IP Library Granted Patent US 9,409,152
Granted Patent B2
US 9,409,152 · App. 14/410,345 · Granted Aug 9, 2016

Catalyst support for purification of exhaust gas, catalyst for purification of exhaust gas using the same, and method for producing the catalyst support for purification of exhaust gas

Inventors: Naoki Kumatani (Nagakute, JP); Akira Morikawa (Nagoya, JP); Kae Konishi (Nagoya, JP); Kimitoshi Sato (Inazawa, JP); Toshitaka Tanabe (Nagakute, JP); Akihiko Suda (Seto, JP); Masahide Miura (Toyota, JP); Isao Chinzei (Toyota, JP); Hiromasa Suzuki (Toyota, JP); Takeshi Nobukawa (Toyota, JP); Takahiro Hayashi (Susono, JP)
Assignees: KABUSHIKI KAISHA TOYOTA CHUO KENKYUSHO; TOYOTA JIDOSHA KABUSHIKI KAISHA
B01J23/10B01J21/066B01J23/44B01J23/63B01J23/83B01J35/002B01J35/023B01J35/1009B01J35/1014B01J35/1038B01J35/1047B01J35/1057B01J35/1061B01J35/1066B01J35/1071B01J35/1076B01J37/0063B01J37/04B01J37/08B01D53/945B01D2255/1023B01D2255/2065B01D2255/2092B01D2255/20715B01D2255/20761B01D2255/908B01D2255/9205B01D2255/9207Y02T10/22
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Quick Facts
Patent No.
US 9,409,152
App. No.
14/410,345
Granted
Aug 9, 2016
Kind
B2
Abstract

A catalyst support for purification of exhaust gas includes a porous composite metal oxide, the porous composite metal oxide containing alumina, ceria, and zirconia and having an alumina content ratio of from 5 to 80% by mass, wherein after calcination in the air at 1100° C. for 5 hours, the porous composite metal oxide satisfies a condition such that standard deviations of content ratios (as at % unit) of aluminum, cerium and zirconium elements are each 19 or less with respect to 100 minute areas (with one minute area being 300 nm in length×330 nm in width) of the porous composite metal oxide, the standard deviation being determined by energy dispersive X-ray spectroscopy using a scanning transmission electron microscope equipped with a spherical aberration corrector.

Claims (48)

1. A catalyst support for purification of exhaust gas comprising a porous composite metal oxide, the porous composite metal oxide containing alumina, ceria, and zirconia and having an alumina content ratio of from 5 to 80% by mass,

wherein the porous composite metal oxide is produced by:

introducing independently a first raw material solution and a second raw material solution directly into a region in which a shear rate is from 1000 to 200000 sec −1 , and homogeneously mixing the raw material solutions to obtain a colloidal solution of metal compounds, the first raw material solution containing an aluminum ion, a cerium ion, and a zirconium ion, and the second raw material solution containing a high-molecular dispersant having a weight average molecular weight of from 3000 to 15000,

adjusting a pH of the colloidal solution to between 3 and 5,

degreasing the colloidal solution after the pH adjustment or a suspension of metal compounds which is obtained by adding an organic amine to the colloidal solution after the pH adjustment, and then

subjecting the solution or the suspension to heat treatment at from 700 to 1050° C. in an oxidizing atmosphere, to obtain the porous composite metal oxide, and

wherein after calcination in air at 1100° C. for 5 hours, the porous composite metal oxide satisfies a condition such that standard deviations of content ratios (as at % unit) of aluminum, cerium and zirconium elements are each 19 or less with respect to 100 minute areas (with one minute area being 300 nm in length×330 nm in width) of the porous composite metal oxide, the standard deviation being determined by energy dispersive X-ray spectroscopy using a scanning transmission electron microscope equipped with a spherical aberration corrector.

2. The catalyst support for purification of exhaust gas according to claim 1 , wherein

the porous composite metal oxide after calcination in air at 1100° C. for 5 hours satisfies conditions such that

a total pore volume of pores having pore diameters within a range of from 1 nm to 0.1 μm is 0.1 cm 3 /g or more, the pore diameter being determined by a nitrogen adsorption method, and

a total pore volume of pores having pore diameters within a range of from 0.1 μm to 10 μm is 0.1 cm 3 /g or more, the pore diameter being determined by a mercury intrusion method.

3. The catalyst support for purification of exhaust gas according to claim 1 , wherein

the porous composite metal oxide after calcination in air at 1100° C. for 5 hours satisfies a condition such that a BET specific surface area determined by a nitrogen adsorption method is 2 m 2 /g or more.

4. The catalyst support for purification of exhaust gas according to claim 1 , wherein

the porous composite metal oxide after calcination in air at 1100° C. for 5 hours satisfies a condition such that standard deviations of content ratios (as at % unit) of aluminum, cerium and zirconium elements are each 18.5 or less with respect to the 100 minute areas, the standard deviation being determined by the energy dispersive X-ray spectroscopy.

