[특허]Catalytic reduction of NOx

Daimler AG

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특허 상세정보

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Catalytic reduction of NOx

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	F01N-003/00 F01N-003/02 F01N-003/20 B01D-053/94 F01N-003/18 F01N-003/10 F01N-003/32 F02B-037/16 F01N-003/035 F01N-013/00
출원번호	US-0250449 (2014-04-11)
등록번호	US-9073010 (2015-07-07)
우선권정보	GB-9802504.2 (1998-02-06)
발명자 / 주소	Andreasson, Anders Chandler, Guy Richard Goersmann, Claus Friedrich Warren, James Patrick
출원인 / 주소	Daimler AG
대리인 / 주소	Brummett TechLaw PLLC
인용정보	피인용 횟수 : 1 인용 특허 : 42

초록

A system for NOx reduction in combustion gases, especially from diesel engines, incorporates an oxidation catalyst to convert at least a portion of NO to NO2, particulate filter, a source of reductant such as NH3 and an SCR catalyst. Considerable improvements in NOx conversion are observed.

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1. A method comprising: (a) passing an exhaust gas from a diesel engine over an oxidation catalyst to provide an adjusted gas stream, the exhaust gas comprising a first content level by volume of NO, a first content level by volume of NO2, and particulate matter, and the adjusted gas stream comprising a second content level by volume of NO that is lower than the first content level of NO, and a second content level by volume of NO2;(b) passing the adjusted gas stream through a particulate trap that results in trapping at least a portion of the particulate matter on the particulate trap;(c) combusting a portion of the trapped particulate matter such that there is no significant accumulation of particulate matter in the particulate trap in the presence of the adjusted gas stream at a combustion temperature that is lower than the temperature necessary to combust the trapped particulate matter in the presence of the exhaust gas such that there is no significant accumulation of particulate matter in the particulate trap, to create a further adjusted gas stream comprising a third content level by volume of NO and a third content level by volume of NO2 that is lower than the second content level of NO2;(d) injecting a reductant fluid comprising urea into the further adjusted gas stream;(e) mixing the further adjusted gas stream with the injected reductant fluid to form a further adjusted gas stream mixed with reductant fluid; and(f) passing the further adjusted gas stream mixed with reductant fluid over an SCR catalyst to provide a final adjusted gas stream comprising a fourth content level by volume of NO and a fourth content level by volume of NO2;wherein the second content level of NO2 is sufficiently higher than the first content level of NO2 such that when a portion of the second content level of NO2 in the adjusted gas stream is consumed during the combustion of the at least a portion of the trapped particulate matter, the resulting third content level of NO2 is still sufficiently high for use with the SCR catalyst to provide the final adjusted gas stream where the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower than the total combined volume of the first content level of NO and the first content level of NO2, and the total combined volume of the fourth content level of NO with the fourth content level of NO2 is lower relative to the respective total combined volume of NO and NO2 in a final exhaust stream that would result from carrying out steps (b)-(f) starting with the exhaust gas instead of the adjusted gas stream. 2. The method of claim 1, wherein the diesel engine is a vehicle engine. 3. The method of claim 1, wherein the diesel engine is a heavy duty diesel truck engine. 4. The method of claim 1, wherein the diesel engine is a turbocharged heavy duty diesel truck engine. 5. The method of claim 4, further comprising cooling the further adjusted gas stream. 6. The method of claim 5, wherein the further adjusted gas stream is cooled by air supplied by the turbocharger. 7. The method of claim 1, wherein the oxidation catalyst converts less than all of the NO in the exhaust gas to NO2. 8. The method of claim 1, wherein the further adjusted gas stream mixed with reductant fluid is at least 225° C. when passed over the SCR catalyst, and the final adjusted gas stream has more than 90% less NOx content by volume than the exhaust gas. 9. The method of claim 8, wherein the final gas stream has at least 67% less particulate matter content by volume than the exhaust gas. 10. A method comprising: (a) passing an exhaust gas from a diesel engine over an oxidation catalyst to provide an adjusted gas stream, the exhaust gas comprising a first content level by volume of NO, a first content level by volume of NO2, and particulate matter, and the adjusted gas stream comprising a second content level by volume of NO that is lower than the first content level of NO, and a second content level by volume of NO2;(b) passing the adjusted gas stream through a particulate trap that results in trapping at least a portion of the particulate matter on the particulate trap;(c) combusting a portion of the trapped particulate matter in the presence of the adjusted gas stream to reduce a combustion temperature necessary to stop significant accumulation of particulate matter in the particulate trap relative to the combustion temperature of a portion of the particulate matter in the presence of the exhaust gas necessary to stop significant accumulation of particulate matter in the particulate trap, and to create a further adjusted gas stream comprising a third content level by volume of NO and a third content level by volume of NO2 that is lower than the second content level of NO2;(d) injecting a reductant fluid comprising urea into the further adjusted gas stream;(e) mixing the further adjusted gas stream with the injected reductant fluid to form a further