IP Library Granted Patent US 7,527,776
Granted Patent B2
US 7,527,776 · App. 11/651,290 · Granted May 5, 2009

Ammonia SCR catalyst and method of using the catalyst

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Quick Facts
Patent No.
US 7,527,776
App. No.
11/651,290
Granted
May 5, 2009
Kind
B2
Abstract

A catalyst and a method for selectively reducing nitrogen oxides with ammonia are provided. The catalyst includes a first component of copper, chromium, cobalt, nickel, manganese, iron, niobium, or mixtures thereof, a second component of cerium, a lanthanide, a mixture of lanthanides, or mixtures thereof, and a zeolite. The catalyst may also include strontium as an additional second component. The catalyst and the method may have special application to selective reduction of nitrogen oxides in exhaust gas from diesel vehicles, although the catalyst and the method have broad application to a wide range of gas streams that contain nitrogen oxides.

Claims (37)

1. A catalyst for selective catalytic reduction of nitrogen oxides with ammonia, the catalyst comprising:

a first component comprising at least one selected from the group consisting of copper, chromium, cobalt, nickel, manganese, iron, niobium, and mixtures thereof;

a second component comprising at least one selected from the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof;

at least one zeolite and

strontium.

2. A catalyst for selective catalytic reduction of nitrogen oxides with ammonia, the catalyst comprising:

a first component comprising at least one selected from the group consisting of copper, chromium, cobalt, nickel, manganese, iron, niobium, and mixtures thereof;

a second component comprising at least one selected from the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof;

at least one zeolite and

an oxygen storage material.

3. The catalyst of claim 2 , wherein the oxygen storage material is selected from the group consisting of Ce 1-a Zr a O 2 and Ce 1-c-d Zr c Lan d O 2 , wherein Lan is selected from the group consisting of Y, La, Pr, Nd, Sm, Eu, Gd, Ho, Yb and mixtures thereof.

4. A catalyst for selective catalytic reduction of nitrogen oxides with ammonia, the catalyst comprising:

approximately 1 to approximately 20 weight percent of a first component, said first component comprising at least one selected from the group consisting of copper, chromium, cobalt nickel, manganese, iron, niobium, and mixtures thereof;

approximately 2 to approximately 35 weight percent of a second component, said second component comprising at least one selected from the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof;

approximately 10 to approximately 90 weight % of at least one zeolite, and

approximately 2 to approximately 35 weight percent of strontium, wherein the weight percent of the strontium is on the basis of strontium metal, and wherein the weight percentages of the first component and the second component are on the basis of the metals.

5. A catalyst composition comprising:

a substrate; and

a catalyst for selective catalytic reduction of nitrogen oxides with ammonia, the catalyst comprising:

a first component comprising at least one selected from the group consisting of copper, chromium, cobalt, nickel, manganese, iron, niobium, and mixtures thereof;

a second component comprising at least one selected from the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof;

at least one zeolite, and an oxygen storage material, wherein the catalyst is placed on the substrate.

6. The catalyst composition of claim 5 , further comprising at least one inorganic oxide selected from the group consisting of alumina, silica, titania, and silica-alumina solutions, composites, and mixtures thereof, and wherein at least one of the zeolite, the oxygen storage material, and the inorganic oxide is placed on the substrate in a form of a washcoat.

7. A method for selective reduction of nitrogen oxides in a gas stream with ammonia, wherein the gas stream comprises nitrogen oxides, the method comprising:

contacting the gas stream with ammonia in the presence of a catalyst, the catalyst comprising:

a first component comprising at least one selected from the group consisting of copper, chromium, cobalt, nickel, manganese, iron, niobium, and mixtures thereof;

a second component comprising at least one selected from the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof;

at least one zeolite and

strontium.

8. A method for selective reduction of nitrogen oxides in a gas stream with ammonia, wherein the gas stream comprises nitrogen oxides, the method comprising:

contacting the gas stream with ammonia in the presence of a catalyst, the catalyst comprising:

a first component comprising at least one selected from the group consisting of copper, chromium, cobalt, nickel, manganese, iron, niobium, and mixtures thereof;

a second component comprising at least one selected from the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof;

at least one zeolite and

an oxygen storage material.

9. The method of claim 8 , wherein the oxygen storage material is selected from the group consisting of Ce 1-a Zr a O 2 and Ce 1-c-d Zr c Lan d O 2 , wherein Lan is selected from the group consisting of Y, La, Pr, Nd, Sm, Eu, Gd, Ho, Yb and mixtures thereof.

10. A method for selective reduction of nitrogen oxides in a gas stream with ammonia, wherein the gas stream comprises nitrogen oxides, the method comprising: contacting the gas stream with ammonia in the presence of a catalyst, the catalyst comprising: a first component comprising at least one of the group consisting of copper, chromium, cobalt, nickel, manganese, iron, niobium, and mixtures thereof, a second component comprising at least one of the group consisting of cerium, a lanthanide, a mixture of lanthanides, and mixtures thereof, and at least one zeolite, wherein the catalyst comprises approximately 1 to approximately 20 weight percent of the first component, approximately 2 to approximately 35 weight percent of the second component, and approximately 10 to approximately 90 weight % of the at least one zeolite, wherein the weight percentages of the first component and the second component are on the basis of the metals, and approximately 2 to approximately 35 weight percent of strontium, wherein the weight percent of the strontium is on the basis of strontium metal.

Assignments (6)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 18, 2014
From: ECS HOLDINGS, INC.
To: CATALYTIC SOLUTIONS, INC.
Reel/Frame 032515/0462 →
RELEASE OF SECURITY INTEREST Recorded Nov 1, 2010
From: ENERTECH CAPITAL PARTNERS II L.P. (AS COLLATERAL AGENT)
To: ECS HOLDINGS, INC.; CATALYTIC SOLUTIONS, INC.
Reel/Frame 025227/0102 →
SECURITY AGREEMENT Recorded Jun 8, 2010
From: CATALYTIC SOLUTIONS, INC.
To: ENERTECH CAPITAL PARTNERS II L.P. (AS COLLATERAL AGENT)
Reel/Frame 024492/0955 →
AMENDED AND RESTATED NOTICE OF PATENT AND TRADEMARK SECURITY INTEREST Recorded Jul 31, 2008
From: CATALYTIC SOLUTIONS, INC.
To: FIFTH THIRD BANK
Reel/Frame 021316/0499 →
NOTICE OF PATENT AND TRADEMARK SECURITY INTEREST Recorded Jan 3, 2008
From: CATALYTIC SOLUTIONS, INC.
To: FIFTH THIRD BANK
Reel/Frame 020309/0413 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 26, 2007
From: GOLDEN, STEPHEN J.; IRETSKAYA, SVETLANA
To: CATALYTIC SOLUTIONS, INC.
Reel/Frame 019214/0458 →