IP Library Granted Patent US 7,968,492
Granted Patent B2
US 7,968,492 · App. 12/463,828 · Granted Jun 28, 2011

Layered catalyst to improve selectivity or activity of manganese containing vanadium-free mobile catalyst

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,968,492
App. No.
12/463,828
Granted
Jun 28, 2011
Kind
B2
Abstract

Low temperature activity and high temperature ammonia selectivity of a vanadium-free selective catalytic reduction catalyst are controlled with a mixed oxide support containing oxides of titanium and zirconium, and a plurality of alternating layers respectively formed of a metal compound and titanium oxide present on the surface of the mixed oxide support. The metal compound is selected from the group consisting of manganese oxide, iron oxide, cerium oxide, tin oxide, and mixtures thereof.

Claims (30)

1. A catalyst composition comprising: (a) a mixed metal oxide support consisting essentially of oxides of titanium, zirconium, and optionally manganese, and (b) alternating layers respectively formed of a metal compound and titanium oxide on the surface of the mixed metal oxide support, wherein the metal compound is selected from the group consisting of manganese oxide, iron oxide, cerium oxide, tin oxide, and mixtures thereof.

2. The catalyst of claim 1 , wherein the mixed metal oxide support is essentially free from vanadium.

3. The catalyst of claim 2 , wherein the molar ratio of titanium oxide to zirconium oxide in the mixed metal oxide support is in the range of from about 60:40 to about 90:10.

4. The catalyst of claim 2 , wherein the mixed metal oxide support further comprises a crystalline inner core surrounded by amorphous metal oxide.

5. The catalyst of claim 4 , wherein the crystalline inner core comprises an oxide selected from the group consisting of anatase, rutile, srilankite, and mixtures thereof.

6. The catalyst of claim 2 , wherein a first layer of manganese oxide is present on the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 15 mol % of the mixed metal oxide support.

7. The catalyst of claim 6 , wherein a first layer of manganese oxide is present on the mixed metal oxide support in an amount in a range of from about 1 mol % to about 10 mol % of the mixed metal oxide support.

8. The catalyst of claim 6 , wherein a second layer of titanium oxide is present on the manganese oxide first layer of the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 10 mol % of the mixed metal oxide support.

9. The catalyst of claim 8 , wherein a second layer of titanium oxide is present on the manganese oxide first layer of the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 5 mol % of the mixed metal oxide support.

10. The catalyst of claim 8 , wherein a third layer of manganese oxide is present on the titanium oxide second layer of the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 10 mol % of the mixed metal oxide support.

11. The catalyst of claim 8 , wherein a third layer of manganese oxide is present on the titanium oxide second layer of the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 5 mol % of the mixed metal oxide support.

12. A vanadium-free catalyst for selective catalytic reduction of nitrogen oxide with ammonia, the catalyst comprising: (a) a mixed metal oxide support consisting essentially of oxides of titanium and zirconium and optionally manganese, wherein the molar ratio of titanium oxide to zirconium oxide in the mixed metal oxide support is in a range of from about 70:30 to about 85:15; (b) a first layer containing a metal compound selected from the group consisting of manganese oxide, iron oxide, cerium oxide, tin oxide, and mixtures thereof, the metal compound being present on the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 15 mol % of the mixed metal oxide support; and (c) a second layer containing titanium oxide present on the metal compound first layer of the mixed metal oxide support in an amount in a range of from about 0.5 mol % to about 10 mol % of the mixed metal oxide support.

13. A method of making a catalyst for selective catalytic reduction of nitrogen oxide, the method comprising the following steps:

providing a mixed metal oxide support consisting essentially of oxides of titanium, zirconium and optionally manganese;

depositing a first layer, the first layer containing manganese, iron, cerium, tin, or mixtures thereof, onto the surface of the mixed metal oxide support; and

depositing a second layer, the second layer containing titanium, over the first layer containing manganese, iron, cerium, tin, or mixtures thereof.

14. The method of claim 13 , wherein the mixed metal oxide support is prepared by precipitating titanium, zirconium, and optionally manganese, from an aqueous solution.

15. The method of claim 13 wherein the mixed metal oxide support is provided by precipitating titanium and zirconium oxides from an aqueous solution containing dissolved titanium and zirconium, wherein the precipitation is encouraged by increasing the pH to a range of from about 5 to about 10, and wherein the resulting mixed metal oxide has a TiO 2 :ZrO 2 molar ratio in a range of from about 70:30 to about 85:15.

16. The method of claim 13 wherein manganese is deposited as the first layer in an amount in a range of from about 0.5 mol % to about 15 mol % of the mixed oxide support.

17. The method of claim 13 wherein titanium is deposited as the second layer in an amount in a range of from about 0.5 mol % to about 10 mol % of the mixed oxide support.

18. The method of claim 13 wherein the step of depositing a second layer containing titanium over the first layer containing manganese comprises depositing titanium from an aqueous solution containing a dissolved compound selected from the group consisting of titanyl sulfate, titanyl chloride, titanium tetrachloride, titanium oxalate, titanium tetraiodide and mixtures thereof.

19. The method of claim 13 further comprising the step of:

depositing a third layer, the third layer containing manganese, over the second layer containing titanium.

20. A method of controlling the activity or selectivity of a catalyst used for selective catalytic reduction of nitrogen oxides with ammonia, the method comprising:

providing a mixed metal oxide support consisting essentially of oxides of titanium, zirconium and optionally manganese; and

depositing alternating layers respectively formed of a metal compound and titanium onto the surface of the mixed metal oxide support, wherein the metal compound is selected from the group consisting of oxides of manganese, iron, cerium, tin and mixtures thereof, and wherein the number of layers and the quantities of the metal compound and the titanium deposited are selected to provide desired levels of low temperature activity or high temperature selectivity.

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

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

a mixed oxide support consisting essentially of oxides of titanium, zirconium, and optionally manganese; and

a plurality of layers respectively formed of a metal compound and titanium oxide deposited on the mixed oxide support, wherein the metal compound is selected from the group consisting of manganese oxide, iron oxide, cerium oxide, tin oxide, and mixtures thereof.

Assignments (7)
SECURITY INTEREST Recorded Sep 26, 2025
From: TRONOX LLC
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 072942/0255 →
RELEASE OF SECURITY INTEREST Recorded Apr 7, 2022
From: WILMINGTON TRUST, NATIONAL ASSOCIATION
To: TRONOX LLC
Reel/Frame 059629/0581 →
SECURITY INTEREST Recorded Mar 12, 2021
From: TRONOX LLC
To: HSBC BANK USA, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 055579/0619 →
SECURITY INTEREST Recorded May 1, 2020
From: TRONOX LLC
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 052554/0529 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 10, 2019
From: CRISTAL USA INC.
To: TRONOX LLC
Reel/Frame 049148/0729 →
CHANGE OF NAME Recorded Aug 9, 2013
From: MILLENNIUM INORGANIC CHEMICALS, INC.
To: CRISTAL USA INC.
Reel/Frame 030982/0732 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 17, 2011
From: AUGUSTINE, STEVEN M
To: MILLENNIUM INORGANIC CHEMICALS, INC.
Reel/Frame 026290/0170 →