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US4358428A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of removing nitrogen oxides from waste gas by selective contact reduction

Assignee: NGK Insulators Ltd
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Filing: 1979-07-09
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Granted: 1982-11-09
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Expires: 1999-07-09
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Abstract

Abstract A method of removing nitrogen oxides from waste gas exhausted from a heat power plant and any other various kinds of workshops, etc. is disclosed. The method comprises bringing the waste gas into contact with a honeycomb-shaped catalyst under the following three conditions, i.e. (1) a hydraulic diameter of each of the channels extending through the honeycomb-shaped catalyst is larger than 2.0 mm, preferably 2.0 mm to 30 mm, (2) an open frontal area is larger than 50%, preferably 50% to 80%, and (3) a waste gas speed is higher than 0.5 m/sec, preferably 0.5 m/sec to 60 m/sec.

Inventors

  • 👤 Tadashi Fujita
  • 👤 Shigeo Soejima

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 13:16
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8628; B01J; B01J35/00; B01J35/50; B01J35/56

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 177 words
In a method of removing nitrogen oxides from dirty, dust or soot containing waste gases from stationary fossil fuel burning sources by selective catalytic reduction, comprising adding ammonia gas to said waste gas, and bringing said waste gas containing ammonia gas into contact with a ceramic honeycomb structural body having catalyst material on or in the channel walls thereof, said catalyst material comprising a metal or metal oxide effective for reducing nitrogen oxides in the presence of ammonia to nitrogen and water, the improvement comprising passing said waste gas through said honeycomb body at a gas speed of 0.5-60 m/sec, said body having walls of substantially uniform thickness forming channels extending through said body, said channels having a hydraulic diameter of 2.0-30 mm, and said body having an open frontal area of 50-80%, said body causing a pressure drop of said waste gases passing through said body of not greater than 200 mm. of H 2 O thereby attaining reduction of nitrogen oxides to nitrogen and preventing the channels from being clogged by said dust or soot.
Claim 2
Dependent Claim 177 words
In a method of removing nitrogen oxides from dirty, dust or soot containing waste gases from stationary fossil fuel burning sources by selective catalytic reduction, comprising adding ammonia gas to said waste gas, and bringing said waste gas containing ammonia gas into contact with a ceramic honeycomb structural body having catalyst material on or in the channel walls thereof, said catalyst material comprising a metal or metal oxide effective for reducing nitrogen oxides in the presence of ammonia to nitrogen and water, the improvement comprising passing said waste gas through said honeycomb body at a gas speed of 0.5-60 m/sec, said body having walls of substantially uniform thickness forming channels extending through said body, said channels having a hydraulic diameter of 2.0-30 mm, and said body having an open frontal area of 50-80%, said body causing a pressure drop of said waste gases passing through said body of not greater than 200 mm. of H 2 O thereby attaining reduction of nitrogen oxides to nitrogen and preventing the channels from being clogged by said dust or soot.

References Cited (Backward Citations)

US3565830A Cited
US3502596A Cited
GB1210867A Cited
US3922412A Cited
US3864451A Cited
JPS5062683A Cited
US3958058A Cited
US4026992A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-11-08 1986-05-10 1986-11-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-11-08 1990-05-10 1990-11-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-11-08 1994-05-10 1994-11-09 $7700.00 Window Closed / Lapsed

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