Composition and method for oxidizing mercury in combustion processes

• US 7,413,719 B2
• Filed: 03/26/2007
• Issued: 08/19/2008
• Est. Priority Date: 10/01/2004
• Status: Expired due to Fees

• Current Assignee: William Troy Digdon
• Original Assignee: William Troy Digdon
• Inventors: Digdon, William Troy
• Primary Examiner(s): Vanoy; Timothy C
• Application Number:
  US11/691,090
• Publication Number:
  US 20070212296A1
• Time in Patent Office: 512 Days
• Field of Search: 423/210, 423/594.18, 431/2
• US Class Current: 423/210
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury
• CPC Class Codes: B01J 20/12 Naturally occurring clays or bleaching earth
• CPC Class Codes: B01J 20/16 Alumino-silicates B01J20/12 takes precedence
• CPC Class Codes: F23J 2215/60 Heavy metals; Compounds thereof
• CPC Class Codes: F23J 7/00 Arrangement of devices for supplying chemicals to fire

Abstract

The invention can be summarized as follows. There is provided a method for oxidizing elemental mercury in a combustion process comprising, adding a composition comprising an aluminum silicate to a combustion chamber, boiler or kiln downstream from the burner region combustion zone. There is further provided a method for reducing the emission of one or more heavy metals in a combustion process by adding a composition comprising an aluminum silicate to a combustion chamber downstream from the burner region combustion zone. There is also provided a composition comprising an aluminum silicate that may be employed to oxidize elemental mercury generated in a combustion process. The composition also may be employed to reduce the emission of one or more heavy metals generated in a combustion process.

Claims

1. A method for converting elemental mercury to oxidized mercury in a combustion process that comprises,

adding a composition comprising bentonite to a combustion chamber, boiler or kiln downstream from the burner region combustion zone at a temperature greater than about 500°

C.

2. The method of claim 1, wherein said bentonite comprises a sodium bentonite.

3. The method of claim 2, wherein said sodium bentonite has a crystalline structure that is swellable and that exhibits colloidal properties.

4. The method of claim 3, wherein said bentonite further comprises one or more of the following characteristics:

SiO₂ from about 51 to about 78wt %,

Al₂O₃ from about 13 to about 23wt %,

Fe₂O₃ from about 1 to about 5wt %,

MgO from about 2 to about 3wt %,

CaO from about 0.1 to 3.0wt %,

Na₂O from about 1 to about 3wt %,

K₂O from about 0 to about 2wt %,

TiO from about 0 to about 0.5wt %,

FeO from about 0 to 0.5wt %;

Moisture;

less than about 12%;

pH about 8 to about 11 at 5% solids;

Specific Gravity;

about 2 to 3;

Sodium;

about 60 to about 65 mEq/100 g;

Calcium;

about 10 to about 30 mEq/100 g;

Magnesium;

about 5 to about 20 mEq/100 g;

or

Potassium;

about 1 to about 5 mEq/100 g.

5. The method of claim 4, wherein said bentonite additionally comprises one or more of the following characteristics:

Viscosity about 180bbl. Untreated;

Sieve about 20% max on 8 mesh;

Sieve about 20% max passing 20 mesh;

Free Swell about 27 ml minimum;

Brightness about 55 to about 65 GE units;

or

Waterplate about 500 to about 800.

6. The method of claim 1, wherein said combustion process comprises one or more fuels selected from the group consisting of oil, coal, solid wastes, biomedical wastes, wax, lignocellulosic material, wood, black liquor, red liquor or a combination thereof.

7. The method of claim 6, wherein the fuel employed in the combustion process is coal.

8. The method of claim 1, wherein downstream of said burner region combustion zone are one or more afterburners, cyclones, filters, heat exchangers, fabric filters, baghouses, electrostatic precipitators, wet scrubbers, emission stacks or a combination thereof.

9. The method of claim 8, wherein downstream of the burner region combustion zone is one or more wet scrubbers.

10. The method of claim 1, wherein said composition comprising bentonite is added to the combustion process in a region of the boiler that exhibits a temperature of between about 500°

C. and about 1300°

C.

11. The method of claim 1, wherein said composition comprising bentonite is added at a ratio (bentonite:

fuel ash content) of from about 0.00001;

1 (w/w) to about 1;

1 (w/w).

12. The method of claim 1, wherein said composition comprising bentonite comprises a particle size in the range of about 90 mesh to about 400 mesh.

13. The method of claim 1, wherein the bentonite is blown into the combustion chamber, boiler or kiln downstream from the burner region combustion zone.

14. The method of claim 1 further comprising a step of adding a composition comprising bentonite to the combustion chamber, boiler or kiln upstream or at the burner region combustion zone, wherein the upstream and downstream additions of bentonites occur simultaneously.

15. The method of claim 14, wherein said bentonites are sodium bentonites.

16. The method of claim 15, wherein the bentonites are different.