Zoned ammonia slip catalyst for use in combustion turbines
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
B01D-053/86
B01D-053/94
F01N-003/10
F01N-003/20
B01J-021/04
B01J-021/06
B01J-023/30
B01J-023/40
B01J-023/42
B01J-023/44
B01J-023/46
B01J-023/54
B01J-023/63
B01J-029/76
B01J-035/00
B01J-035/02
B01J-035/04
출원번호
US-0279661
(2016-09-29)
등록번호
US-10105692
(2018-10-23)
발명자
/ 주소
Andersen, Paul Joseph
Doura, Kevin
출원인 / 주소
Johnson Matthey Public Limited Company
인용정보
피인용 횟수 :
0인용 특허 :
26
초록▼
A catalytic article for treating an exhaust gas stream containing one or more of NOx, hydrocarbons, CO, SOx and ammonia from a combustion turbine comprises (a) a substrate having an inlet end and an outlet end defining an axial length; (b) an oxidation layer comprising an oxidation catalyst comprisi
A catalytic article for treating an exhaust gas stream containing one or more of NOx, hydrocarbons, CO, SOx and ammonia from a combustion turbine comprises (a) a substrate having an inlet end and an outlet end defining an axial length; (b) an oxidation layer comprising an oxidation catalyst comprising one or more noble metals, the oxidation layer being positioned on the substrate and covering the axial length of the substrate; and (c) an SCR layer comprising an SCR catalyst, the SCR layer being positioned on the oxidation layer and overlapping a portion of the oxidation layer, wherein the portion is less than 100%.
대표청구항▼
1. A catalytic article for treating an exhaust gas stream from a combustion turbine, comprising: (a) a substrate having an inlet end and an outlet end defining an axial length;(b) an oxidation layer comprising an oxidation catalyst comprising one or more noble metals, the oxidation layer being posit
1. A catalytic article for treating an exhaust gas stream from a combustion turbine, comprising: (a) a substrate having an inlet end and an outlet end defining an axial length;(b) an oxidation layer comprising an oxidation catalyst comprising one or more noble metals, the oxidation layer being positioned on the substrate and covering the axial length of the substrate; and(c) an SCR layer comprising an SCR catalyst, the SCR layer being positioned on the oxidation layer and overlapping a portion of the oxidation layer, wherein the portion is less than 100%,wherein the article is configured for treating an exhaust gas stream containing one or more of NOx, hydrocarbons, CO, SOx and ammonia from a combustion turbine. 2. The catalytic article of claim 1, wherein the SCR layer comprises a first SCR catalyst and a second SCR catalyst wherein the first SCR catalyst is different than the second SCR catalyst and the first SCR catalyst is located on an inlet side of the article relative to the second SCR catalyst. 3. The catalytic article of claim 2, wherein the first SCR catalyst and the second SCR catalyst differ based on SCR catalyst loading. 4. The catalytic article of claim 2, wherein a loading of the second SCR catalyst is higher than in the first SCR catalyst. 5. The catalytic article of claim 1, wherein the oxidation layer comprises a first oxidation catalyst and a second oxidation catalyst wherein the first oxidation catalyst is different than the second oxidation catalyst and the first oxidation catalyst is located on an inlet side of the article relative to the second oxidation catalyst. 6. The catalytic article of claim 1, further comprising a third catalyst coating, wherein the third catalyst coating extends from the outlet end toward the inlet end and the oxidation layer comprises an area that is not coated by the SCR layer or the third catalyst coating. 7. The catalytic article of claim 1, wherein the SCR layer covers 90% or less of the axial length of the substrate. 8. The catalytic article of claim 1, wherein the oxidation catalyst comprises a platinum group metal. 9. The catalytic article of claim 1, wherein the oxidation catalyst comprises platinum on a support with low ammonia storage. 10. The catalytic article of claim 1, wherein the oxidation layer further comprises an SCR catalyst, and the oxidation catalyst and the SCR catalyst in the oxidation layer are present as a blend. 11. The catalytic article of claim 1, wherein the article provides higher CO/HC conversion and reduced ammonia slip than a comparable article wherein the SCR layer completely overlaps the oxidation layer. 12. The catalytic article of claim 1, wherein the one or more noble metals are disposed on a refractory metal oxide support. 13. The catalytic article of claim 12, wherein the SCR catalyst comprises a molecular sieve or a metal-containing molecular sieve and the molecular sieve or the molecular sieve in the metal-containing molecular sieve comprises a Framework Type selected from the group consisting of: AEI, BEA (beta zeolite), CHA (Chabazite), FAU (zeolite Y), FER (ferrierite), MFI (ZSM-5) and MOR (mordenite). 14. The catalyst article of claim 12, wherein the metal supported on a mixed oxide comprises a catalytic composition containing at least one catalytic component consisting of (i) at least one transition metal dispersed on a mixed oxide or composite oxide or a mixture thereof as support material consisting of cerium and zirconium; or (ii) cerium oxide and zirconium oxide as single oxides or a composite oxide thereof or a mixture of the single oxides and the composite oxide dispersed on an inert oxide support material, wherein at least one transition metal is dispersed thereon, and the at least one transition metal is selected from the group consisting of a Group VIB metal, a Group IB metal, a Group IVA metal, a Group VB metal, a Group VIIB metal, a Group VIII metal and mixtures of any two or more thereof, provided that at least one selected transition metal is tungsten, and the content of cerium and zirconium as oxides in the catalytic component is CexZr1-xO2, wherein X−0.1-0.5. 15. The catalytic article of claim 1, wherein the SCR catalyst comprises a base metal, an oxide of a base metal, a molecular sieve, a metal-containing molecular sieve, a metal supported on a mixed oxide, or a mixture thereof. 16. The catalytic article of claim 15, wherein the base metal is selected from the group consisting of cerium, chromium, cobalt, copper, iron, manganese, molybdenum, nickel, tungsten, and vanadium, and mixtures thereof. 17. The catalytic article of claim 15, wherein the SCR catalyst comprises a metal-containing molecular sieve wherein the metal is selected from the group consisting of cerium, chromium, cobalt, copper, gallium, indium, iridium, iron, manganese, molybdenum, nickel, palladium, platinum, ruthenium, rhenium, silver, tin and zinc. 18. The catalytic article of claim 1, wherein the SCR catalyst comprises an aluminosilicate molecular sieve, an aluminophosphate molecular sieve, a silicoaluminophosphate molecular sieve, a metal-containing aluminosilicate molecular sieve, a metal-containing aluminophosphate molecular sieve, or a metal-containing silicoaluminophosphate molecular sieve. 19. A method of increasing the conversion of CO and HC in an exhaust gas from a combustion turbine, the method comprising contacting an exhaust gas comprising CO and HC with a catalytic article of claim 1. 20. A method of reducing ammonia slip in an exhaust gas from a combustion turbine, the method comprising contacting an exhaust gas comprising ammonia with a catalytic article of claim 1.
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