adjusted gas stream mixed with reductant fluid; and(f) passing the further adjusted gas stream mixed with reductant fluid over an SCR catalyst to provide a final adjusted gas stream comprising a fourth content level by volume of NO and a fourth content level by volume of NO2;wherein the second content level of NO2 is sufficiently higher than the first content level of NO2 such that when a portion of the second content-level of NO2 in the adjusted gas stream is consumed during the combustion of the at least a portion of the trapped particulate matter, the resulting third content level of NO2 is still sufficiently high for use with the SCR catalyst to provide the final adjusted gas stream where the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower than the total combined volume of the first content level of NO and the first content level of NO2, and the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower relative to the respective total combined volume of NO and NO2 in a final exhaust stream that would result from carrying out steps (b)-(f) starting with the exhaust gas instead of the adjusted gas stream. 11. The method of claim 10, wherein the diesel engine is a vehicle engine. 12. The method of claim 10, wherein the diesel engine is a heavy duty diesel truck engine. 13. The method of claim 10, wherein the diesel engine is a turbocharged heavy duty diesel truck engine. 14. The method of claim 13, further comprising cooling the further adjusted gas stream. 15. The method of claim 14, wherein the further adjusted gas stream is cooled by air supplied by the turbocharger. 16. The method of claim 10, wherein the oxidation catalyst converts less than all of the NO in the exhaust gas to NO2. 17. The method of claim 13, wherein the further adjusted gas stream mixed with reductant fluid is at least 225° C. when passed over the SCR catalyst, and the final adjusted gas stream has more than 90% less NOx content by volume than the exhaust gas. 18. The method of claim 17, wherein the final gas stream has at least 67% less particulate matter content by volume than the exhaust gas. 19. A method comprising: (a) passing an exhaust gas from a diesel engine over an oxidation catalyst to provide an adjusted gas stream, the exhaust gas comprising a first content level by volume of NO, a first content level by volume of NO2, and particulate matter, and the adjusted gas stream comprising a second content level by volume of NO that is lower than the first content level of NO, and a second content level by volume of NO2;(b) passing the adjusted gas stream through a particulate trap that results in trapping at least a portion of the particulate matter on the particulate trap;(c) combusting a portion of the trapped particulate matter such that there is no significant accumulation of particulate matter in the particulate trap in the presence of the adjusted gas stream at a combustion temperature that is lower than the temperature necessary to combust the trapped particulate matter in the presence of the exhaust gas such that there is no significant accumulation of particulate matter in the particulate trap, to create a further adjusted gas stream comprising a third content level by volume of NO and a third content level by volume of NO2 that is lower than the second content level of NO2;(d) injecting a reductant fluid comprising urea into the further adjusted gas stream;(e) mixing the further adjusted gas stream with the injected reductant fluid to form a further adjusted gas stream mixed with reductant fluid; and(f) passing the further adjusted gas stream mixed with reductant fluid over an SCR catalyst to provide a final adjusted gas stream comprising a fourth content level by volume of NO and a fourth content level by volume of NO2;wherein the second content level of NO2 is sufficiently higher than the first content level of NO2 such that when a portion of the second content-level of NO2 in the adjusted gas stream is consumed during the combustion of the at least a portion of the trapped particulate matter, the resulting third content level of NO2 is still sufficiently high for use with the SCR catalyst to provide the final adjusted gas stream where the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower than the total combined volume of the first content level of NO and the first content level of NO2, and the total combined volume of the fourth content level of NO and the fourth content level of NO2 is lower relative to the respective total combined volume of NO and NO2 in a final exhaust stream that would result from carrying out steps (b)-(f) starting with the exhaust gas instead of the adjusted gas stream; andwherein the further adjusted gas stream mixed with reductant fluid is at least 225° C. when passed over the SCR catalyst, and the final adjusted gas stream has more than 90% less NOx content by volume and at least 67% less particulate matter content by volume than the exhaust gas. 20. The method of claim 19, wherein the diesel engine is a vehicle engine. 21. The method of claim 19, wherein the diesel engine is a heavy duty diesel truck engine. 22. The method of claim 19, wherein the diesel engine is a turbocharged heavy duty diesel truck engine. 23. The method of claim 22, further comprising cooling the further adjusted gas stream. 24. The method of claim 23, wherein the further adjusted gas stream is cooled by air supplied by the turbocharger. 25. The method of claim 19, wherein the oxidation catalyst converts less than all of the NO in the exhaust gas to NO2.

이 특허에 인용된 특허 (42)

이 특허를 인용한 특허 피인용횟수: 1

Kato, Naohiro; Dornhaus, Franz. Exhaust gas treatment system. USP2018059981251.

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Catalytic reduction of NOx

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Catalytic reduction of NOx

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