Methods and devices for reducing hazardous air pollutants

• US 8,506,916 B2
• Filed: 07/27/2012
• Issued: 08/13/2013
• Est. Priority Date: 09/19/2007
• Status: Active Grant

• Current Assignee: C-Quest Technology LLC
• Original Assignee: C-Quest Technologies LLC
• Inventors: Comrie, Douglas C.
• Primary Examiner(s): Olsen, Kaj K
• Assistant Examiner(s): WOOD, JARED M
• Application Number:
  US13/559,719
• Publication Number:
  US 20120288428A1
• Time in Patent Office: 382 Days
• Field of Search: 951/29, 951/37, 961/21, 961/23, 961/31, 961/33, 961/38, 961/50, 961/51, 502/407, 502/445, 423/244.07, 423/242.1, 423/244.01
• US Class Current: 423/230
• CPC Class Codes: B01D 2251/404 of calcium
• CPC Class Codes: B01D 2253/106 Silica or silicates
• CPC Class Codes: B01D 2257/2045 Hydrochloric acid
• CPC Class Codes: B01D 2257/2064 Chlorine
• CPC Class Codes: B01D 2257/2066 Fluorine
• CPC Class Codes: B01D 2257/302 Sulfur oxides
• CPC Class Codes: B01D 2257/404 Nitrogen oxides other than dinitrogen oxide
• CPC Class Codes: B01D 2257/502 Carbon monoxide
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2257/602 Mercury or mercury compounds
• CPC Class Codes: B01D 2257/708 Volatile organic compounds V.O.C.'s
• CPC Class Codes: B01D 53/02 by adsorption, e.g. preparative gas chromatography solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01
• CPC Class Codes: B01D 53/508 by treating the gases with solids
• CPC Class Codes: B01D 53/565 by treating the gases with solids
• CPC Class Codes: B01D 53/62 Carbon oxides
• CPC Class Codes: Y02C 20/40 of CO2
• CPC Class Codes: Y02E 20/32 Direct CO2 mitigation

Abstract

The disclosure provides methods and systems for sequestering and/or reducing sulfur oxides, nitrogen oxides and/or carbon dioxide present in industrial effluent fluid streams. A solid particulate material comprising a slag component, a binder component (distinct from the slag component), and optionally water is formed and then contacted with the effluent fluid stream to reduce at least one of the sulfur oxides, nitrogen oxides, and/or carbon dioxide. The contacting of the effluent stream may occur in a packed bed reactor with the solid dry particulate material. Methods of reducing pollutants from exhaust generated by combustion sources, lime and/or cement kilns, iron and/or steel furnaces, and the like are provided.

Claims

1. A method of removing sulfur oxides and carbon dioxide from an effluent stream, the method comprising:

contacting the effluent stream comprising sulfur oxides and carbon dioxide with a substantially dry solid material formed by admixing a slag component having one or more reactive silicate compounds with a binder component, wherein the slag component comprises silicon dioxide at greater than or equal to about 25% by weight, and wherein greater than or equal to about 70% of an initial amount of sulfur oxides present in the effluent stream prior to the contacting are removed and greater than or equal to about 20% of an initial amount of carbon dioxide present in the effluent stream prior to the contacting is removed after the contacting with the substantially dry solid material;

monitoring the amount of sulfur oxides and carbon dioxide present in the effluent stream after the contacting; and

comparing the amount of at least one of the sulfur oxides or carbon dioxide present in the effluent stream after the contacting to a predetermined set point amount for at least one of carbon dioxide or sulfur oxides, wherein when the amount of monitored sulfur oxides or carbon dioxide after the contacting exceeds the predetermined set point amount, replacing the substantially dry solid material with new substantially dry solid material.

2. The method according to claim 1, wherein the effluent stream is generated by an industrial process and the effluent stream further comprises one or more additional air pollutants selected from the group consisting of:

nitrogen oxides, carbon monoxide, chlorofluorocarbons, hydrochloric acid, particulate matter, volatile organic compounds, aerosol compounds, mercury, lead, ammonia, and ozone, wherein the contacting with the substantially dry solid material also reduces an amount of at least one of the one or more additional air pollutants in the effluent stream.

