System and method for two and three way mixed metal oxide ZPGM catalyst
US-9216408-B2 · Dec 22, 2015 · US
US2022010714A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022010714-A1 |
| Application number | US-202117483135-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 23, 2021 |
| Priority date | Dec 8, 2014 |
| Publication date | Jan 13, 2022 |
| Grant date | — |
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A nitrous oxide (N2O) removal catalyst composite is provided, comprising a N2O 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 H2-consumption peak of about 100° C. or less as measured by hydrogen temperature-programmed reduction (H2-TPR). Methods of making and using the same are also provided.
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1 - 21 . (canceled) 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 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. 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 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 (COO, or N 2 , water, and CO 2 under conditions of the exhaust stream. 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. 31 - 34 . (canceled)
characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title
Nanoparticles · CPC title
Compounds characterised by their crystallite size · CPC title
Coatings comprising several layers · CPC title
X-ray diffraction · CPC title
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