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US4519995A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of desulfurizing flue gases of coal firings

Assignee: OSTERREICHISCHE DRAUKFTWERKE AG
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Filing: 1982-11-19
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Granted: 1985-05-28
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Expires: 2002-11-19
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Abstract

Abstract In a method for desulfurizing flue gas generated in coal combusting plants, the coal is burned in the presence of a dry additive material, such as CaCO optionally in presence of recycled cold flue gas whereby additive material which has not reacted is discharged together with the flue gas from the firing space and is separated together with the ashes in dust filters. The relative moisture of the flue gas is increased before entering the dust filter so that the sulfur compounds in the flue gas react to a greater extent with the additive material in the dust filters. The device for practicing this method comprises a heat exchanger and/or an injection cooler arranged streamup of the flue gas filtering installation.

Inventors

  • 👤 Herbert Schrofelbauer
  • 👤 Gernot Staudinger

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 20:49
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; F; F23; F23C; F23C9/00; F23C9/003; F23J; F23J15/00; F23J15/02; F23J15/022; F23J15/025; F23J15/06; F23K; F23K1/00; Y; Y02; Y02E; Y02E20/00; Y02E20/30

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 152 words
A method of desulfurizing flue gas generated in a coal-combusting installation operating with dry additives selected from the group consisting of calcium oxide and calcium carbonate wherein coal is fired in a combustion chamber in the presence of the dry additives reacting with sulfur oxide components, then the stream of flue gas having normally a temperature of about 150° C. and being laden with ashes and residual additives is discharged from the combustion chamber and supplied to a dust filter where the flue gas is separated from the ashes and residual additives, comprising the step of increasing the relative moisture of the discharged stream before its entry in the filter by cooling the discharged stream to a lower temperature which exceeds the temperature of condensation point of water present in the stream, thus enhancing reaction of sulfur oxide components still present in the flue gas with the residual additives in the filter.
Claim 2
Independent Claim 152 words
A method of desulfurizing flue gas generated in a coal-combusting installation operating with dry additives selected from the group consisting of calcium oxide and calcium carbonate wherein coal is fired in a combustion chamber in the presence of the dry additives reacting with sulfur oxide components, then the stream of flue gas having normally a temperature of about 150° C. and being laden with ashes and residual additives is discharged from the combustion chamber and supplied to a dust filter where the flue gas is separated from the ashes and residual additives, comprising the step of increasing the relative moisture of the discharged stream before its entry in the filter by cooling the discharged stream to a lower temperature which exceeds the temperature of condensation point of water present in the stream, thus enhancing reaction of sulfur oxide components still present in the flue gas with the residual additives in the filter.
Claim 3
Dependent Claim 22 words
A method as defined in claim 1, wherein a partial stream of cold recycled flue gas is applied to the combustion chamber.
Claim 4
Dependent Claim 35 words
A method as defined in claim 1, wherein the relative increase of moisture is accomplished by cooling down the discharged stream by means of a heat exchanger and by spraying water into the discharged stream.
Claim 5
Dependent Claim 24 words
A method as defined in claim 1, wherein the temperature of the discharged stream is reduced to a value between 50° and 100° C.
Claim 6
Dependent Claim 31 words
A method as defined in claim 1, wherein the relative moisture of the discharged flue gas stream is increased to a value between 50% and 100%, preferably between 80% and 100%.

References Cited (Backward Citations)

FR1424831A Cited
US3505008A Cited
US4105744A Cited
US3976747A Cited
DE2625280A1 Cited
DE2539500A1 Cited
US4185080A Cited
US4197278A Cited
US4197278B1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-05-27 1988-11-26 1989-05-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-05-27 1992-11-26 1993-05-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-05-27 1996-11-26 1997-05-28 $7700.00 Window Closed / Lapsed

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