5. A catalyst for purification of exhaust gas comprising:

the catalyst support for purification of exhaust gas according to claim 4 ; and

a noble metal supported on the catalyst support, wherein the porous composite metal oxide contains from 5 to 30% by mass of alumina, from 25 to 39% by mass of ceria, and from 33 to 51% by mass of zirconia.

6. The catalyst for purification of exhaust gas according to claim 5 , wherein

the noble metal is palladium.

7. The catalyst support for purification of exhaust gas according to claim 1 , wherein

the porous composite metal oxide after calcination in air at 1100° C. for 5 hours satisfies a condition such that standard deviations of content ratios (as at% unit) of cerium and zirconium elements are each 15 or less with respect to the 100 minute areas, the standard deviation being determined by the energy dispersive X-ray spectroscopy.

8. A catalyst for purification of exhaust gas comprising:

the catalyst support for purification of exhaust gas according to claim 1 ; and

a transition metal supported on the catalyst support, wherein the porous composite metal oxide contains from 30 to 80% by mass of alumina.

9. The catalyst for purification of exhaust gas according to claim 8 , wherein

the transition metal is copper.

10. A method for producing a catalyst support for purification of exhaust gas comprising a porous composite metal oxide containing alumina, ceria, and zirconia, the method comprising the steps of:

preparing a first raw material solution containing an aluminum ion, a cerium ion, and a zirconium ion so that an alumina content ratio of the porous composite metal oxide can be from 5 to 80% by mass;

preparing a second raw solution containing a high-molecular dispersant having a weight average molecular weight of from 3000 to 15000;

introducing independently the first raw material solution and the second raw material solution directly into a region in which a shear rate is from 1000 to 200000 sec −1 , and homogeneously mixing the raw material solutions to obtain a colloidal solution of metal compounds;

adjusting a pH of the colloidal solution to between 3 and 5; and

degreasing the colloidal solution after the pH adjustment and subjecting the solution to heat treatment at from 700 to 1050° C. in an oxidizing atmosphere, to obtain the porous composite metal oxide.

11. The method for producing a catalyst support for purification of exhaust gas according to claim 10 , wherein

at least one of the first and second raw material solutions further contains a low-molecular dispersant having a molecular weight of from 40 to 200.

12. The method for producing a catalyst support for purification of exhaust gas according to claim 11 , wherein

the low-molecular dispersant is contained in the first raw material solution.

13. A method for producing a catalyst support for purification of exhaust gas comprising a porous metal composite metal oxide containing alumina, ceria and zirconia, the method comprising the steps of:

preparing a first raw material solution containing an aluminum ion, a cerium ion, and a zirconium ion so that an alumina content ratio of the porous composite metal oxide can be from 5 to 80% by mass;

preparing a second raw solution containing a high-molecular dispersant having a weight average molecular weight of from 3000 to 15000;

introducing independently the first raw material solution and the second raw material solution directly into a region in which a shear rate is from 1000 to 200000 sec −1 , and homogeneously mixing the raw material solutions to obtain a colloidal solution of metal compounds;

adjusting a pH of the colloidal solution to between 3 and 5;

adding an organic amine to the colloidal solution and performing gelation treatment to obtain a suspension of metal compounds; and

degreasing the suspension and subjecting the suspension to heat treatment at from 700 to 1050° C. in an oxidizing atmosphere, to obtain the porous composite metal oxide.

14. The method for producing a catalyst support for purification of exhaust gas according to claim 13 , wherein

at least one of the first and second raw material solutions further contains a low-molecular dispersant having a molecular weight of from 40 to 200.

15. The method for producing a catalyst support for purification of exhaust gas according to claim 14 , wherein

the low-molecular dispersant is contained in the first raw material solution.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 21, 2015
From: KUMATANI, NAOKI; MORIKAWA, AKIRA; KONISHI, KAE; TANABE, TOSHITAKA; SUDA, AKIHIKO; MIURA, MASAHIDE; CHINZEI, ISAO; SUZUKI, HIROMASA; NOBUKAWA, TAKESHI; HAYASHI, TAKAHIRO
To: KABUSHIKI KAISHA TOYOTA CHUO KENKYUSHO; TOYOTA JIDOSHA KABUSHIKI KAISHA
Reel/Frame 035455/0659 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 21, 2015
From: KUMATANI, NAOKI; MORIKAWA, AKIRA; KONISHI, KAE; TANABE, TOSHITAKA; SUDA, AKIHIKO; MIURA, MASAHIDE; CHINZEI, ISAO; SUZUKI, HIROMASA; NOBUKAWA, TAKESHI; HAYASHI, TAKAHIRO
To: KABUSHIKI KAISHA TOYOTA CHUO KENKYUSHO; TOYOTA JIDOSHA KABUSHIKI KAISHA
Reel/Frame 035455/0791 →
Priority Claims (3)
JP 2012-138950 · Jun 20, 2012 · national
JP 2012-138958 · Jun 20, 2012 · national
JP 2013-125459 · Jun 14, 2013 · national
Continuity (1)
Related Publication 20150266004A1 · Sep 24, 2015