Non-PGM ammonia slip catalyst

US11198094B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11198094-B2
Application numberUS-201514726924-A
CountryUS
Kind codeB2
Filing dateJun 1, 2015
Priority dateJun 4, 2014
Publication dateDec 14, 2021
Grant dateDec 14, 2021

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

An ammonia slip catalyst having an SCR catalyst and an oxidation catalyst comprising at least two metals, each of which is selected from a specific group, and a substrate upon which at least oxidation catalyst is located is described. The ammonia slip catalyst can have dual layers, with one of the layers containing an SCR catalyst, a second layer containing the oxidation catalyst with comprises at least two metals, each of which is selected from a specific group, and the ammonia slip catalyst does not contain a platinum group metal. Methods of making and using the ammonia slip catalyst to reduce ammonia slip are described.

First claim

Opening claim text (preview).

What is claimed is: 1. A dual layer ammonia slip catalyst comprising an SCR layer and an oxidation layer, wherein at least the oxidation layer is positioned proximal to a substrate, wherein the SCR layer comprises a molecular sieve or a vanadium/titania SCR catalyst; and the oxidation layer consists of: (a) an ammonia oxidation catalyst consisting of copper and manganese; and (b) an oxide support material consisting of alumina and either a CeO 2 /ZrO 2 mixed oxide or a Zr-stabilized CeO 2 mixed oxide; wherein the ammonia slip catalyst does not comprise a platinum group metal. 2. The dual layer ammonia slip catalyst of claim 1 , wherein the oxidation layer further comprises an oxide support material comprising one or both of alumina and silica. 3. A method for reducing the concentration of ammonia in a flue gas stream generated by a combustion source, the method comprising contacting a flue gas stream containing ammonia with a dual layer ammonia slip catalyst of claim 1 . 4. The dual layer ammonia slip catalyst of claim 1 , wherein the substrate is a flow-through substrate. 5. The dual layer ammonia slip catalyst of claim 1 , wherein the Zr-stabilized CeO 2 mixed oxide comprises Ce and Zr present in about a 1:1 mole ratio. 6. The dual layer ammonia slip catalyst of claim 1 , wherein the oxide support material comprises about 20 mole % La-stabilized Al 2 O 3 and about 80 mole % Zr-stabilized CeO 2 . 7. The dual layer ammonia slip catalyst of claim 1 , wherein the molecular sieve is selected from the group consisting of MOR (mordenite), FER (ferrierite), FAU (zeolite Y), MFI (ZSM-5), BEA (beta zeolites), Fe-BEA, CHA (Chabazite), Cu-CHA and a silicoaluminophosphate comprising a structurally similar framework. 8. The dual layer ammonia slip catalyst of claim 7 , wherein the SCR layer comprises a Fe-BEA or a Cu-CHA zeolite catalyst or a silicoaluminophosphate comprising a structurally similar framework. 9. The dual layer ammonia slip catalyst of claim 8 , wherein the SCR layer comprises a Fe-BEA or a Cu-CHA zeolite or a silicoaluminophosphate comprising a structurally similar framework catalyst and the oxidation layer comprises Cu and Mn. 10. The dual layer ammonia slip catalyst of claim 1 , wherein the catalyst in the oxidation layer is present at a concentration of 0.3 to 1.5 g per in 3 , based on the total weight of metal in the catalyst. 11. The dual layer ammonia slip catalyst of claim 1 , wherein the catalyst in the SCR layer is present at a concentration of 0.5 to 2.5 g per in 3 , based on the total weight of metal in the catalyst. 12. The dual layer ammonia slip catalyst of claim 1 , wherein the ratio of the amount of catalyst in the SCR layer (in g per in 3 ) to the amount of catalyst in the oxidation layer (in g per in 3 ) is between 0.3 and 8.3, based on the total weight of metal in each layer of the catalyst. 13. The dual layer ammonia slip catalyst of claim 1 , wherein the SCR layer is positioned as an overlayer over the oxidation layer or the oxidation layer is located sequential to the SCR layer.

Assignees

Inventors

Classifications

  • CHA-type, e.g. Chabazite, LZ-218 · CPC title

  • Iron group metals or copper · CPC title

  • Iron group metals or copper · CPC title

  • Iron group metals or copper · CPC title

  • Iron group metals or copper · CPC title

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What does patent US11198094B2 cover?
An ammonia slip catalyst having an SCR catalyst and an oxidation catalyst comprising at least two metals, each of which is selected from a specific group, and a substrate upon which at least oxidation catalyst is located is described. The ammonia slip catalyst can have dual layers, with one of the layers containing an SCR catalyst, a second layer containing the oxidation catalyst with comprises…
Who is the assignee on this patent?
Johnson Matthey Plc
What technology area does this patent fall under?
Primary CPC classification B01D53/8634. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Dec 14 2021 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 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).