IP Library › Granted Patent US 11,161,101
Granted Patent B2
US 11,161,101 · App. 15/994,098 · Granted Nov 2, 2021

Catalyst structure and method for producing the catalyst structure

Inventors: Sadahiro Kato (Tokyo, JP); Masayuki Fukushima (Tokyo, JP); Hiroko Takahashi (Tokyo, JP); Yuichiro Banba (Tokyo, JP); Kaori Sekine (Tokyo, JP); Takao Masuda (Tokyo, JP); Yuta Nakasaka (Tokyo, JP); Takuya Yoshikawa (Tokyo, JP)
Assignee: Furukawa Electric Co., Ltd.
B01J29/89B01J23/42B01J23/44B01J23/462B01J23/464B01J23/468B01J23/745B01J23/75B01J23/755B01J29/12B01J29/14B01J35/0013B01J35/0066B01J35/1057B01J35/1061B01J37/0009B01J37/0201B01J37/10B01J2229/186C01B3/40C01B2203/0233C01B2203/0238C01B2203/066C01B2203/107C01B2203/1052C01B2203/1058C01B2203/1064C01B2203/1082C01B2203/1235C01B2203/1241
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Quick Facts
Patent No.
US 11,161,101
App. No.
15/994,098
Granted
Nov 2, 2021
Kind
B2
Abstract

A catalyst structure includes a carrier having a porous structure composed of a zeolite type compound and at least one catalytic material existing in the carrier. The carrier has channels communicating with each other, and the catalytic material is a metal fine particle and exists at least in the channel of the carrier.

Claims (24)

1. A catalyst structure comprising:

a carrier having a porous structure comprising a zeolite compound having a framework; and

at least one catalytic material comprising a metal fine particle and existing in the carrier,

wherein the carrier has a plurality of channels communicating with each other,

the channels include at least one of a one-dimensional pore, a two-dimensional pore and a three-dimensional pore defined by the framework of the zeolite compound, and a plurality of enlarged diameter portions which are different from the one-dimensional pore, the two-dimensional pore and the three-dimensional pore and are not defined by the framework of the zeolite compound, and

the catalytic materials are included in the enlarged diameter portions such that one of the enlarged diameter portions encloses one of the catalytic materials and separates the one of the catalytic materials from another of the catalytic materials.

2. The catalyst structure according to claim 1 , wherein the metal fine particle is a fine particle composed of at least one metal selected from the group consisting of rhodium (Rh), ruthenium (Ru), iridium (Ir), palladium (Pd), platinum (Pt), iron (Fe), cobalt (Co) and nickel (Ni).

3. The catalyst structure according to claim 1 , wherein the enlarged diameter portion makes a plurality of pores forming any one of the one-dimensional pore, the two-dimensional pore and the three-dimensional pore communicate with each other.

4. The catalyst structure according to claim 1 , wherein an average particle diameter of the metal fine particles is greater than an average inner diameter of the channels and is equal to or smaller than an inner diameter of the enlarged diameter portion.

5. The catalyst structure according to claim 1 , wherein a metal element (M) of the metal fine particle is contained in an amount of 0.5 to 2.5 mass % with respect to the catalyst structure.

6. The catalyst structure according to claim 1 , wherein an average particle diameter of the metal fine particles is 0.08 nm to 30 nm.

7. The catalyst structure according to claim 6 , wherein the average particle diameter of the metal fine particles is 0.4 nm to 11.0 nm.

8. The catalyst structure according to claim 1 , wherein a ratio of an average particle diameter of the metal fine particles to an average inner diameter of the channels is 0.05 to 300.

9. The catalyst structure according to claim 8 , wherein the ratio of the average particle diameter of the metal fine particles to the average inner diameter of the channels is 0.1 to 30.

10. The catalyst structure according to claim 9 , wherein the ratio of the average particle diameter of the metal fine particles to the average inner diameter of the channels is 1.4 to 3.6.

11. The catalyst structure according to claim 1 , wherein

an average inner diameter of the channels is 0.1 nm to 1.5 nm, and

an inner diameter of the enlarged diameter portion is 0.5 nm to 50 nm.

12. The catalyst structure according to claim 1 , further comprising at least one other catalytic material held at an outer surface of the carrier.

13. The catalyst structure according to claim 12 , wherein a content of the at least one catalytic material existing in the carrier is greater than a content of the at least one other catalytic material held at the outer surface of the carrier.

14. The catalyst structure according to claim 1 , wherein the enlarged diameter portions are pores formed in a synthesis of the zeolite compound.

15. The catalyst structure according to claim 1 , wherein the catalyst structure is produced by a method including baking a precursor material (B) including a precursor material (A) for obtaining a carrier of the porous structure comprising the zeolite compound, impregnated with a metal-containing solution, and

the baking of the precursor material (B) forms the enlarged diameter portions enclosing the catalytic materials.

16. A synthesis gas producing apparatus comprising the catalyst structure according to claim 1 .

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 31, 2020
From: MASUDA, TAKAO; NAKASAKA, YUTA; YOSHIKAWA, TAKUYA
To: FURUKAWA ELECTRIC CO., LTD.
Reel/Frame 053370/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 14, 2018
From: KATO, SADAHIRO; FUKUSHIMA, MASAYUKI; TAKAHASHI, HIROKO; BANBA, YUICHIRO; SEKINE, KAORI
To: FURUKAWA ELECTRIC CO., LTD.
Reel/Frame 047501/0213 →
Priority Claims (2)
JP 2017-108609 · May 31, 2017 · national
JP 2017-108640 · May 31, 2017 · national
Continuity (1)
Related Publication 20190039056A1 · Feb 7, 2019
Cited By (2)
US 12,208,375 US 12,654,158