IP Library Granted Patent US 11,794,171
Granted Patent B2
US 11,794,171 · App. 16/390,072 · Granted Oct 24, 2023

High porosity metal oxide catalyst coatings

Inventors: Mark Thomas Buelow (Flemington, NJ); Steven W. Chin (Port Reading, NJ); Jeffrey Barmont Hoke (North Brunswick, NJ); Nicholas R. Leclerc (Hillsborough, NJ); David M. Robinson (Princeton, NJ)
Assignee: BASF Corporation
B01J23/75A61L9/00B01D53/8675B01D53/88B01J23/34B01J31/28B01J31/32B01J35/1019B01J35/1042B01J35/1047B01J35/1061B01J37/0215B01D2255/2073B01D2255/2092B01D2255/20746B01D2255/30B01D2255/92B01D2257/106B01D2257/404B01D2257/502B01D2257/702B01D2257/708B01D2259/4566B01J35/002B01J37/0201B01J37/0203B01J37/0219B01J2231/62
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Quick Facts
Patent No.
US 11,794,171
App. No.
16/390,072
Granted
Oct 24, 2023
Kind
B2
Abstract

Disclosed in certain implementations is a catalysis composition that includes a metal catalyst and a support material impregnated with the metal catalyst.

Claims (34)

1. A catalyst composition comprising:

a manganese oxide catalyst, wherein a cumulative pore volume of the manganese oxide catalyst is from 1.2 mL/g to 2 mL/g;

a support material impregnated with the manganese oxide catalyst, wherein at least about 15% of a total number of manganese atoms in the manganese oxide catalyst are dispersed as crystallites within about 10 nanometers of an outer surface of the catalyst composition as detectable by surface X-ray photoelectron spectroscopy (XPS); and

at least two acrylic binders, wherein a first acrylic binder of the at least two acrylic binders exhibits a glass transition temperature of about 20° C. or less, wherein a second acrylic binder of the at least two acrylic binders exhibits a glass transition temperature of greater than about 20° C., wherein a total binder concentration including the first acrylic binder and the second acrylic binder is less than about 16% based on a total weight of the catalyst composition, and wherein the concentrations of the first acrylic binder and the second acrylic binder are selected such that an ultrasonic washcoat adhesion weight loss of the catalyst composition when adhered to a substrate is less than 1.60%.

2. The catalyst composition of claim 1 , wherein the manganese oxide catalyst is impregnated in the support material in an amount ranging from about 10% to about 25% manganese atoms by mass, based on the total composition.

3. The catalyst composition of claim 1 , wherein an average pore radius of the catalysis composition is from about 6 nanometers to about 15 nanometers, and wherein an average pore radius of the catalysis composition is from about 6 nanometers to about 15 nanometers.

4. The catalyst composition of claim 1 , wherein the support material is selected from the group consisting of ceria, lanthana, alumina, titania, silica, zirconia, carbons, metal organic framework, clay, zeolites, and combinations thereof.

5. The catalyst composition of claim 1 , wherein a surface area of the catalysis composition is from about 100 m 2 /g to about 200 m 2 /g.

6. The catalyst composition of claim 1 , wherein the manganese oxide catalyst comprises at least one of Mn 3 O 4 crystallites or MnO crystallites.

7. The catalyst composition of claim 1 , wherein an x-ray diffraction spectrum of the catalysis composition comprises at least one characteristic peak comprising at least one of a manganosite peak, pyrolusite peak, a bixbyite peak, or a hausmannite peak.

8. The catalyst composition of claim 1 , wherein the first acrylic binder and the second acrylic binder each comprise a styrene acrylic binder.

9. The catalyst composition of claim 8 , wherein:

the first acrylic binder exhibits a glass transition temperature ranging from about 5° C. to about 20° C.; and

the second acrylic binder exhibits a glass transition temperature ranging from about 70° C. to about 90° C.

