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US4268488A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the catalytic reduction of nitrogen oxides in gaseous mixtures

Assignee: Honeywell UOP LLC
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Filing: 1979-05-10
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Granted: 1981-05-19
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Expires: 1999-05-10
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Abstract

Abstract A process for the reductive removal of a nitrogen oxide from a gaseous stream, particularly a stream containing oxygen, water, sulfur dioxide, nitrogen oxide and nitrogen, by contacting the stream with ammonia in the presence of a mixture of two catalysts. The first catalyst comprises copper or a copper compound, preferably copper sulfate supported on a porous carrier material. The second catalyst is a combination of metals or compounds thereof, preferably sulfates of vanadium and iron or tungsten and iron, also dispersed on a porous carrier material.

Inventors

  • 👤 Edward A. Ginger

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 13:32
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8621; B01D53/8625; B01D53/8628; B01J; B01J35/00; B01J35/19

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 148 words
A process for the reductive removal of a nitrogen oxide from a gaseous stream containing said oxide which comprises contacting, at a reductive reaction temperature and pressure, said stream and ammonia with a physical mixture of a first catalyst and a second catalyst, said first catalyst comprising on an elemental basis from about 1 to about 15 wt % copper or a copper compound supported on a first porous carrier material, and said second catalyst comprising on an elemental basis from about 4 to about 10 wt % of a first component selected from the group consisting of vanadium, chromium, molybdenum and tungsten, and compounds thereof, in combination with on an elemental basis from about 4 to about 10 wt % of a second component selected from the group consisting of iron, cobalt and nickel, and compounds thereof, said combination being supported on a second porous carrier material.
Claim 2
Dependent Claim 148 words
A process for the reductive removal of a nitrogen oxide from a gaseous stream containing said oxide which comprises contacting, at a reductive reaction temperature and pressure, said stream and ammonia with a physical mixture of a first catalyst and a second catalyst, said first catalyst comprising on an elemental basis from about 1 to about 15 wt % copper or a copper compound supported on a first porous carrier material, and said second catalyst comprising on an elemental basis from about 4 to about 10 wt % of a first component selected from the group consisting of vanadium, chromium, molybdenum and tungsten, and compounds thereof, in combination with on an elemental basis from about 4 to about 10 wt % of a second component selected from the group consisting of iron, cobalt and nickel, and compounds thereof, said combination being supported on a second porous carrier material.
Claim 3
Dependent Claim 25 words
The process of claim 1 further characterized in that said gaseous stream comprises a mixture of oxygen, water, sulfur dioxide, a nitrogen oxide and nitrogen.
Claim 4
Dependent Claim 34 words
The process of claim 1 further characterized in that said first catalyst comprises on an elemental basis from about 1 to about 15 wt % copper sulfate supported on said first porous carrier material.
Claim 5
Dependent Claim 49 words
The process of claim 1 further characterized in that said first component comprises on an elemental basis from about 4 to about 10 wt % vanadium sulfate or tungsten sulfate and said second component comprises on an elemental basis from about 4 to about 10 wt % iron sulfate.
Claim 6
Dependent Claim 36 words
The process of claim 1 further characterized in that the ratio of the apparent bulk density of said first catalyst to the apparent bulk density of said second catalyst is from about 0.6 to about 1.2.
Claim 7
Dependent Claim 21 words
The process of claim 5 further characterized in that equal volumes of said first catalyst and said second catalyst are utilized.
Claim 8
Dependent Claim 17 words
The process of claim 1 further characterized in that said porous carrier material comprises an inorganic oxide.
Claim 9
Dependent Claim 15 words
The process of claim 7 further characterized in that said inorganic oxide comprises aluminum oxide.
Claim 10
Dependent Claim 38 words
The process of claim 1 further characterized in that said reductive reaction temperature is within a range from about 250° C. to about 400° C. and a pressure within a range from about atmospheric to about 2 psig.
Claim 11
Dependent Claim 29 words
The process of claim 1 further characterized in that said reductive reaction pressure is within a range from about atmospheric pressure to about 10 pounds per square inch gauge.
Claim 12
Dependent Claim 36 words
The process of claim 1 further characterized in that said ammonia is present in an amount sufficient to result in a mole ratio of said ammonia to said nitrogen oxide from about 0.75 to about 1.50.

References Cited (Backward Citations)

US4107272A Cited
US4164546A Cited
JPS522889A Cited
US4070305A Cited
JPS52135889A Cited
US4138368A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-05-18 1984-11-17 1985-05-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-05-18 1988-11-17 1989-05-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-05-18 1992-11-17 1993-05-19 $7700.00 Window Closed / Lapsed

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