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US4192855A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the simultaneous separation of sulfur and nitrogen oxides from a gaseous mixture

Assignee: Honeywell UOP LLC
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Filing: 1978-04-10
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Granted: 1980-03-11
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Expires: 1998-04-10
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Abstract

Abstract An improved process for the simultaneous separation of sulfur and nitrogen oxides from a gaseous mixture containing said oxides and oxygen is disclosed. The gaseous mixture and ammonia are contacted with a solid sulfur oxides acceptor comprising copper, copper oxide, or mixture thereof dispersed on a carrier material in combination with a nitrogen oxides conversion catalyst consisting of a rare earth metal, metal oxide or mixture thereof.

Inventors

  • 👤 Edward A. Ginger

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 09:14
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8637

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 104 words
A process for the simultaneous separation of oxides of sulfur and nitrogen from a gaseous mixture containing said oxides and oxygen which comprises contacting said mixture and ammonia with a solid sulfur oxides acceptor at a temperature of from about 150° to about 450° C., said solid acceptor comprising copper, copper oxide, or a mixture thereof dispersed on a carrier material in combination with a nitrogen oxides conversion catalyst consisting of cerium metal, cerium oxide, or a mixture thereof, said nitrogen oxides conversion catalyst being present in the range of from about 0.01 to about 2.0 wt. % of said solid sulfur oxides acceptor.
Claim 2
Dependent Claim 104 words
A process for the simultaneous separation of oxides of sulfur and nitrogen from a gaseous mixture containing said oxides and oxygen which comprises contacting said mixture and ammonia with a solid sulfur oxides acceptor at a temperature of from about 150° to about 450° C., said solid acceptor comprising copper, copper oxide, or a mixture thereof dispersed on a carrier material in combination with a nitrogen oxides conversion catalyst consisting of cerium metal, cerium oxide, or a mixture thereof, said nitrogen oxides conversion catalyst being present in the range of from about 0.01 to about 2.0 wt. % of said solid sulfur oxides acceptor.
Claim 3
Dependent Claim 29 words
The process of claim 1 further characterized in that said copper, copper oxide, or mixture thereof comprises from about 5 to about 15 wt. % of said solid acceptor.
Claim 4
Dependent Claim 27 words
The process of claim 1 further characterized in that said carrier material is an alumina with a surface area of at least about 50 m 2 /gm.
Claim 5
Dependent Claim 14 words
The process of claim 1 further characterized in that said carrier material is gamma-alumina.
Claim 6
Dependent Claim 14 words
The process of claim 1 further characterized in that said carrier material is eta-alumina.
Claim 7
Dependent Claim 33 words
The process of claim 1 further characterized in that said ammonia is employed in from about a 0.1:1 to about a 2.5:1 mole ratio with the nitrogen oxides content of said gaseous mixture.
Claim 8
Dependent Claim 36 words
The process of claim 1 further characterized in that said solid acceptor is regenerated by heating the same in contact with a reducing gas comprising hydrogen and from about 50 to about 90 vol. % steam.

References Cited (Backward Citations)

SU451458A1 Cited
GB1438119A Cited
US3914390A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-03-11 1983-09-10 1984-03-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-03-11 1987-09-10 1988-03-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-03-11 1991-09-10 1992-03-11 $7700.00 Window Closed / Lapsed

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