Compositions and methods for removing mercury from mercury-containing fluids

• US 7,858,061 B2
• Filed: 12/15/2005
• Issued: 12/28/2010
• Est. Priority Date: 12/15/2005
• Status: Active Grant

• Current Assignee: United States Environmental Protection Agency
• Original Assignee: United States Of America As Represented By The Administrator Of The United States Environmental Protection Agency
• Inventors: Sikdar, Subhas, Keener, Timothy C., Lee, Joo Youp, Varma, Rajender S., Ju, Yuhong
• Primary Examiner(s): Vanoy; Timothy C
• Assistant Examiner(s): Rump; Richard M
• Application Number:
  US11/300,879
• Publication Number:
  US 20070140940A1
• Time in Patent Office: 1,839 Days
• Field of Search: 502405-407, 502/410, 502/413, 588/313, 588/400, 588/412
• US Class Current: 423/215.5
• CPC Class Codes: B01D 2253/106 Silica or silicates
• CPC Class Codes: B01D 2257/602 Mercury or mercury compounds
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury

Abstract

Oxidative sorbents are provided for adsorbing elemental or oxidized mercury from mercury-containing fluids such as flue gas from a coal-burning power utility or the like at a temperature range of about 50 to 350° C. The method of preparing and using the oxidative sorbents is also provided. The oxidative sorbent compositions include one or more silicates capable of cation exchange with a plurality of active metal cations and their counter anions. The silicates may include those selected from clays such as montmorillonite, laumonite, bentonite, Mica, vermiculite and kaolinite, and from silica gels, natural and synthetic molecular sieves, zeolites, and ashes from stoker- and pulverized coal-fired boilers. The one or more oxidative metal halides and/or sulfates may be selected from the group consisting of CuCl, CuBr, CuCl₂, CuBr₂, CuSO₄, FeCl₂, FeCl₃, FeSO₄, Fe₂(SO₄)₃, ZnCl₂, ZnBr₂, NiCl₂, and NiSO₄. The oxidative sorbents may also include activated carbon.

Claims

1. An oxidative sorbent composition for the substantial removal of mercury from mercury-containing fluids comprising:

a matrix material selected from one or more silicates;

at least one metal halide impregnated in the matrix material for oxidizing Hg⁰ present in the mercury-containing fluids to one of Hg(I) and Hg(II); and

about 1% to about 30% activated carbon.

2. The oxidative sorbent composition of claim 1, wherein the at least one metal halide is selected from the group consisting of CuCl, CuBr, CuCl₂, CuBr₂, FeCl₂, FeCl₃, ZnCl₂, ZnBr₂, and NiCl₂.

3. The oxidative sorbent composition of claim 1, wherein the one or more silicates are selected from the group consisting of clays such as montmorillonite, laumonite, bentonite, mica, vermiculite and kaolinite, and from silica gels, natural and synthetic molecular sieves, zeolites, and ashes from stoker and pulverized coal-fired boilers.

4. The oxidative sorbent composition of claim 1, further comprising activated carbon.

5. The oxidative sorbent composition of claim 1, wherein the mercury-containing fluids comprise acidic flue gas.

6. The oxidative sorbent composition of claim 1, wherein the composition comprises about 1 to about 35% (wt) of at least one metal halide and from about 65 to about 99% (wt) matrix material.

7. The oxidative sorbent composition of claim 1, wherein the matrix material has a particle size range of about one to about 100 microns.

8. The oxidative sorbent composition of claim 7, wherein the matrix material has an average particle size of less than about 32 microns.

9. A method for preparation of an oxidative sorbent composition for use in substantially removing mercury from fluids, comprising the steps of:

contacting one or more silicates with at least one metal halide, wherein the at least one metal halide is in a solution, to make metal-impregnated silicates for oxidizing Hg⁰ to one of Hg (I) and Hg(II);

adding activated carbon to the metal-impregnated silicates; and

removing the solution from the oxidative sorbent composition;

wherein the at least one metal halide is selected from the group consisting of CuCl, CuBr, CuCl₂, CuBr₂, FeCl₂, FeCl₃, ZnCl₂, ZnBr₂, and NiCl₂; and

wherein the one or more silicates are selected from the group consisting of clays such as montmorillonite, laumonite, bentonite, Mica, vermiculite and kaolinite, and from silica gels, natural and synthetic molecular sieves, zeolites, and ashes from stoker—

and pulverized coal-fired boilers.

10. The method of claim 9, wherein the at least one metal halide is only CuCl₂.

11. The method of claim 9, wherein the one or more silicates is montmorillonite.

12. The method of claim 9, wherein the solution is an aqueous solution of about 6.25% to about 20% of the at least one metal halide in water.

13. The method of claim 9, wherein the solution is an acetone solution of about 6.25% to about 20% of the at least one metal halide in acetone.

14. The method of claim 9, wherein the one or more silicates have an average particle size ranging from about 1 to about 100 micrometers.

15. A method to capture mercury from mercury-containing fluid, comprising the steps of:

contacting the mercury-containing fluid with an oxidative sorbent, the oxidative sorbent comprising one or more silicates impregnated with at least one metal halide for oxidizing Hg⁰ to one of Hg(I) and Hg(II);

oxidizing Hg⁰ present in the mercury-containing fluid to one of Hg(I) and Hg(II) with the metal halide; and

capturing the Hg(I) and Hg(II) onto at least one of the silicates of the oxidative sorbent;

wherein the at least one metal halide is selected from the group consisting of CuCl, CuBr, CuCl₂, CuBr₂, FeCl₂, FeCl₃, ZnCl₂, ZnBr₂, and NiCl₂; and

wherein the one or more silicates are selected from the group consisting of clays such as montmorillonite, laumonite, bentonite, Mica, vermiculite and kaolinite, and from silica gels, natural and synthetic molecular sieves, zeolites, and ashes from stoker—

and pulverized coal-fired boilers.

16. The method of claim 15, wherein the oxidative sorbent further comprises activated carbon and wherein the silicate is montmorillonite clay and the metal halide is CuCl₂.

17. A method to capture mercury from a flue gas stream containing elemental and ionic mercury, comprising the steps of:

injecting a porous oxidative sorbent into the flue gas stream, wherein the porous oxidative sorbent comprises;

at least one metal halide selected from the group consisting of CuCl, CuBr, CuCl₂, CuBr₂, FeCl₂, FeCl₃, ZnCl₂, ZnBr₂, and NiCl₂ for oxidizing Hg⁰ to one of Hg(I) and Hg(II); and

a matrix material selected from one or more silicates selected from the group consisting of clays such as montmorillonite, laumonite, bentonite, Mica, vermiculite and kaolinite, and from silica gels, natural and synthetic molecular sieves, zeolites, and ashes from stoker—

and pulverized coal-fired boilers;

oxidizing Hg⁰ present in the flue gas stream to one of Hg(I) and Hg(II) with the metal halide;

capturing the oxidized mercury onto the porous oxidative sorbent when the oxidative sorbent is exposed to the flue gas stream; and

removing and disposing of the spent oxidative sorbent.

18. A process for treating the surface of one or more silicates for ion exchange comprising:

contacting the surface of montmorillonite clay with CuCl₂ in acetone solution, wherein the CuCl₂ is used to oxidize Hg⁰ present in a flue gas stream to one of Hg(I) and Hg(II).