US4049777A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of waste gas treatment
Assignee: Didier Engineering GmbH
•
Filing: 1976-05-20
•
Granted: 1977-09-20
•
Expires: 1996-05-20
Abstract
Abstract Waste gas, for example exhaust gas from an adipic acid production process, containing nitrogen oxides and a high proportion of oxygen and/or oxygen compounds is treated to remove the nitrogen oxides by reducing the nitrogen oxides with ammonia at an elevated temperature in the presence of a catalyst comprising an iron oxide and a chromium oxide.
Inventors
- 👤 Rudolf Divivier
- 👤 Gotthard Uckert
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 23:20
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
115 words
A method of removing nitrogen oxides from a feed stock containing at least 10% by volume of oxygen and/or at least 12% by volume of oxygen compounds other than the nitrogen oxides, which comprises providing at least two separate beds of a catalyst comprising at least one oxide of the iron group and at least one oxide of the chromium group, and passing the feed stock sequentially through the catalyst beds while simultaneously introducing ammonia into the feed stock prior to passage of the feed stock through each catalyst bed, thus causing the nitrogen oxides to undergo a reduction reaction, said reduction reaction being carried out at a temperature between 260° C. and 350° C.
Claim 2
Independent Claim
115 words
A method of removing nitrogen oxides from a feed stock containing at least 10% by volume of oxygen and/or at least 12% by volume of oxygen compounds other than the nitrogen oxides, which comprises providing at least two separate beds of a catalyst comprising at least one oxide of the iron group and at least one oxide of the chromium group, and passing the feed stock sequentially through the catalyst beds while simultaneously introducing ammonia into the feed stock prior to passage of the feed stock through each catalyst bed, thus causing the nitrogen oxides to undergo a reduction reaction, said reduction reaction being carried out at a temperature between 260° C. and 350° C.
Claim 3
Dependent Claim
16 words
A method according to claim 1, in which the catalyst comprises ferric oxide and chromic oxide.
Claim 4
Dependent Claim
22 words
A method according to claim 1, in which the feed stock is heated to a temperature between 260° C. and 310° C.
Claim 5
Dependent Claim
33 words
A method according to claim 1, in which the feed stock contains up to 10,000 volume parts per million of NO, NO 2 or a mixture thereof, and a major proportion of nitrogen.
Claim 6
Dependent Claim
27 words
A method according to claim 4, in which the feed stock contains 5,000 to 10,000 volume parts per million of NO, NO 2 or a mixture thereof.
Claim 7
Dependent Claim
18 words
A method according to claim 5, in which the feed stock contains about 16% by volume of oxygen.
Claim 8
Dependent Claim
35 words
A method according to claim 1, in which the catalyst is a mixture of a major proportion by weight of an iron oxide and a minor proportion by weight of at least one chromium oxide.
Claim 9
Dependent Claim
18 words
A method according to claim 1, in which the catalyst comprises ferric oxide, chromic oxide and chromium trioxide.
Claim 10
Dependent Claim
24 words
A method according to claim 8, in which the chromic oxide is present in an amount greater than the amount of the chromium trioxide.
Claim 11
Dependent Claim
20 words
A method according to claim 9, in which the ratio by weight of chromic oxide to chromium trioxide is 5:1.
Claim 12
Dependent Claim
24 words
A method according to claim 7, in which the ratio by weight of the iron oxide to the chromium oxide is at least 7:1.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-19 | 1981-03-21 | 1981-09-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-19 | 1985-03-21 | 1985-09-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-19 | 1989-03-21 | 1989-09-20 | $7700.00 | Window Closed / Lapsed |