Nitrous oxide removal catalysts for exhaust systems

US10634030B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10634030-B2
Application numberUS-201515532751-A
CountryUS
Kind codeB2
Filing dateDec 8, 2015
Priority dateDec 8, 2014
Publication dateApr 28, 2020
Grant dateApr 28, 2020

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Abstract

Official abstract text for this publication.

A nitrous oxide (N 2 O) removal catalyst composite is provided, comprising a N 2 O removal catalytic material on a substrate, the catalytic material comprising a rhodium (Rh) component supported on a ceria-based support, wherein the catalyst composite has a H 2 -consumption peak of about 100° C. or less as measured by hydrogen temperature-programmed reduction (H 2 -TPR). Methods of making and using the same are also provided.

First claim

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What is claimed: 1. A nitrous oxide (N 2 O) removal catalyst composite for an exhaust stream of an internal combustion engine comprising: a N 2 O removal catalytic material on a substrate, the catalytic material comprising a rhodium (Rh) component supported on a ceria-based support, wherein the catalytic material has a H 2 -consumption peak of about 100° C. or less as measured by hydrogen temperature-programmed reduction (H 2 -TPR) and is effective to decompose at least a portion of nitrous oxide (N 2 O) in the exhaust stream to nitrogen (N 2 ) and oxygen (O 2 ) or to reduce at least a portion of the N 2 O to N 2 and water, N 2 and carbon dioxide (CO 2 ), or N 2 , water, and CO 2 under conditions of the exhaust stream, and wherein the ceria-based support comprises ceria in an amount in the range of about 56 to about 100% by weight of the support on an oxide basis. 2. The N 2 O removal catalyst composite of claim 1 , wherein the H 2 -consumption peak after aging at 750° C. for 20 hours with 10 volume % water in air occurs at a lower temperature than the temperature of the H 2 -consumption peak of fresh catalytic material. 3. The N 2 O removal catalyst composite of claim 1 , wherein N 2 O removal activity of the catalytic material after aging at 750° C. for 20 hours with 10 volume % water is higher than N 2 O removal activity of fresh catalytic material. 4. The N 2 O removal catalyst composite of claim 1 , wherein the ceria-based support maintains about 90 to about 100% of its pore volume after aging at 750° C. for 20 hours with 10 weight % water in air. 5. The N 2 O removal catalyst composite of claim 1 , wherein the ceria-based support comprises about 90 to about 100 weight % CeO 2 and has a pore volume that is at least about 0.20 cm 3 /g. 6. The N 2 O removal catalyst composite of claim 1 , wherein the ceria-based support comprises a fresh surface area that is in the range of about 40 to about 200 m 2 /g. 7. The N 2 O removal catalyst composite of claim 1 , wherein the ceria-based support comprises a surface area that is in the range of about 20 to about 140 m 2 /g after aging at 750° C. for 20 hours with 10 weight % water in air. 8. The N 2 O removal catalyst composite of claim 1 , wherein the ceria has a crystallite size in the range of about 3 to about 20 nm measured by x-ray diffraction (XRD). 9. The N 2 O removal catalyst composite of claim 1 , wherein the ceria-based support comprise: an x-ray diffraction crystallite size ratio of aged material to fresh material of about 2.5 or less, where aging is at 750° C. for 20 hours with 10% H 2 O in air. 10. The N 2 O removal catalyst composite of claim 1 , wherein the ceria-based support further comprises a promoter comprising yttria, samaria, gadolinia, zirconia, or silica. 11. The N 2 O removal catalyst composite of claim 1 , wherein the rhodium component is present on the support in an amount in the range of about 0.01 to about 5% by weight of the support. 12. The N 2 O removal catalyst composite of claim 1 , wherein the rhodium component is present in an amount of about 0.04 to about 3% by weight of the support. 13. The N 2 O removal catalyst composite of claim 1 , wherein the rhodium component has a crystallite size of less than about 5 nm. 14. The N 2 O removal catalyst composite of claim 1 , wherein the rhodium component is loaded on the substrate in an amount in the range of about 1 to about 105 g/ft 3 . 15. The N 2 O removal catalyst composite of claim 1 , wherein the catalytic material further comprises an additional metal component. 