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US4525142A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for treating flue gas with alkali injection and electron beam

Assignee: Hamon Research Cottrell SA
•
Filing: 1984-06-11
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Granted: 1985-06-25
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Expires: 2004-06-11
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Abstract

Abstract A process uses limestone injection into a combustion boiler burning pulverized coal or liquid hydrogen fuel. Effluent gas from the boiler is humidified and cooled to below 200° F. During the humidifying and cooling step, sulfur dioxide removal occurs in addition to that which takes place in the combustion zone of the boiler. The effluent gas and unreacted alkali is then fed into an electron beam irradiation chamber which produces energetic conditions for rapid reaction of sulfur dioxide and nitrogen oxides in the presence of water vapor. The remaining unreacted alkali reacts rapidly and in-situ with the sulfuric acid and nitric acid formed in the electron beam chamber.

Inventors

  • 👤 Robert J. Gleason
  • 👤 Paul L. Feldman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 13:26
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01D53/501; B01D53/60; B01J; B01J19/00; B01J19/08; B01J19/081; B01J19/085; Y; Y02; Y02A; Y02A50/00; Y02A50/20

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 189 words
A process for removing pollutants comprising either sulfur oxides or nitrogen oxides or both from effluent gas, the steps comprising: (a) injecting alkali reagent into the combustion zone of a combustion boiler fired by fuel selected from the group of pulverized coal, liquid hydrocarbon, or mixture thereof, some of said alkali reagent reacting with sulfur oxides in the effluent gas to form a reaction product; (b) passing said effluent gases and said unreacted alkali out of said combustion boiler and into a cooling stage and cooling said effluent gases and unreacted alkali reagent to below 200° F. such that an additional amount of said alkali reagent react with sulfur oxides in the effluent gas to form a reaction product; (c) passing the cooled effluent gas and remaining unreacted alkali reagent into an irradiation chamber; (d) irradiating the effluent gas and unreacted alkali reagent with ionizing radiation in the irradiation chamber causing said unreacted alkali reagent to convert gaseous either sulfur oxides or nitrogen oxides or both into either mist or solid particles or both; and (e) subjecting the irradiated effluent gas to particulate collection in a particulate collection device.
Claim 2
Dependent Claim 189 words
A process for removing pollutants comprising either sulfur oxides or nitrogen oxides or both from effluent gas, the steps comprising: (a) injecting alkali reagent into the combustion zone of a combustion boiler fired by fuel selected from the group of pulverized coal, liquid hydrocarbon, or mixture thereof, some of said alkali reagent reacting with sulfur oxides in the effluent gas to form a reaction product; (b) passing said effluent gases and said unreacted alkali out of said combustion boiler and into a cooling stage and cooling said effluent gases and unreacted alkali reagent to below 200° F. such that an additional amount of said alkali reagent react with sulfur oxides in the effluent gas to form a reaction product; (c) passing the cooled effluent gas and remaining unreacted alkali reagent into an irradiation chamber; (d) irradiating the effluent gas and unreacted alkali reagent with ionizing radiation in the irradiation chamber causing said unreacted alkali reagent to convert gaseous either sulfur oxides or nitrogen oxides or both into either mist or solid particles or both; and (e) subjecting the irradiated effluent gas to particulate collection in a particulate collection device.
Claim 3
Dependent Claim 34 words
The process of claim 1 wherein the cooling of the gas is accomplished by evaporative cooling of water injected into the effluent gas downstream from said combustion boiler and upstream from said irradiation chamber.
Claim 4
Dependent Claim 27 words
The process of claim 2 wherein the process removes up to or at least 90% of sulfur dioxide and nitrogen oxides gas pollutants in the effluent gas.
Claim 5
Dependent Claim 16 words
The process of claim 3 wherein said alkali reagent is injected only into said combustion boiler.
Claim 6
Dependent Claim 22 words
The process of claim 4 wherein the temperature of the effluent gas fed to said particulate collection device is below 200° F.
Claim 7
Dependent Claim 57 words
The process of claim 5 wherein 50 to 60% of the sulfur dioxide in the effluent gas is reacted in the combustion boiler, 25 to 40% of the sulfur dioxide is reacted between the evaporative cooler and the collection device, and 60% of the remaining unreacted sulfur dioxide is converted to sulfur trioxide in said irradiation chamber.
Claim 8
Dependent Claim 22 words
The process of claim 6 wherein at least 90% of unreacted nitrogen oxides are converted to nitric acid in said irradiation chamber.
Claim 9
Dependent Claim 27 words
The process of claim 7 wherein said alkali reagent consists essentially of a member of the group of: lime, limestone, sodium compounds, magnesium compounds, or mixtures thereof.
Claim 10
Dependent Claim 13 words
The process of claim 8 wherein said ionizing radiation is electron beam irradiation.
Claim 11
Dependent Claim 12 words
The process of claim 9 wherein said particulate collection includes electrostatic precipitation.
Claim 12
Dependent Claim 36 words
The process of claim 2 wherein said alkali reagent consists essentially of a member of the group of: lime, limestone, sodium compounds, magnesium compounds, or mixtures thereof, and wherein said ionizing radiation is electron beam irradiation.
Claim 13
Dependent Claim 33 words
The process of claim 2 wherein said alkali reagent reacts to form CaSO 3 in said combustion boiler and in said cooling stage and reacts to form CaSO 4 in said irradiation chamber.

References Cited (Backward Citations)

US2718453A Cited
US3869362A Cited
US3869362B1 Cited
US4004995A Cited
US4004995B1 Cited
US4105744A Cited
US3976747A Cited
US4372832A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-06-24 1988-12-24 1989-06-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-06-24 1992-12-24 1993-06-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-06-24 1996-12-24 1997-06-25 $7700.00 Window Closed / Lapsed

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