IP Library › Granted Patent US 7,393,804
Granted Patent B2
US 7,393,804 · App. 10/535,331 · Granted Jul 1, 2008

Exhaust gas purifying catalyst and process for purification of exhaust gas

Assignees: ICT Co., Ltd.; International Catalyst Technology Inc.
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Quick Facts
Patent No.
US 7,393,804
App. No.
10/535,331
Granted
Jul 1, 2008
Kind
B2
Abstract

An exhaust gas purifying catalyst has a catalytic component including copper, ZSM-5, and β zeolite. This exhaust gas purifying catalyst reduces nitrogen oxides even from low temperature range and exhibits durability even under a thermal load of high temperature.

Claims (19)

1. A catalyst for purifying exhaust gases, comprising a catalytic component including copper, ZSM-5, and β zeolite; wherein the ZSM-5 has a SiO 2 /Al 2 O 3 molar ratio of (20-100)/1 and an average crystal diameter observed under an electron microscope in a range not exceeding 0.5 μm, the β zeolite has a SiO 2 /Al 2 O 3 molar ratio of (10-50)/1, and the weight ratio of the ZSM-5 and the β zeolite is in the range of 1:0.1-1:5.

2. A catalyst according to claim 1 , wherein the copper is deposited on both of the ZSM-5 and the β zeolite.

3. A catalyst according to claim 1 , wherein, on a refractory three-dimensional structure, the zeolite is deposited in the range of 70-300 g and the copper is deposited in the state of oxide in the range of 3-30 g per liter of the refractory three-dimensional structure.

4. A catalyst according to claim 1 further comprising at least one element selected from the group consisting of phosphorus, cerium, and boron.

5. A process for purifying an exhaust gas, which comprises treating an exhaust gas from a diesel engine with a catalyst set forth in claim 1 .

6. A catalyst according to claim 1 , wherein the copper is deposited on both of the ZSM-5 and the β zeolite.

7. A catalyst according to claim 1 , wherein the copper is deposited on both of the ZSM-5 and the β zeolite.

8. A catalyst according to claim 1 , wherein, on a refractory three-dimensional structure, the zeolite is deposited in the range of 70-300 g and the copper is deposited in the state of oxide in the range of 3-30 g per liter of the refractory three-dimensional structure.

9. A catalyst according to claim 1 , wherein, on a refractory three-dimensional structure, the zeolite is deposited in the range of 70-300 g and the copper is deposited in the state of oxide in the range of 3-30 g per liter of the refractory three-dimensional structure.

10. A catalyst according to claim 2 , wherein, on a refractory three-dimensional structure, the zeolite is deposited in the range of 70-300 g and the copper is deposited in the state of oxide in the range of 3-30 g per liter of the refractory three-dimensional structure.

11. A catalyst according to claim 1 further comprising at least one element selected from the group consisting of phosphorus, cerium, and boron.

12. A catalyst according to claim 1 further comprising at least one element selected from the group consisting of phosphorus, cerium, and boron.

13. A catalyst according to claim 2 further comprising at least one element selected from the group consisting of phosphorus, cerium, and boron.

14. A catalyst according to claim 3 further comprising at least one element selected from the group consisting of phosphorus, cerium, and boron.

15. A process for purifying an exhaust gas, which comprises treating an exhaust gas from a diesel engine with a catalyst set forth in claim 1 .

16. A process for purifying an exhaust gas, which comprises treating an exhaust gas from a diesel engine with a catalyst set forth in claim 1 .

17. A process for purifying an exhaust gas, which comprises treating an exhaust gas from a diesel engine with a catalyst set forth in claim 2 .

18. A process for purifying an exhaust gas, which comprises treating an exhaust gas from a diesel engine with a catalyst set forth in claim 3 .

19. A process for purifying an exhaust gas, which comprises treating an exhaust gas from a diesel engine with a catalyst set forth in claim 4 .

Assignments (3)
CHANGE OF NAME Recorded Mar 27, 2013
From: INTERNATIONAL CATALYST TECHNOLOGY, INC.
To: UMICORE SHOKUBAI USA INC.
Reel/Frame 030102/0238 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 5, 2013
From: ICT CO., LTD.
To: UMICORE SHOKUBAI JAPAN CO., LTD.
Reel/Frame 029925/0593 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 18, 2005
From: MATSUMOTO, TAKESHI; KOBAYASHI, TAKAO; NAKANE, TAKUJI; UNO, TAKAHIRO; HORIUCHI, MAKOTO
To: ICT CO., LTD.; INTERNATIONAL CATALYST TECHNOLOGY INC.
Reel/Frame 017009/0456 →
Priority Claims (1)
JP 2002-333629 · Nov 18, 2002 · national
Continuity (1)
Related Publication 20060014630A1 · Jan 19, 2006