 , said process further comprising the step of utilizing at least a portion of said sulfuric acid solution in connection with other processing operations.

14. The process of claim 10 wherein said step of pressure leaching at least a portion of said feed slurry is conducted at a temperature in the range in excess of about 235° C.

15. The process of claim 10 wherein said step of forming a feed slurry comprises combining said feed material with a sufficient amount of ground sand or mineral processing tailings.

16. A process for the production of sulfuric acid and recovery of precious metals from an elemental sulfur-bearing material comprising the steps of:

a) providing an elemental sulfur-bearing material, wherein said elemental sulfur-bearing material comprises an elemental sulfur-containing residue from a pressure leaching operation;

b) pressure leaching said elemental sulfur-bearing material at a temperature in the range of about 220° C. to about 275° C. in an oxygen-containing atmosphere in an, agitated multiple-compartment pressure leaching vessel to form a product slurry comprising a sulfuric acid solution;

c) adding a dispersant during said pressure leaching step;

d) separating at least a portion of said sulfuric acid solution from said product slurry to yield a solid residue;

e) recovering at least one precious metal value from said solid residue.

17. The process of claim 16 wherein said step of providing an elemental sulfur-bearing material comprises providing an elemental sulfur-containing residue from a pressure leaching operation carried out at a temperature in the range of about 140° C. to about 180° C.

18. The process of claim 16 wherein said step of pressure leaching comprises pressure leaching at a temperature of about 235° C.

Assignments (3)
CHANGE OF NAME Recorded Jul 23, 2014
From: FREEPORT-MCMORAN CORPORATION
To: FREEPORT MINERALS CORPORATION
Reel/Frame 033389/0300 →
MERGER Recorded Jul 17, 2014
From: FREEPORT-MCMORAN CORPORATION
To: FREEPORT-MCMORAN CORPORATION
Reel/Frame 033357/0849 →
CHANGE OF NAME Recorded Jul 30, 2009
From: PHELPS DODGE CORPORATION
To: FREEPORT-MCMORAN CORPORATION
Reel/Frame 023015/0851 →