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US4447333A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the elimination of ammonia in coke plant waste waters

Assignee: Didier Engineering GmbH
•
Filing: 1983-01-12
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Granted: 1984-05-08
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Expires: 2003-01-12
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Abstract

Abstract A process for the elimination of ammonia in waste waters from a coke oven battery wherein ammonia-containing waste water or ammonia-containing vapor obtained by means of ammonia separation from the waste water are mixed with flue gas from the coke oven battery and sprayed into a NO x reactor at an elevated temperature with the resulting mixture being subjected to a catalytic redox reaction.

Inventors

  • 👤 Dietrich Wagener
  • 👤 Theo Sander
  • 👤 Karl H. Laue

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 18:43
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/54; B01D53/56; C; C02; C02F; C02F1/00; C02F1/58; C02F1/586; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/903; Y10S210/918; Y10S210/919

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 211 words
A process for concurrently treating an ammonia-containing waste fluid stream and a NO x -containing flue gas from a coking plant comprising: separating the waste fluid stream into a major portion and a minor portion; combining the major portion of the waste fluid stream with the flue gas to form a mixture containing at least a stoichiometric ration of NO x to ammonia; introducing the mixture into a reactor in the form of a spray or vapor; reacting the mixture in a first catalyst bed at a temperature of at least about 250° C. for converting a substantial amount of ammonia in the waste fluid stream and NO x in the flue gas into a nitrogen and water vapor reaction product, the reaction being exothermic; heating the minor portion of the waste fluid stream in the reactor with the heat generated from the reaction of the mixture in the first catalyst bed; and reacting in a second catalyst bed the minor portion of the waste fluid stream with the reaction product of the first catalyst bed for converting a further amount of ammonia in the waste fluid stream and NO x in the flue gas into a nitrogen and water vapor waste gas, and removing said waste gas from said reactor.
Claim 2
Dependent Claim 211 words
A process for concurrently treating an ammonia-containing waste fluid stream and a NO x -containing flue gas from a coking plant comprising: separating the waste fluid stream into a major portion and a minor portion; combining the major portion of the waste fluid stream with the flue gas to form a mixture containing at least a stoichiometric ration of NO x to ammonia; introducing the mixture into a reactor in the form of a spray or vapor; reacting the mixture in a first catalyst bed at a temperature of at least about 250° C. for converting a substantial amount of ammonia in the waste fluid stream and NO x in the flue gas into a nitrogen and water vapor reaction product, the reaction being exothermic; heating the minor portion of the waste fluid stream in the reactor with the heat generated from the reaction of the mixture in the first catalyst bed; and reacting in a second catalyst bed the minor portion of the waste fluid stream with the reaction product of the first catalyst bed for converting a further amount of ammonia in the waste fluid stream and NO x in the flue gas into a nitrogen and water vapor waste gas, and removing said waste gas from said reactor.
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein said ammonia-containing fluid stream is ammonia-containing waste water.
Claim 4
Dependent Claim 24 words
The process of claim 1 wherein said ammonia-containing fluid stream is an ammonia-containing gas obtained from the separation of ammonia from ammonia-containing waste water.
Claim 5
Dependent Claim 20 words
The process of claim 1 wherein said mixture contains an approximate stoichiometric ratio of NO x to NH 3 .
Claim 6
Dependent Claim 21 words
The process of claim 1 wherein the major portion is an amount of about 75% by volume of the waste fluid.

References Cited (Backward Citations)

US1428618A Cited
JPS49118691A Cited
JPS5053271A Cited
US3970739A Cited
SU659533A1 Cited
US4160725A Cited
US4273749A Cited
JPS54110969A Cited
US4272497A Cited
US4294706A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-05-08 1987-11-07 1988-05-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-05-08 1991-11-07 1992-05-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-05-08 1995-11-07 1996-05-08 $7700.00 Window Closed / Lapsed

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