High ammonia storage capacity SCR catalysts
AssigneeBASF Mobile Emissions Catalysts LLC
InventorsEdgar Viktor Huennekes, Petra Cordes, Jan Martin Becker, Kevin Beard, Nicholas McGuire, Jaya L Lakshmi, John K Hochmuth, Joseph A Patchett, Kenneth E Voss
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Abstract
The present invention relates to a catalyst for the selective catalytic reduction of nitrogen oxide, the catalyst comprising a first coating comprising a 12-membered ring pore zeolitic material comprising a first metal which is one or more of copper and iron, and a second coating comprising an 8-membered ring pore zeolitic material comprising a second metal which is one or more of copper and iron.
Claims16
A catalyst for selective catalytic reduction of nitrogen oxide comprising:
- (i) a substrate comprising an inlet end, an outlet end, a substrate axial length extending from the inlet end to the outlet end, and a plurality of passages defined by internal walls of the substrate extending therethrough;
- (ii) a first coating comprising a 12-membered ring pore zeolitic material comprising a first metal which is one or more of copper and iron, wherein the 12-membered ring pore zeolitic material comprises the first metal in an amount of z1 weight-%, calculated as the weight of the first metal, calculated as CuO and Fe2O3, divided by the weight of the 12-membered ring pore zeolitic material comprising the first metal;
- (iii) a second coating comprising an 8-membered ring pore zeolitic material comprising a second metal which is one or more of copper and iron, wherein the 8-membered ring pore zeolitic material comprises the second metal in an amount of z2 weight-%, calculated as the weight of the second metal, calculated as CuO and Fe2O3, divided by the weight of the 8-membered ring pore zeolitic material comprising the second metal;
- wherein the first coating is disposed on the surface of the internal walls of the substrate, which surface defines the interface between the internal walls and the passages, and extends over x % of the substrate axial length from the inlet end toward the outlet end of the substrate, wherein x ranges from 10 to 75;
- wherein the second coating extends over y % of the substrate axial length from the outlet end toward the inlet end of the substrate, wherein y ranges from 25 to 90;
- wherein the ratio z1:z2 is in the range of from 0.5:1 to 0.95:1.
A process for preparing a catalyst for selective catalytic reduction of nitrogen oxide comprising:
- (1) providing a substrate comprising an inlet end, an outlet end, a substrate axial length extending from the inlet end to the outlet end, and a plurality of passages defined by internal walls of the substrate extending therethrough;
- (2) preparing a first mixture comprising water and a 12-membered ring pore zeolitic material comprising a first metal which is one or more of copper and iron, wherein the 12-membered ring pore zeolitic material comprises the first metal in an amount of z1 weight-%, calculated as the weight of the first metal, calculated as CuO and Fe2O3, divided by the weight of the 12-membered ring pore zeolitic material comprising the first metal;
- (3) disposing the first mixture obtained in (2) on the surface of the internal walls of the substrate provided in (1), over x % of the substrate axial length from the inlet end toward the outlet end of the substrate, wherein x ranges from 10 to 75;
- (4) drying the mixture-treated substrate obtained in (3), obtaining the substrate having a first coating disposed thereon;
- optionally calcining;
- (5) preparing a second mixture comprising water and a 8-membered ring pore zeolitic material comprising a second metal which is one or more of copper and iron, wherein the 8-membered ring pore zeolitic material comprises the second metal in an amount of z2 weight-%, calculated as the weight of the second metal, calculated as CuO and Fe2O3, divided by the weight of the 8-membered ring pore zeolitic material comprising the second metal;
- (6) disposing the second mixture obtained in (5) on the substrate having a first coating disposed thereon obtained in (4) over y % of the substrate axial length from the outlet end toward the inlet end of the substrate, wherein y ranges from 25 to 90;
- (7) drying the mixture-treated substrate obtained in (6), obtaining the substrate having the first coating and a second coating disposed thereon;
- and
- (8) calcining the substrate having the first coating and the second coating disposed thereon obtained in (7), obtaining the catalyst;
- wherein the ratio z1:z2 ranges from 0.5:1 to 0.95:1.
A catalyst for selective catalytic reduction of nitrogen oxide comprising:
- a substrate comprising an inlet end, an outlet end, a substrate axial length extending from the inlet end to the outlet end, and a plurality of passages defined by internal walls of the substrate extending therethrough, and
- a coating disposed on the surface of the internal walls of the substrate, which surface defines the interface between the internal walls and the passages,
- wherein the coating comprising a 12-membered ring pore zeolitic material comprising a first metal which is one or more of copper and iron, and the 12-membered ring pore zeolitic material comprises the first metal in an amount of z weight-%, calculated as the weight of the first metal, calculated as CuO and Fe2O3, divided by the weight of the 12-membered ring pore zeolitic material comprising the first metal,
- wherein the coating further comprises a 10-membered ring pore zeolitic material comprising a second metal which is one or more of copper and iron, wherein the 10-membered ring pore zeolitic material comprises the second metal in an amount of y weight-%, calculated as the weight of the second metal, calculated as CuO and Fe2O3, divided by the weight of the 10-membered ring pore zeolitic material comprising the second metal;
- and
- wherein y ranges from 0.5 to 9 and y<z.
Dependencies are inferred from the claim text.