Low temperature thermal upgrading of lateritic ores

• US 5,178,666 A
• Filed: 12/03/1991
• Issued: 01/12/1993
• Est. Priority Date: 12/03/1991
• Status: Expired due to Fees

• Current Assignee: Inco Limited (Caixa de Previdência Dos Funcionários Do Banco Do Brasil)
• Original Assignee: Inco Limited (Caixa de Previdência Dos Funcionários Do Banco Do Brasil)
• Inventors: Shi, Dingzhu, MacVicar, Douglas J., Warner, Anthony E. M., Doyle, Christopher D., Vahed, Ahmed, Diaz, Carlos M.
• Primary Examiner(s): ROSENBERG, PETER
• Application Number:
  US07/801,945
• Time in Patent Office: 406 Days
• Field of Search: 75/629
• US Class Current: 75/629
• CPC Class Codes: C22B 1/245 with carbonaceous material for the production of coked agglomerates

Abstract

This invention relates to a thermal upgrading process whereby nickel-containing limonite or limonite/saprolite blends are pelletized with requisite amounts of solid carbon reductant and a sulfure-bearing concentrating agent. The pellets are fed to a reactor where they are gradually heated, causing reduction of the metal values. The reduced pellets are then held in a "metallics growth zone" of the reactor at a temperature high enough to allow for liquid-phase migration of the metallics within the pellets but below the point at which the pellets become sticky. The metallics growth zone is provided with a carefully controlled combustion gas atmosphere equivalent to about 60-65% aeration of partial combustion of natural gas which prevents further reduction or re-oxidation and thus provides a good environment for metallic particle growth. After a sufficient retention time, the pellets are then rapidly cooled to prevent the disproportionation of wustite to magnetite. The cooled pellets are then ground and the magnetic fraction separated.

Claims

1. A process for concentrating nickel values contained in lateritic ores, comprising:

(a) forming agglomerates incorporating the ore, a solid reductant and a sulfur-bearing agent;

(b) feeding the agglomerates to a reaction vessel having a feed end and a discharge end, the discharge end having a burner for the partial combustion of a fossil fuel to thereby produce combustion gases, such that the agglomerates and the combustion gases flow counter-currently within the vessel to gradually heat the agglomerates to a final temperature as they pass through the vessel from the feed end towards the discharge end, whereby the iron and nickel values in the ore are selectively reduced;

(c) retaining the agglomerates in a metallics growth zone, the metallics growth zone being located adjacent the discharge end of the vessel and characterized by a generally constant final temperature and an atmosphere equivalent to the partial combustion of natural gas at between about 60-65% aeration, to prevent re-oxidation or further reduction, and to allow for the formation of distinct ferronickel particles;

(d) cooling the agglomerates in an inert atmosphere at a rate sufficient to substantially prevent the disproportionation of wustite to magnetite;

(e) grinding the agglomerates; and

(f) magnetically separating the magnetic fraction of the ground agglomerates.

2. The process of claim 1, wherein the lateritic ore is limonite or a limonite/saprolite blend.

3. The process of claim 2, wherein the aeration percentage is about 62-63%.

4. The process of claim 3, wherein the solid reductant is bituminous coal.

5. The process of claim 4, wherein bituminous coal is present at between 4-6 wt. %.

6. The process of claim 3, wherein the sulfur-bearing agent is present in amounts between 2-5 wt. % sulfur.

7. The process of claim 3, wherein the total residence time of the pellets within the furnace is about 3 hours.

8. The process of claim 3, wherein the pellets are heated to a final temperature of between 950°

-1150°

C. and held at such temperature for at least 40 minutes.

9. The process of claim 8, wherein the pellets are held at about 1000°

-1100°

C. for about 60 minutes.

10. The process of claim 3, wherein the pellets are cooled to 100°

C. in less than 60 minutes.

11. The process of claim 10, wherein the pellets are cooled in less than 30 minutes.

12. The process of claim 8, wherein the agglomerates are cooled to 100°

C. in less than 60 minutes.

13. The process of claim 9, wherein the agglomerates are cooled to 100°

C. in less than 60 minutes.

14. The process of claim 8, wherein the solid reductant is bituminous coal present at about 4-6 wt. % and the sulfur-bearing agent is present at about 2-5 wt. % sulfur.

15. The process of claim 9, wherein the solid reductant is bituminous coal present at about 4-6 wt. % and the sulfur-bearing agent is present at about 2-5 wt. % sulfur.

16. The process of claim 10, wherein the solid reductant is bituminous coal present at about 4-6 wt. % and the sulfur-bearing agent is present at about 2-5 wt. % sulfur.

17. The process of claim 11, wherein the solid reductant is bituminous coal present at about 4-6 wt. % and the sulfur-bearing agent is present at about 2-5 wt. % sulfur.

18. The process of claim 2, wherein the ferronickel particles formed have an iron/nickel weight ratio of from 3 to 6.

19. The process of claim 2, wherein the reduction reaction takes place substantially within the agglomerates.