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Process for the reduction of nitrogen oxides in an effluent using sugar

Assignee: Fuel Tech Inc
•
Filing: 1987-03-13
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Granted: 1989-10-31
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Expires: 2007-03-13
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Abstract

Abstract A process is presented for the reduction of nitrogen oxides in the effluent from the combustion of a carbonaceous fuel. The process comprises injecting a treatment agent comprising sugar into an effluent under conditions effective to reduce the concentration of nitrogen oxides in the effluent.

Inventors

  • 👤 William R. Epperly
  • 👤 James C. Sullivan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 15:23
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/54; B01D53/56; Y; Y02; Y02W; Y02W10/00; Y02W10/30; Y02W10/37

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 59 words
A process for the reduction of the concentration of nitrogen oxides in the oxygen-rich effluent from the combustion of a carbonaceous fuel, the process comprising injecting a treatment agent which comprises urea and sugar into an effluent having a temperature of greater than about 1300° F. under conditions effective to reduce the concentration of nitrogen oxides in the effluent.
Claim 2
Dependent Claim 59 words
A process for the reduction of the concentration of nitrogen oxides in the oxygen-rich effluent from the combustion of a carbonaceous fuel, the process comprising injecting a treatment agent which comprises urea and sugar into an effluent having a temperature of greater than about 1300° F. under conditions effective to reduce the concentration of nitrogen oxides in the effluent.
Claim 3
Dependent Claim 10 words
The process of claim 1 wherein said sugar comprises sucrose.
Claim 4
Dependent Claim 18 words
The process of claim 2 wherein the effluent is at a temperature of greater than about 1450° F.
Claim 5
Dependent Claim 16 words
The process of claim 2 wherein the temperature of the effluent is below about 2000° F.
Claim 6
Dependent Claim 12 words
The process of claim 2 wherein said treatment agent is in solution.
Claim 7
Dependent Claim 12 words
The process of claim 5 wherein said solution comprises an aqueous solution.
Claim 8
Dependent Claim 23 words
The process of claim 6 wherein urea is present in said solution in an amount of about 2% to about 60% by weight.
Claim 9
Dependent Claim 23 words
The process of claim 7 wherein sugar is present in said solution in an amount of about 0.5% to about 25% by weight.
Claim 10
Dependent Claim 38 words
The process of claim 3 wherein said treatment agent is injected into the effluent at a molar ratio of the nitrogen contained in said treatment agent to the baseline nitrogen oxides level of about 1:5 to about 10:1.
Claim 11
Dependent Claim 24 words
The process of claim 9 wherein the molar ratio of treatment agent nitrogen to baseline nitrogen oxides level is about 1:3 to about 5:1.
Claim 12
Dependent Claim 21 words
The process of claim 1 wherein said effluent has an excess of oxygen of no greater than about 12% by volume.
Claim 13
Dependent Claim 121 words
A process for the reduction of the concentration of nitrogen oxides in the oxygen-rich effluent from the combustion of a carbonaceous fuel, the process comprising injecting a treatment agent which comprises an aqueous solution of about 2% to about 60% urea by weight and about 0.5% to about 25% sugar by weight into an effluent having an excess of oxygen of about 1% to about 6% by volume and a temperature of about 1450° F. to about 1900° F. in an amount sufficient to provide a molar ratio of the nitrogen contained in said treatment agent to the baseline nitrogen oxides level of about 1:3 to about 5:1 under conditions effective to reduce the concentration of nitrogen oxides in the effluent.
Claim 14
Dependent Claim 121 words
A process for the reduction of the concentration of nitrogen oxides in the oxygen-rich effluent from the combustion of a carbonaceous fuel, the process comprising injecting a treatment agent which comprises an aqueous solution of about 2% to about 60% urea by weight and about 0.5% to about 25% sugar by weight into an effluent having an excess of oxygen of about 1% to about 6% by volume and a temperature of about 1450° F. to about 1900° F. in an amount sufficient to provide a molar ratio of the nitrogen contained in said treatment agent to the baseline nitrogen oxides level of about 1:3 to about 5:1 under conditions effective to reduce the concentration of nitrogen oxides in the effluent.

References Cited (Backward Citations)

US4212853A Cited
US4350669A Cited
US4400362A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1992-10-30 1993-05-01 1993-10-31 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1996-10-30 1997-05-01 1997-10-31 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2000-10-30 2001-05-01 2001-10-31 $7700.00 Window Closed / Lapsed

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