3. The method according to claim 1, wherein the effluent stream further comprises nitrogen oxides, wherein greater than or equal to about 20% of an initial amount of nitrogen oxides present in the effluent stream prior to the contacting are removed by the contacting with the substantially dry solid material.

4. The method according to claim 1, wherein the effluent stream has a flow rate of greater than or equal to about 10,000 actual ft³/min (about 285 m³/min) to less than or equal to about 3,000,000 actual ft³/min (about 85,000 m³/min).

5. The method according to claim 1, wherein prior to the contacting, the effluent stream has a temperature of less than or equal to about 600°

F. (about 316°

C.).

6. The method according to claim 1, wherein the binder component comprises one or more materials selected from the group consisting of:

Portland cement, cement clinker, molasses, guar gum, starch, and combinations thereof, and the slag component comprises one or more materials selected from the group consisting of;

carbon slag, air cooled blast furnace slag, granulated blast furnace slag, ground granulated blast furnace slag, expanded and/or pelletized blast furnace slag, basic oxygen furnace steel slag, open hearth furnace steel slag, electric arc furnace steel slag, and combinations thereof.

7. The method according to claim 1, wherein the slag component comprises stainless steel slag and the binder component comprises Portland cement and/or cement clinker.

8. The method according to claim 1, wherein the substantially dry solid material further comprises a third component comprising a source of calcium oxide and a source of alkali metal ions comprising free lime (free CaO) at greater than or equal to about 3% by weight and Na₂O, K₂O, or combinations thereof at greater than or equal to about 1% by weight.

9. The method according to claim 1, wherein a ratio of the slag component to the binder component in the substantially dry solid material is about 6:

1 to about 99;

1 on a dry basis.

10. The method according to claim 1, wherein the effluent stream is generated by a combustion source selected from the group consisting of:

a boiler, an incinerator, a cement kiln, a lime kiln, an iron furnace, a steel furnace, and combinations thereof.

11. A method of removing sulfur oxides and carbon dioxide from an effluent stream, the method comprising:

contacting the effluent stream comprising sulfur oxides and carbon dioxide with a substantially dry solid material formed by admixing a slag component having one or more reactive silicate compounds with a binder component and a third component comprising a source of calcium oxide and a source of alkali metal ions, the third component comprising free lime (free CaO) at greater than or equal to about 3% by weight and Na₂O, K₂O, or combinations thereof at greater than or equal to about 1% by weight, wherein the slag component comprises silicon dioxide at greater than or equal to about 25% by weight, wherein greater than or equal to about 80% of an initial amount of sulfur oxides present in the effluent stream prior to the contacting are removed and greater than or equal to about 30% of an initial amount of carbon dioxide present in the effluent stream prior to the contacting is removed by the contacting with the substantially dry solid material.

12. The method according to claim 11, wherein the effluent stream further comprises one or more additional air pollutants selected from the group consisting of:

nitrogen oxides, carbon monoxide, chlorofluorocarbons, hydrochloric acid, particulate matter, volatile organic compounds, aerosol compounds, mercury, lead, ammonia, and ozone, and wherein the contacting with the substantially dry solid material also reduces an amount of at least one of the one or more additional air pollutants in the effluent stream.

13. The method according to claim 11, where the effluent stream further comprises nitrogen oxides, wherein the nitrogen oxides present in the effluent stream are removed after the contacting to a removal efficiency of greater than or equal to about 20% in comparison to an initial amount of nitrogen oxides present in the effluent stream prior to the contacting.

