IP Library › Patent Application 13891668
Patent Application
App. No. 13/891,668

Perovskite and Mullite-like Structure Catalysts for Diesel Oxidation and Method of Making Same

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Patent No.
US None
App. No.
13/891,668
Abstract

Disclosed here are material formulations of use in the conversion of exhaust gases. A catalyst is formed by using a perovskite structure having the general formula ABO3 or a mullite structure having the general formula of AB2O5 where components “A” and “B” may be any suitable non-platinum group metals. Suitable materials may include Yttrium, Lanthanum, Silver, Manganese and formulations thereof.

Claims (34)

1 . A zero platinum group metal (ZPGM) catalyst system, comprising:

a substrate;

a washcoat suitable for deposition on the substrate, comprising at least one oxide solid selected from the group consisting of at least one of a carrier material oxide, and a ZPGM catalyst; and

an overcoat suitable for deposition on the substrate, comprising at least one overcoat oxide solid selected from the group consisting of at least one of a carrier material oxide, and a ZPGM catalyst;

wherein at least one of the ZPGM catalysts comprises at least one perovskite structured compound having a formula ABO 3 , wherein A is selected from the group consisting of at least one of yttrium, lanthanum, silver, magnesium, and mixtures thereof.

2 . The catalyst system of claim 1 , wherein the carrier material oxide is selected from the group consisting of ZrO2, doped ZrO2 with lanthanid group metals, alumina, doped alumina, TiO 2 doped TiO 2 , Nb 2 O 5 , Nb 2 O 5 -ZrO 2 , and combinations thereof.

3 . The catalyst system of claim 1 , wherein at least one of the ZPGM catalysts is deposited by co-precipitation at a temperature of about 600° C. to about 800° C.

4 . The catalyst system of claim 1 , wherein at least one of the ZPGM catalysts is deposited by co-precipitation at a temperature of about 500° C. to about 800° C. .

5 . The catalyst system of claim 1 , wherein the T50 conversion temperature for carbon monoxide is less than 250° Celsius.

6 . The catalyst system of claim 1 , wherein the T50 conversion temperature for NO is less than 300° Celsius.

7 . A zero platinum group metal (ZPGM) catalyst system, comprising:

a substrate;

a washcoat suitable for deposition on the substrate, comprising at least one oxide solid selected from the group consisting at least one of a carrier metal oxide, and a ZPGM catalyst; and

an overcoat suitable for deposition on the substrate;

wherein the ZPGM catalyst comprises at least one structured compound having the formula A 1-x M x BO 3 , wherein x is 0 to 1. and wherein each of A, B and M is selected from the group consisting at least one of yttrium, lanthanum, silver, manganese, and combinations thereof.

8 . The catalyst of claim 7 , wherein the overcoat further comprises at least one overcoat oxide solid selected from the group consisting at least one of a carrier metal oxide, and a ZPGM catalyst.

9 . The catalyst system of claim 7 , wherein the T50 conversion temperature for carbon monoxide is less than 250° Celsius.

10 . The catalyst system of claim 7 , wherein the T50 conversion temperature for NO is less than 300° Celsius.

11 . A zero platinum group metal (ZPGM) catalyst system, comprising:

a substrate;

a washcoat suitable for deposition on the substrate, comprising at least one oxide solid selected from the group consisting at least one of a carrier metal oxide, and a ZPGM catalyst; and

an overcoat suitable for deposition on the substrate, comprising at least one overcoat oxide solid selected from the group consisting at least one of a carrier metal oxide, and a ZPGM catalyst;

wherein at least one of the ZPGM catalysts comprises at least one mullite structured compound having the formula AB 2 O 5 , wherein each of A and B is selected from the group consisting at least one of yttrium, lanthanum, silver, manganese, and combinations thereof.

12 . The catalyst system of claim 11 , wherein at least one of the ZPGM catalysts oxidizes carbon monoxide, hydrocarbons or nitrogen oxides.

13 . The catalyst system of claim 11 , wherein the T50 conversion temperature for carbon monoxide is less than 250° Celsius.

14 . The catalyst system of claim 11 , wherein the T50 conversion temperature for NO is less than 300° Celsius.

15 . A zero platinum group metal (ZPGM) catalyst system, comprising:

a substrate;

a washcoat suitable for deposition on the substrate, comprising at least one oxide solid selected from the group consisting at least one of a carrier metal oxide, and a ZPGM catalyst; and

an overcoat suitable for deposition on the substrate;

wherein the ZPGM catalyst comprises at least one structured compound having the formula A 1-x M x B 2 O 5 , wherein x is 0 to 1 and wherein each of A and B is selected from the group consisting at least one of yttrium, lanthanum, silver, manganese, and combinations thereof.

16 . The catalyst system of claim 15 , wherein the ZPGM catalyst oxidizes carbon monoxide, hydrocarbons or nitrogen oxides.

17 . The catalyst system of claim 15 , wherein the T50 conversion temperature for carbon monoxide is less than 250° Celsius.

18 . The catalyst system of claim 15 , wherein the T50 conversion temperature for NO is less than 300° Celsius.

Assignments (3)
NUNC PRO TUNC ASSIGNMENT Recorded Jul 5, 2016
From: NAZARPOOR, ZAHRA; GOLDEN, STEPHEN J.
To: CLEAN DIESEL TECHNOLOGIES, INC. (CDTI)
Reel/Frame 039077/0082 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 23, 2015
From: CLEAN DIESEL TECHNOLOGIES, INC. (CDTI)
To: CLEAN DIESEL TECHNOLOGIES, INC.
Reel/Frame 036933/0646 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 6, 2013
From: NAZARPOOR, ZAHRA; GOLDEN, STEPHEN J.
To: CLEAN DIESEL TECHNOLOGY INC (CDTI)
Reel/Frame 031150/0817 →