10. A catalytic device comprising:

an automobile radiator; and

a catalyst composition coated onto the automobile radiator, the catalyst composition comprising:

a manganese oxide catalyst, wherein at least about 15% of a total number of manganese atoms in the manganese oxide catalyst are dispersed as crystallites within about 10 nanometers of an outer surface of the catalyst composition as detectable by surface X-ray photoelectron spectroscopy (XPS), wherein at least 50% of the manganese oxide catalyst is in amorphous form, and wherein a cumulative pore volume of the manganese oxide catalyst is from 1.2 mL/g to 2 mL/g;

a support material impregnated with the manganese oxide catalyst; and

at least two acrylic binders, wherein a first acrylic binder of the at least two acrylic binders exhibits a glass transition temperature of about 20° C. or less, wherein a second acrylic binder of the at least two acrylic binders exhibits a glass transition temperature of greater than about 20° C., wherein a total binder concentration including the first acrylic binder and the second acrylic binder is less than about 16% based on a total weight of the catalyst composition, and wherein the concentrations of the first acrylic binder and the second acrylic binder are selected such that an ultrasonic washcoat adhesion weight loss of the catalyst composition when adhered to a substrate is less than 1.60%.

11. The catalytic device of claim 10 , further comprising:

an over layer formed over the support material and the manganese oxide catalyst, wherein the over layer comprises at least one of a protective coat, an adhesion coat, or an additional catalytic material.

12. The catalytic device of claim 10 , wherein the manganese oxide catalyst is impregnated in the support material in an amount ranging from about 10% to about 25% manganese atoms by mass, based on the total composition, wherein an average pore radius of the catalysis composition is from about 6 nanometers to about 15 nanometers, and wherein an average pore radius of the catalysis composition is from about 6 nanometers to about 15 nanometers.

13. The catalytic device of claim 10 , wherein the support material is selected from the group consisting of ceria, lanthana, alumina, titania, silica, zirconia, carbons, metal organic framework, clay, zeolites, and combinations thereof.

14. The catalytic device of claim 10 , wherein a surface area of the catalysis composition is from about 100 m 2 /g to about 200 m 2 /g.

15. The catalytic device of claim 10 , wherein the manganese oxide catalyst comprises at least one of Mn 3 O 4 crystallites or MnO crystallites.

16. The catalytic device of claim 10 , wherein an x-ray diffraction spectrum of the catalysis composition comprises at least one characteristic peak comprising at least one of a manganosite peak, pyrolusite peak, a bixbyite peak, or a hausmannite peak.

17. The catalytic device of claim 10 , wherein the first acrylic binder and the second acrylic binder each comprise a styrene acrylic binder, and wherein:

the first acrylic binder exhibits a glass transition temperature ranging from about 5° C. to about 20° C.; and

the second acrylic binder exhibits a glass transition temperature ranging from about 70° C. to about 90° C.

18. A method of forming a manganese oxide catalyst, the method comprising:

mixing a manganese compound with a support material to form a manganese-impregnated support;

calcining the manganese-impregnated support to form the manganese oxide catalyst, wherein at least about 15% of a total number of manganese atoms in the manganese oxide catalyst are dispersed as crystallites within about 10 nanometers of an outer surface of the catalyst composition as detectable by surface X-ray photoelectron spectroscopy (XPS), wherein at least 50% of the manganese oxide catalyst is in amorphous form, and wherein a cumulative pore volume of the manganese oxide catalyst is from 1.2 mL/g to 2 mL/g; and

incorporating the manganese oxide catalyst into a slurry comprising at least two acrylic binders, wherein a first acrylic binder of the at least two acrylic binders exhibits a glass transition temperature of about 20° C. or less, wherein a second acrylic binder of the at least two acrylic binders exhibits a glass transition temperature of greater than about 20° C., wherein a total binder concentration including the first acrylic binder and the second acrylic binder is less than about 16% based on a total weight of the catalyst, and wherein the concentrations of the first acrylic binder and the second acrylic binder are selected such that an ultrasonic washcoat adhesion weight loss of the catalyst when adhered to a substrate is less than 1.60%.

Assignments (2)
NUNC PRO TUNC ASSIGNMENT Recorded Aug 8, 2024
From: BASF CORPORATION
To: BASF MOBILE EMISSIONS CATALYSTS LLC
Reel/Frame 068518/0394 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 23, 2019
From: BUELOW, MARK THOMAS; CHIN, STEVEN W.; HOKE, JEFFREY BARMONT; LECLERC, NICHOLAS R.; ROBINSON, DAVID M.
To: BASF CORPORATION
Reel/Frame 048963/0493 →
Continuity (3)
Continuation 14528208 · Oct 30, 2014
Provisional Application 61897557 · Oct 30, 2013
Related Publication 20190240645A1 · Aug 8, 2019