14. A method of removing sulfur oxides and carbon dioxide from an effluent stream generated by an industrial process, the method comprising:

reducing an amount of sulfur oxides and carbon dioxide in the effluent stream generated by the industrial process selected from the group consisting of;

cement manufacturing, lime manufacturing, metal manufacturing, power generation, incineration, and combinations thereof, by contacting the effluent stream with a substantially dry solid material comprising a slag component having one or more reactive silicate compounds with a binder component, wherein the slag component comprises silicon dioxide at greater than or equal to about 25% by weight, wherein greater than or equal to about 70% of an initial amount of sulfur oxides present in the effluent stream prior to the contacting are removed and greater than or equal to about 20% of an initial amount of carbon dioxide present in the effluent stream prior to the contacting is removed by the contacting with the substantially dry solid material;

monitoring the amount of sulfur oxides and carbon dioxide present in the effluent stream after the contacting; and

comparing the amount of at least one of the sulfur oxides or carbon dioxide present in the effluent stream after the contacting to a predetermined set point amount for at least one of carbon dioxide or sulfur oxides, wherein when the amount of monitored sulfur oxides or carbon dioxide after the contacting exceeds the predetermined set point amount, replacing the substantially dry solid material with new substantially dry solid material.

15. The method according to claim 14, wherein after the contacting, greater than or equal to about 80% of the initial amount of sulfur oxides present in the effluent stream prior to the contacting are removed and greater than or equal to about 30% of the initial amount of carbon dioxide present in the effluent stream prior to the contacting is removed by the contacting with the substantially dry solid material.

16. The method according to claim 14, wherein the effluent stream is generated by one or more combustion sources in the industrial process selected from the group consisting of:

a furnace, an incinerator, a boiler, a kiln, and combinations thereof.

17. The method according to claim 14, wherein the effluent stream further comprises one or more additional air pollutants selected from the group consisting of:

nitrogen oxides, carbon monoxide, chlorofluorocarbons, hydrochloric acid, particulate matter, volatile organic compounds, aerosol compounds, mercury, lead, ammonia, and ozone, wherein the contacting with the substantially dry solid material also reduces an amount of at least one of the one or more additional air pollutants in the effluent stream.

18. The method according to claim 14, wherein the effluent stream further comprises nitrogen oxides, and greater than or equal to about 20% of an initial amount of nitrogen oxides present in the effluent stream prior to the contacting are removed by the contacting with the substantially dry solid material.

19. The method according to claim 14, wherein the binder component comprises one or more materials selected from the group consisting of:

Portland cement, cement clinker, molasses, guar gum, starch, and combinations thereof, and the slag component comprises one or more materials selected from the group consisting of;

carbon slag, air cooled blast furnace slag, granulated blast furnace slag, ground granulated blast furnace slag, expanded and/or pelletized blast furnace slag, basic oxygen furnace steel slag, open hearth furnace steel slag, electric arc furnace steel slag, and combinations thereof.

20. The method according to claim 14, wherein the effluent stream has a flow rate of greater than or equal to about 10,000 actual ft³/min (about 285 m³/min) to less than or equal to about 3,000,000 actual ft³/min (about 85,000 m³/min) and a temperature of less than or equal to about 600°

F. (about 316°

C.) prior to the contacting.

21. A method of removing sulfur oxides and carbon dioxide from an effluent stream, the method comprising:

contacting the effluent stream comprising sulfur oxides and carbon dioxide with a substantially dry solid material consisting essentially of;

a slag component having one or more reactive silicate compounds, wherein the slag component comprises silicon dioxide at greater than or equal to about 25% by weight;

a binder component; and

an optional third component comprising a source of calcium oxide and a source of alkali metal ions, the third component comprising free lime (free CaO) at greater than or equal to about 3% by weight and Na₂O, K₂O, or combinations thereof at greater than or equal to about 1% by weight,

wherein greater than or equal to about 70% of an initial amount of sulfur oxides present in the effluent stream prior to the contacting are removed and greater than or equal to about 20% of an initial amount of carbon dioxide present in the effluent stream prior to the contacting is removed after the contacting with the substantially dry solid material.

22. The method according to claim 21, wherein the binder component is selected from the group consisting of:

Portland cement, cement clinker, molasses, guar gum, starch, and combinations thereof.