Method for reducing formation of CaSO4 and Fe2O3 containing deposits in a pressure oxidation autoclave and/or adjacent circuits during pressure oxidation of gold-containing ore

Patent metadata

Field	Value
Publication number	US-11535911-B2
Application number	US-201916666616-A
Country	US
Kind code	B2
Filing date	Oct 29, 2019
Priority date	Oct 29, 2019
Publication date	Dec 27, 2022
Grant date	Dec 27, 2022

Abstract

Formation of CaSO4 and Fe2O3 containing deposits is reduced in a pressure oxidation autoclave and/or adjacent circuits during pressure oxidation of gold-containing ore. The gold-containing ore is combined with water to create an aqueous slurry that is heated and introduced into the autoclave. The method includes providing a scale inhibitor that is free of an organic polymer and includes an inorganic phosphate according to formula (I), (XPO3)m, wherein X is Na, K, H, or combinations thereof, and m is at least about 6, an inorganic phosphate according to formula (II), Yn+2PnO3n+1, wherein Y is Na, K, H, an organic phosphonate; or combinations thereof, and n is at least about 6. The method includes the step of combining the scale inhibitor and at least one of the gold-containing ore, the water, and the aqueous slurry to reduce scale.

First claim

What is claimed is:

1. A method for reducing formation of CaSO 4 and Fe 2 O 3 containing deposits in a pressure oxidation autoclave and/or adjacent circuits during pressure oxidation of gold-containing ore, wherein the gold-containing ore is combined with water to create an aqueous slurry that is heated and introduced into the pressure oxidation autoclave, said method comprising:
providing a scale inhibitor that is free of an organic polymer and comprises;
an inorganic phosphate according to formula (I),
(XPO 3 ) m   (I)

wherein X is Na, K, H, or combinations thereof, and m is at least about 6,
an inorganic phosphate according to formula (II),
Y n+2 P n O 3n+1   (II)

wherein Y is Na, K, H, or combinations thereof, and n is at least about 6, or
an organic phosphonate (III); or
a combination thereof;

combining the scale inhibitor and at least one of the gold-containing ore, the water, and the aqueous slurry; and
contacting the combination of the scale inhibitor and at leas one of the gold-containing ore, the water, and the aqueous slurry with the pressure oxidation autoclave and/or adjacent circuits to reduce the formation of scale in the pressure oxidation autoclave and/or adjacent circuits.

2. The method of claim 1 , wherein the inorganic phosphate of formula (I) comprises sodium hexametaphosphate and wherein m of formula (I) is about 6.

3. The method of claim 1 , wherein the inorganic phosphate of formula (II) comprises sodium poly(phosphate) and wherein n of formula (II) is about 21.

4. The method of claim 1 , wherein the organic phosphonate (III) is bis(hexamethylenetriamine penta(methylene phosphonic acid)).

5. The method of claim 1 , wherein the organic phosphonate (III) comprises 2-phosphonobutane-1,2,4-tricarboxylic acid, 1-hydroxyethane-1,1-diphosphonic acid, bis(phosphonomethyl)aminotris(methylene phosphonic acid), hexamethylenediamine tetra(methylene phosphonic acid), diethylenetriamine penta(methylene phosphonic acid), or combinations thereof.

6. The method of claim 1 , further comprising the step of adding oxygen to the pressure oxidation autoclave to react with the aqueous slurry at a temperature of from about 150° C. to about 250° C. and at a pressure of about 10 bar to about 35 bar, and wherein the scale inhibitor is added to the aqueous slurry prior to introduction into the pressure oxidation autoclave.

7. The method of claim 1 , wherein the CaSO 4 and Fe 2 O 3 containing deposit is reduced by at least 15% percent as compared to a control sample that is free of the scale inhibitor.

8. The method of claim 7 wherein the scale reduction is observed on at least one of a surface of a chamber of the autoclave, a slurry feed valve, a slurry discharge valve, a pump isolation valve, a depressurization valve, and/or attached piping.

