Method of removing a metal from a stream of hot gas

• US 5,897,688 A
• Filed: 04/18/1997
• Issued: 04/27/1999
• Est. Priority Date: 04/18/1997
• Status: Expired due to Term

• Current Assignee: Minplus B.V.
• Original Assignee: B. V. Cdem Holland
• Inventors: Voogt, Nicolaas, Biermann, Joseph Jan Peter
• Primary Examiner(s): SPITZER, ROBERT H
• Application Number:
  US08/844,268
• Time in Patent Office: 739 Days
• Field of Search: 95/133, 95/134, 423/89, 423/99, 423/107, 423/108, 423/210, 423/244.05
• US Class Current: 95/133
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury

Abstract

The present invention relates to a method of removing a metal from a stream of hot gas, wherein a particulate material comprising calcium and aluminum-silicate is contacted in the hot gas to absorb metal present in the hot gas. According to the invention, a meta-kaolin-containing substance is introduced in the hot gas, said meta-kaolin-containing substance being formed by thermally converting a material chosen from the group of I) waste paper, and ii) residue from the paper industry. The invention may be used to remove metals before, during or after the combustion or gasification of fossil fuels, biomass and organic waste.

Claims

1. In a method of removing a metal from a stream of hot gas containing metal in the gaseous phase, wherein an aluminum-silicate compound and a calcium compound are contacted with the hot gas containing metal in the gaseous phase to absorb the metal, the improvement comprising using particles containing both calcium and aluminum-silicate to contact the hot gas containing metal in the gaseous phase, said particles comprising meta-kaolin and said particles formed by thermal conversion of a material selected from the group consisting of waste paper and residue from the paper industry.

2. The method of claim 1, wherein the hot gas has a temperature between 850 and 1400°

C.

3. The method of claim 1, wherein the particles containing meta-kaolin are contacted with the hot gas having a temperature of at least 1000°

C.

4. The method of claim 1, wherein at least 90% by weight of the particles comprising meta-kaolin have a diameter of at least 2 μ

m and wherein the particles comprising meta-kaolin are contacted with the hot gas at a temperature of less than 1000°

C.

5. The method of claim 1, wherein the particles comprising meta-kaolin are formed by thermal conversion in a fluidized bed.

6. The method of claim 5, wherein the fluidized bed has a free board and wherein the free board is kept below 850°

C.

7. The method of claim 5, wherein the fluidized bed has a free board and wherein the free board is kept below 800°

C.

8. The method of claim 5, wherein the particles comprising a diameter of at least 0.5 mm are used in a reactor selected from the group consisting of a fluidized bed reactor and a fixed bed reactor.

9. The method of claim 5, wherein the particles comprising meta-kaolin have a diameter of at least 0.5 mm and wherein the particles further comprise a core material coated with the meta-kaolin containing material and wherein the particles may be used in a reactor selected from the group consisting of a fluidized bed reactor and a fixed bed reactor.

10. The method of claim 1, wherein the metal is a heavy metal.

11. Metal-containing particles formed by the method of claim 1.

12. Metal-containing particles formed by the method of claim 2.

13. Metal-containing particles formed by the method of claim 3.

14. Metal-containing particles formed by the method of claim 4.

15. Metal-containing particles formed by the method of claim 5.

16. Metal-containing particles formed by the method of claim 6.

17. Metal-containing particles formed by the method of claim 7.

18. Metal-containing particles formed by the method of claim 8.

19. Metal-containing particles formed by the method of claim 9.

20. Metal-containing particles formed by the method of claim 10.