초록 ▼

The present invention provides compositions, systems, and methods for achieving high efficiencies of nitrogen oxide (NOx) removal from exhaust gases while minimizing ammonia slip and sulfur dioxide oxidation. In one embodiment, a method of removing nitrogen oxides from an exhaust gas comprises provi

The present invention provides compositions, systems, and methods for achieving high efficiencies of nitrogen oxide (NOx) removal from exhaust gases while minimizing ammonia slip and sulfur dioxide oxidation. In one embodiment, a method of removing nitrogen oxides from an exhaust gas comprises providing a first catalyst layer, adding an ammonia-containing compound to the exhaust gas upstream of the first catalyst layer in excess of the stoichiometric equivalent of the nitrogen oxides in the exhaust gas, flowing the exhaust gas through the first catalyst layer, selectively catalytically decomposing ammonia in excess of the stoichiometric reaction equivalent of the nitrogen oxides in the exhaust gas, and catalytically reducing the nitrogen oxides by reaction with ammonia not selectively catalytically decomposed.

대표청구항 ▼

That which is claimed is: 1. A method of removing nitrogen oxides from an exhaust gas comprising: providing a first catalyst layer; adding an ammonia-containing compound to the exhaust gas upstream of the first catalyst layer in excess of the stoichiometric reaction equivalent of the nitrogen oxide

That which is claimed is: 1. A method of removing nitrogen oxides from an exhaust gas comprising: providing a first catalyst layer; adding an ammonia-containing compound to the exhaust gas upstream of the first catalyst layer in excess of the stoichiometric reaction equivalent of the nitrogen oxides in the exhaust gas; flowing the exhaust gas through the first catalyst layer; and selectively catalytically decomposing ammonia in excess of the stoichiornetric reaction equivalent of the nitrogen oxides in the exhaust gas at one or more points in the first catalyst layer; while catalytically reducing the nitrogen oxides by reaction with ammonia not selectively catalytically decomposed at one or more points in the first catalyst layer. 2. The method of claim 1, wherein at least 95% of the nitrogen oxides are removed from the exhaust gas exiting the first catalyst layer. 3. The method of claim 1, wherein at least 97% of the nitrogen oxides are removed from the exhaust gas exiting the first catalyst layer. 4. The method of claim 1, wherein less than about 5 ppmvd of ammonia exits the first catalyst layer. 5. The method of claim 1, wherein less than about 3 ppmvd of ammonia exits the first catalyst layer. 6. The method of claim 1, wherein less than about 2 ppmvd of ammonia exits the first catalyst layer. 7. The method of claim 1, wherein the exhaust gas further comprises an amount of sulfur trioxide and wherein flowing the exhaust gas through the first catalyst layer results in substantially no increase in the amount of sulfur trioxide. 8. The method of claim 1, wherein the first catalyst layer comprises at least one monolithic structural catalyst body formed from a uniform composition comprising 50-99.9% by weight an inorganic oxide composition and a catalytically active metal function group comprising ruthenium. 9. The method of claim 8, wherein the uniform composition comprises from 0.01% to 0.2% by weight of the catalytically active metal function group comprising ruthenium. 10. The method of claim 8, wherein the uniform composition comprises greater than 1% to about 5% by weight of the catalytically active metal function group comprising ruthenium. 11. The method of claim 8, wherein the monolithic structural catalyst body is coated with additional catalytic material. 12. The method of claim 8, wherein the monolithic structural catalyst comprises an outer peripheral wall and a plurality of inner partition walls formed of the uniform chemical composition. 13. The method of claim 12, wherein the catalytically active metal functional group further comprises vanadium pentoxide, tungsten oxide or molybdenum oxide or a mixture thereof. 14. The method of claim 13, wherein ruthenium is present in an amount ranging from about 0.2 weight percent to about 0.6 weight percent. 15. The method of claim 1, further comprising providing at least one additional nitrogen oxide reduction catalyst layer downstream of the first catalyst layer and flowing the exhaust gas through the at least one additional nitrogen oxide reduction catalyst layer. 16. The method of claim 15, wherein the monolithic structural catalyst body is coated with additional catalytic material. 17. The method of claim 15, wherein at least 95% of the nitrogen oxides are removed from the exhaust gas exiting the at least one additional nitrogen oxide reduction catalyst layer. 18. The method of claim 15, wherein at least 97% of the nitrogen oxides are removed from the exhaust gas exiting the at least one additional nitrogen oxide reduction catalyst layer. 19. The method of claim 15, wherein less than about 2 ppmvd of ammonia exits the at least one additional nitrogen oxide reduction catalyst layer. 20. A method of removing nitrogen oxides from an exhaust gas comprising: providing a first catalyst layer; adding an amount of ammonia-containing compound to the exhaust gas; flowing the exhaust gas through the first catalyst layer, wherein the amount of ammonia-containing compound added produces a NH3/NOx molar ratio in excess of equivalence at one or more points in the first catalyst layer; and selectively catalytically decomposing ammonia in excess of equivalence at the one or more points in the first catalyst layer; while catalytically reducing nitrogen oxides by reaction with ammonia not selectively catalytically decomposed. 21. The method of claim 20, wherein at least 95% of the nitrogen oxides are removed from the exhaust gas exiting the first catalyst layer. 22. The method of claim 20, wherein at least 97% of the nitrogen oxides are removed from the exhaust gas exiting the first catalyst layer. 23. The method of claim 20, wherein at least 99% of the nitrogen oxides are removed from the exhaust gas exiting the first catalyst layer. 24. The method of claim 20, wherein less than about 5 ppmvd of ammonia exits the first catalyst layer. 25. The method of claim 20, wherein less than about 3 ppmvd of ammonia exits the first catalyst layer. 26. The method of claim 20, wherein less than about 2 ppmvd of ammonia exits the first catalyst layer. 27. The method of claim 20, wherein the exhaust gas further comprises an amount of sulfur trioxide and wherein flowing the exhaust gas through the first catalyst layer results in substantially no increase in the amount of sulfur trioxide. 28. The method of claim 20, wherein the first catalyst layer comprises at least one monolithic structural catalyst body formed from a uniform composition comprising 50-99.9% by weight an inorganic oxide composition and a catalytically active metal function group comprising ruthenium. 29. The method of claim 28, wherein the uniform composition comprises from 0.01% to 0.2% by weight of the catalytically active metal function group comprising ruthenium. 30. The method of claim 28, wherein the uniform composition comprises greater than 1% to about 5% by weight of the catalytically active metal function group comprising ruthenium. 31. The method of claim 28, wherein the monolithic structural catalyst body is coated with additional catalytic material. 32. The method of claim 20, further comprising providing at least one additional nitrogen oxide reduction catalyst layer downstream of the first catalyst layer and flowing the exhaust gas through the at least one additional nitrogen oxide reduction catalyst layer. 33. The method of claim 32, wherein at least 97% of the nitrogen oxides are removed from the exhaust gas exiting the at least one additional nitrogen oxide reduction catalyst layer. 34. The method of claim 32, wherein at least 99% of the nitrogen oxides are removed from the exhaust gas exiting the at least one additional nitrogen oxide reduction catalyst layer. 35. The method of claim 32, wherein less than about 2 ppmvd of ammonia exits the at least one additional nitrogen oxide reduction catalyst layer.