9. A composition for reducing CaSO 4 and Fe 2 O 3 containing deposit in a pressure oxidation autoclave and/or adjacent circuits during pressure oxidation of gold-containing ore, said composition comprising:
an aqueous slurry of the gold-containing ore and water; and
a scale inhibitor that is free of an organic polymer and comprises;
an inorganic phosphate according to formula (I),
(XPO 3 ) m   (I)

wherein X is Na, K, H, or combinations thereof, and m is at least about 6,
an inorganic phosphate according to formula (II),
Y n+2 P n O 3n+1   (II)

wherein Y is Na, K, H, or combinations thereof, and n is at least about 6,
an organic phosphonate (III); or
a combination thereof.

10. The composition of claim 9 , wherein the inorganic phosphate of formula (I) comprises sodium hexametaphosphate and wherein m of formula (I) is about 6.

11. The composition of claim 9 , wherein the inorganic phosphate of formula (II) comprises sodium poly(phosphate) and wherein n of formula (II) is about 21.

12. The composition of claim 9 , wherein the organic phosphonate is bis-(hexamethylene-triamine penta (methylene phosphonic acid)).

13. The composition of claim 9 , wherein the organic phosphonate (III) comprises 2-phosphonobutane-1,2,4-tricarboxylic acid, 1-hydroxyethane-1,1-diphosphonic acid, bis(phosphonomethyl)aminotris(methylene phosphonic acid), hexamethylenediamine tetra(methylene phosphonic acid), diethylenetriamine penta(methylene phosphonic acid), or combinations thereof.

14. A system for reducing formation of CaSO 4 and Fe 2 O 3 containing deposit in a pressure oxidation autoclave and/or adjacent circuits during pressure oxidation of gold-containing ore, said system comprising:
a substrate of the pressure oxidation autoclave and/or adjacent circuits having a surface in contact with at least one of the gold-containing ore and/or an aqueous slurry of the gold-containing ore and water; and
a scale inhibitor that is disposed in the pressure oxidation autoclave and/or adjacent circuits, that is free of an organic polymer, and comprises;
an inorganic phosphate according to formula (I),
(XPO 3 ) m   (I)

wherein X is Na, K, H, or combinations thereof, and m is at least about 6,
an inorganic phosphate according to formula (II),
Y n+2 P n O 3n+1   (II)

wherein Y is Na, K, H, or combinations thereof, and n is at least about 6,
an organic phosphonate (III); or
a combination thereof;

wherein the system comprising the scale inhibitor exhibits a reduced formation of the CaSO 4 and Fe 2 O 3 containing deposit on the surface as compared to a system free of the scale inhibitor.

15. The system of claim 14 , wherein the inorganic phosphate of formula (I) comprises sodium hexametaphosphate and wherein m of formula (I) is about 6.

16. The system of claim 14 , wherein the inorganic phosphate of formula (II) comprises sodium poly(phosphate) and wherein n of formula (II) is about 21.

17. The system of claim 14 , wherein the surface is a surface of a pressure oxidation autoclave.

18. The system of claim 14 , wherein the inorganic phosphate of formula (I) comprises sodium hexametaphosphate and wherein m of formula (I) is about 6 and wherein the inorganic phosphate of formula (II) comprises sodium poly(phosphate) and wherein n of formula (II) is about 21.

19. The system of claim 14 , wherein the organic phosphonate is bis-(hexamethylene-triamine penta (methylene phosphonic acid)).

20. The system of claim 14 , wherein the organic phosphonate (III) comprises the organic phosphonate (III) comprises 2-phosphonobutane-1,2,4-tricarboxylic acid, 1-hydroxyethane-1,1-diphosphonic acid, bis(phosphonomethyl)aminotris (methylene phosphonic acid), hexamethylenediamine tetra(methylene phosphonic acid), diethylenetriamine penta(methylene phosphonic acid), or combinations thereof.

Assignees

• Solenis Tech Lp

Inventors

• Bakeev Kirill N
• Dimaio Andrew M

Classifications

• C22B3/00

  Extraction of metal compounds from ores or concentrates by wet processes · CPC title

• C02F5/086 Primary

  Condensed phosphates · CPC title

• C02F2101/203

  Iron or iron compound · CPC title

• C02F2103/16

  from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes · CPC title

• C22B11/04 Primary

  by wet processes (extraction of metal compounds by leaching in organic solutions C22B3/16; treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title