16. The N 2 O removal catalyst composite of claim 15 , wherein the additional metal component comprises platinum (Pt), palladium (Pd), silver (Au), copper (Cu), or combinations thereof. 17. The N 2 O removal catalyst composite of claim 15 , wherein the catalytic material further comprises a metal oxide for promoting the Rh and/or additional metal component. 18. The N 2 O removal catalyst composite of claim 17 , wherein the metal oxide comprises ceria, praseodymia, yttria, samaria, or gadolinia. 19. The N 2 O removal catalyst composite of claim 1 , wherein the substrate comprises a monolithic substrate. 20. The N 2 O removal catalyst composite of claim 1 , wherein the substrate comprises a wall-flow filter. 21. The N 2 O removal catalyst composite of claim 1 for an exhaust stream of an internal combustion engine comprising: a N 2 O removal catalytic material in a washcoat on a substrate, the catalytic material comprising a rhodium (Rh) component supported on a ceria-based support and is effective to convert nitrous oxide (N 2 O) under conditions of the exhaust stream, wherein the ceria-based support comprises: about 90 to about 100 weight % CeO 2 ; a pore volume that is in the range of about 0.20 to about 0.40 cm 3 /g; a fresh surface area that is in the range of about 40 to about 200 m 2 /g; and an aged surface area that is in the range of about 20 to about 140 m 2 /g after aging at 750° C. for 20 hours with 10 weight % water in air. 22. An emissions treatment system for treatment of an internal combustion engine exhaust stream including hydrocarbons, carbon monoxide, and nitrogen oxides, the emission treatment system comprising: an exhaust conduit in fluid communication with the internal combustion engine via an exhaust manifold; a treatment catalyst; and the N 2 O removal catalyst composite of claim 1 . 23. The emissions treatment system of claim 22 , wherein the treatment catalyst comprises a precious metal on a high surface area refractory metal oxide support that is effective to oxidize hydrocarbons and/or carbon monoxide under conditions of the exhaust stream. 24. The emissions treatment system of claim 23 , wherein the treatment catalyst comprises a nitrogen oxides treatment catalyst selected from the group consisting of a three-way conversion (TWC) catalyst, a lean NOx trap (LNT), and a Selective Catalytic Reduction (SCR) catalyst. 25. The emissions treatment system of claim 24 , wherein the N 2 O removal catalyst composite is located downstream of the nitrogen oxides treatment catalyst. 26. The emissions treatment system of claim 24 , wherein the system is zoned and the nitrogen oxides treatment catalyst is in a front, upstream zone and the N 2 O removal catalyst composite is in a back, downstream zone. 27. The emissions treatment system of claim 24 , wherein the system is layered and the nitrogen oxides treatment catalyst is in an outer layer and the N 2 O removal catalytic material of the catalyst composite is in an inner layer. 28. The emissions treatment system of claim 24 , wherein the system is layered and the nitrogen oxides treatment catalyst is in an inner layer and the N 2 O removal catalytic material of the N 2 O catalyst composite is in an outer layer. 29. A method for treating exhaust gases comprising contacting a gaseous stream comprising hydrocarbons, carbon monoxide, and nitrogen oxides with the N 2 O removal catalyst composite of claim 1 . 30. The method of claim 29 , wherein N 2 O removal activity of the catalytic material after aging at 750° C. for 20 hours with 10 weight % water is higher than N 2 O removal activity of fresh catalytic material.

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What does patent US10634030B2 cover?
A nitrous oxide (N 2 O) removal catalyst composite is provided, comprising a N 2 O removal catalytic material on a substrate, the catalytic material comprising a rhodium (Rh) component supported on a ceria-based support, wherein the catalyst composite has a H 2 -consumption peak of about 100° C. or less as measured by hydrogen temperature-programmed reduction (H 2 -TPR). Methods of making and u…
Who is the assignee on this patent?
Basf Corp
What technology area does this patent fall under?
Primary CPC classification B01J21/06. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Apr 28 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 5 related publications on this page (citations in our corpus or others sharing the same primary CPC).