Pyro-metallurgical process in a rotary kiln

Patent metadata

Field	Value
Publication number	US-12018345-B2
Application number	US-202117539728-A
Country	US
Kind code	B2
Filing date	Dec 1, 2021
Priority date	Dec 9, 2020
Publication date	Jun 25, 2024
Grant date	Jun 25, 2024

Abstract

A pyro-metallurgical process for producing a non-ferrous metal or a compound thereof, wherein a metal raw material is fed into a rotary kiln, the metal being one of arsenic (As), antimony (Sb), lead (Pb), cadmium (Cd), mercury (Hg), silver (Ag), tin (Sn), nickel (Ni), or zinc (Zn). The raw material is heated to produce a volatized material, in which the non-ferrous metal or compound thereof is produced from the volatized material. A magnesium-based additive is additionally fed to the rotary kiln in an amount of between 0.5 wt. % and 9.5 wt. % relative to the total weight of the raw material. The magnesium-based additive is heated together with the raw material to produce the volatized material and a solid product while also counteracting ring formation in the rotary kiln.

First claim

The invention claimed is:

1. A pyro-metallurgical process for producing at least one non-ferrous metal or a compound thereof; wherein said metal is selected from the group consisting of arsenic (As), antimony (Sb), lead (Pb), cadmium (Cd), mercury (Hg), silver (Ag), tin (Sn), nickel (Ni), and zinc (Zn), and wherein at least one raw material is fed into a rotary kiln, wherein said at least one raw material comprises at least said metal, and wherein said raw material is heated to produce a volatized material, in Which the non-ferrous metal or compound thereof is produced from the volatized material, in which process a magnesium-based additive, is additionally fed in the rotary kiln in an amount of between 0.5 wt. % and 9.5 wt. % relative to the total weight of said raw materials, which magnesium-based additive is heated together with said raw material to produce at least the volatized material and a solid product, thereby counteracting ring formation in the rotary kiln; and
wherein the additional feeding of the magnesium-based additive provide between 0.03 wt. % and 5.00 wt % of magnesium oxide in the solid product.

2. The process according to claim 1 , wherein the magnesium-based additive is additionally fed in the rotary kiln in an amount of between 3.0 wt. and 7.5 wt. % relative to the total weight of said raw materials.

3. The process according to claim 1 , wherein the magnesium-based additive is a compound comprising at least one magnesium salt or a composition comprising at least one magnesium salt, or a mixture thereof.

4. The process according to claim 1 , wherein the magnesium-based additive comprises at least one magnesium salt selected from the group consisting of magnesium carbonate, magnesium oxide, and magnesium hydroxide.

5. The process according to claim 1 , wherein the magnesium-based additive is a compound comprising at least one magnesium salt and at least one calcium salt, wherein the total amount of the at least one magnesium salt and the at least one calcium salt is more than 80.0 wt. % relative to the total weight of the composition, and wherein the magnesium salt content varies from 10.0 wt, % to 90.0 wt. %, relative to the total weight of the magnesium salt and the calcium salt.

6. The process according to claim 5 , wherein the magnesium-based additive is a dolomitic limestone comprising MgCO 3 and CaCO 3 , and wherein the total content of MgCO 3 and CaCO 3 is more than 95.0 wt. % relative to the total weight of the dolomitic limestone, and wherein the MgCO 3 content ranges from 20.0 wt. % to 45.0 wt. %, relative to the total weight of MgCO 3 and CaCO 3 .

7. The process according to claim 6 , wherein the magnesium-basal additive is a dolomite.

8. The process according to claim 1 , wherein the magnesium-based additive is a composition comprising at least one magnesium salt and at least one calcium salt, wherein the total amount of the at least one magnesium salt and the at least one calcium salt is more than 80.0 wt, % relative to the total weight of the composition, and wherein the magnesium salt content varies from 10.0 wt. % to 90.0 wt, % relative to the total weight of the magnesium salt and the calcium salt.

9. The process according to claim 1 , wherein the raw material is heated to produce the volatized material at a temperature of at least 900° C.

10. The process according to claim 1 , wherein at least one mincing agent is additionally fed in the rotary kiln.

11. The process according to claim 10 , wherein the at least one reducing agent is a carbonaceous material selected from the group consisting of coal, coke and anthracite.

12. The process according to claim 11 , wherein the reducing agent is fed into the rotary kiln in an amount of between 5.0 and 40.0 wt. % relative to the total weight of said at least one raw material.

13. The process according to claim 12 , wherein the raw material is an electric arc furnace (EAF) dust comprising zinc and compounds thereof in an amount between 7.0 wt. % and 40.0 wt. % as expressed in zinc oxide wt. %, relative to the weight of the EAF dust.

14. The process according to claim 1 , wherein the pyro-metallurgical process is a Waelz process for the production of non-ferrous metal or a compound thereof, chosen from the group consisting of zinc and lead and cadmium.

Assignees

• Lhoist Rech Et Developpement Sa

Inventors

• Saratovsky Ian
• Johnson Jr Wliiiam Edward

Classifications

• C22B19/38

  in rotary furnaces · CPC title

• C22B43/00

  Obtaining mercury · CPC title

• C22B30/04

  Obtaining arsenic {(extraction of metal compounds by leaching in organic solutions C22B3/16; treatment or purification of solutions by adsorption on solids C22B3/24, by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42)} · CPC title

• C22B30/02

  Obtaining antimony · CPC title

• C22B25/02

  by dry processes · CPC title