US4093561A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalyst for the reduction of nitrogen oxides and method for the production thereof
Assignee: Krosaki Harima Corp
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Filing: 1977-02-01
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Granted: 1978-06-06
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Expires: 1997-02-01
Abstract
Abstract Disclosed is a substance which is obtained by calcining an iron hydroxide or a water-containing iron oxide and coating the surface of the resultant calcined product with alumina. This substance is useful as a catalyst in the removal of nitrogen oxides from an exhaust gas containing the nitrogen oxides.
Inventors
- 👤 Yasuo Nishikawa
- 👤 Akira Watanabe
- 👤 Tetsuya Sugimoto
- 👤 Kazuyasu Yabuki
- 👤 Yoshio Hatayama
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 22:10
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8628; B01J; B01J23/00; B01J23/70; B01J23/74; B01J23/745; B01J33/00
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
116 words
A catalyst for the reduction of nitrogen oxides obtained by calcining at least one particulate iron hydroxide at a temperature not exceeding 550° C and coating the calcined particles with an aqueous solution of an aluminum salt, washing, drying and molding the particles having the aluminum salt coating, followed by baking to form an alumina coating, said catalyst containing 60 to 90 percent by weight of Fe 2 O 3 and 40 to 10 percent by weight of Al 2 O 3 and having an average pore diameter of not more than 500 A, a pore volume of not less than 0.1 cc/g and a specific surface area of not less than 10 m 2 /g.
Claim 2
Dependent Claim
116 words
A catalyst for the reduction of nitrogen oxides obtained by calcining at least one particulate iron hydroxide at a temperature not exceeding 550° C and coating the calcined particles with an aqueous solution of an aluminum salt, washing, drying and molding the particles having the aluminum salt coating, followed by baking to form an alumina coating, said catalyst containing 60 to 90 percent by weight of Fe 2 O 3 and 40 to 10 percent by weight of Al 2 O 3 and having an average pore diameter of not more than 500 A, a pore volume of not less than 0.1 cc/g and a specific surface area of not less than 10 m 2 /g.
Claim 3
Dependent Claim
20 words
The catalyst of claim 1, wherein said average pore diameter falls in the range of from 100 to 300 A.
Claim 4
Dependent Claim
19 words
The catalyst of claim 1, wherein said pore volume falls in the range of from 0.15 to 0.75 cc/g.
Claim 5
Dependent Claim
22 words
The catalyst of claim 1, wherein said specific surface area falls in the range of from 20 to 300 m 2 /g.
Claim 6
Dependent Claim
27 words
The catalyst of claim 1, wherein the calculating of said iron hydroxide is carried out at a temperature in the range of from 130 to 550° C.
Claim 7
Dependent Claim
22 words
The catalyst of claim 1 wherein said particulate material has a particle diameter in the range of from 100 to 1000 A.
Claim 8
Independent Claim
163 words
A method for the production of a catalyst for the reduction of nitrogen oxides, which method comprises: (a) calcining at least one iron hydroxide at a temperature not exceeding 550° C; (b) pulverizing the resultant calcined material to a size of not more than 100μ; (c) introducing 0.1 to 1 parts by weight of the thus pulverized material, while agitating into 1 to 10 parts by weight of an aqueous solution containing 5 to 80% by weight of an aluminum salt and subsequently neutralizing the solution thereby causing precipitation of the aluminum salt present in said mixture; (d) ageing the neutralized mixture, thereby coating the surface of said calcined material with said aluminum salt; (e) separating the coated calcined material obtained in step (d), washing and drying the coated material and molding the coated material to suitable shape; and (f) subsequently baking the calcined material thus coated with the aluminum salt at a temperature in the range of from 300° to 1200° C.
Claim 9
Independent Claim
163 words
A method for the production of a catalyst for the reduction of nitrogen oxides, which method comprises: (a) calcining at least one iron hydroxide at a temperature not exceeding 550° C; (b) pulverizing the resultant calcined material to a size of not more than 100μ; (c) introducing 0.1 to 1 parts by weight of the thus pulverized material, while agitating into 1 to 10 parts by weight of an aqueous solution containing 5 to 80% by weight of an aluminum salt and subsequently neutralizing the solution thereby causing precipitation of the aluminum salt present in said mixture; (d) ageing the neutralized mixture, thereby coating the surface of said calcined material with said aluminum salt; (e) separating the coated calcined material obtained in step (d), washing and drying the coated material and molding the coated material to suitable shape; and (f) subsequently baking the calcined material thus coated with the aluminum salt at a temperature in the range of from 300° to 1200° C.
Claim 10
Dependent Claim
22 words
The method of claim 7, wherein said iron hydroxide has a particle diameter in the range of from 100 to 1000 A.
Claim 11
Dependent Claim
28 words
The method of claim 7, wherein the calcining of said iron hydroxide is carried out at a temperature falling in the range of from 130° to 550° C.
Claim 12
Dependent Claim
25 words
The method of claim 7, wherein said aluminum salt is one member selected from the group consisting of aluminum nitrate, aluminum sulfate and aluminum formate.
Claim 13
Dependent Claim
27 words
The method of claim 7, wherein said neutralizing is performed with an agent selected from the group consisting of ammonia, ammonium hydroxide, caustic soda and sodium carbonate.
Claim 14
Dependent Claim
9 words
The product produced by the process of claim 7.
References Cited (Backward Citations)
US3816594A
Cited
US3987146A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-06-05 | 1981-12-05 | 1982-06-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-06-05 | 1985-12-05 | 1986-06-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-06-05 | 1989-12-05 | 1990-06-06 | $7700.00 | Window Closed / Lapsed |