IP Library Granted Patent US 10,118,127
Granted Patent B2
US 10,118,127 · App. 15/425,448 · Granted Nov 6, 2018

Catalyst for treating exhaust gas

Inventors: Guy Richard Chandler (Royston, GB); Hai-Ying Chen (Wayne, PA); Jillian Elaine Collier (Royston, GB); Joseph Michael Fedeyko (Wayne, PA); Alexander Nicholas Michael Green (Royston, GB)
Assignee: Johnson Matthey Public Limited Company
B01D53/9418B01D53/9477B01J29/072B01J29/56B01J29/76B01J29/763B01J35/023B01J35/04B01J37/0215B01J37/0246B01J37/08B01J37/30F01N3/035F01N3/103F01N3/2066F01N3/2842G06F9/467G06F13/287G06F15/17331B01D2251/2062B01D2255/20761B01D2255/50B01D2255/904B01D2255/9155B01J35/0006B01J2229/186Y02C20/10
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Quick Facts
Patent No.
US 10,118,127
App. No.
15/425,448
Granted
Nov 6, 2018
Kind
B2
Abstract

Provided is a method for reducing N 2 O emissions in an exhaust gas comprising contacting an exhaust gas containing NH 3 and an inlet NO concentration with an SCR catalyst composition containing small pore zeolite having an SAR of about 3 to about 15 and having about 1-5 wt. % of an exchanged transition metal.

Claims (13)

1. A method for reducing N 2 O emissions in an exhaust gas comprising contacting an exhaust gas containing NH 3 and an inlet NO concentration with an SCR catalyst composition containing small pore zeolite having an AEI framework and an SAR of about 3 to about 15 and having about 1-5 wt. % of an exchanged transition metal to produce a purified gas containing an outlet NO concentration and an outlet N 2 O concentration,

a. wherein the inlet NO concentration and outlet NO concentration have a relative ratio of >about 4, and

b. wherein the inlet NO concentration and outlet N 2 O concentration have a relative ratio of >about 50.

2. The method of claim 1 , wherein the inlet NO concentration and outlet NO concentration have a relative ratio of >about 5.

3. The method of claim 1 , wherein the inlet NO concentration and outlet NO concentration have a relative ratio of >about 10.

4. The method of claim 1 , wherein the inlet NO concentration and outlet N 2 O concentration have a relative ratio of >about 80.

5. The method of claim 4 , wherein the inlet NO concentration and outlet N 2 O concentration have a relative ratio of >about 100.

6. The method of claim 1 , wherein the transition metal is copper.

7. The method of claim 1 , wherein the small pore zeolite has a SAR of about 5 to about 9.

8. The method of claim 1 , wherein the small pore zeolite has a SAR of about 10 to about 15.

9. The method of claim 1 , wherein the NO and NO 2 are present in a ratio of about 4:1 to about 1:3 by volume.

10. The method of claim 1 , wherein the NH 3 is present in exhaust gas entering the SCR catalyst at an NH 3 /NO ratio of about 0.5:1 to about 1:2 and an NH 3 /NO 2 ratio of about 1:1 to about 6:3.

11. A system for treating an exhaust gas comprising, in series and in fluid communication, a diesel oxidation catalyst, a source of nitrogen-based reductant, and an SCR catalyst, wherein the SCR catalyst comprises a small pore zeolite having an AEI framework and an SAR of about 3 to about 15 and having about 1-5 wt. % of an exchanged transition metal, and wherein the SCR catalyst is coated on a honeycomb wall-flow filter or flow-through monolith or is an extruded honeycomb body.

Assignments (2)
CHANGE OF ADDRESS Recorded Jan 14, 2026
From: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
To: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
Reel/Frame 074703/0733 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 8, 2017
From: FEDEYKO, JOSEPH MICHAEL; GREEN, ALEXANDER NICHOLAS MICHAEL; CHANDLER, GUY RICHARD; COLLIER, JILLIAN ELAINE; CHEN, HAI-YING
To: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
Reel/Frame 043232/0672 →
Continuity (3)
Continuation 14665051 · Mar 23, 2015
Provisional Application 61969350 · Mar 24, 2014
Related Publication 20170144105A1 · May 25, 2017