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US4197285A Expired / Lapsed US ⏱️ 0.0 years remaining

Regeneration of lime from sulfates for fluidized-bed combustion

Assignee: United States Department of Energy
•
Filing: 1977-12-07
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Granted: 1980-04-08
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Expires: 1997-12-07
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Abstract

Abstract In a fluidized-bed combustor the evolving sulfur oxides are reacted with CaO to form calcium sulfate which is then decomposed in the presence of carbonaceous material, such as the fly ash recovered from the combustion, at temperatures of about 900° to 1000° C., to regenerate lime. The regenerated lime is then recycled to the fluidized bed combustor to further react with the evolving sulfur oxides. The lime regenerated in this manner is quite effective in removing the sulfur oxides.

Inventors

  • 👤 Ralph T. Yang
  • 👤 Meyer Steinberg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 22:26
CPC Classifications
F; F23; F23C; F23C10/00; F23C10/002; B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01J; B01J8/00; B01J8/18; B01J8/24; C; C01; C01F; C01F11/00; C01F11/02

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 112 words
A process for the regeneration of lime in the fluidized-bed combustion of coal comprising: (a) combusting coal containing sulfurous material in a fluidized-bed combustor forming SO 2 in the presence of fluidized bed particulates comprising CaO, wherein the CaO is reacted with the combustion SO 2 to form CaSO 4 ; (b) reacting the particulates comprising the CaSO 4 from the combustor, at a temperature from about 850° C. to about 1100° C., with solid carbonaceous material to form CaO wherein the carbonaceous material comprises fly ash recovered from fluidized-bed combustion; and (c) recycling the particulates comprising the regenerated CaO at substantially the temperature of step (b) to the fluidized bed combustor.
Claim 2
Dependent Claim 112 words
A process for the regeneration of lime in the fluidized-bed combustion of coal comprising: (a) combusting coal containing sulfurous material in a fluidized-bed combustor forming SO 2 in the presence of fluidized bed particulates comprising CaO, wherein the CaO is reacted with the combustion SO 2 to form CaSO 4 ; (b) reacting the particulates comprising the CaSO 4 from the combustor, at a temperature from about 850° C. to about 1100° C., with solid carbonaceous material to form CaO wherein the carbonaceous material comprises fly ash recovered from fluidized-bed combustion; and (c) recycling the particulates comprising the regenerated CaO at substantially the temperature of step (b) to the fluidized bed combustor.
Claim 3
Dependent Claim 15 words
The process of claim 1, wherein the reaction of step (b) is in a kiln.
Claim 4
Dependent Claim 20 words
The process of claim 1, wherein the pressure of the reaction of step (b) is from 1 to 10 atmospheres.
Claim 5
Dependent Claim 14 words
The process of claim 1, wherein the carbonaceous material is a finely divided solid.
Claim 6
Dependent Claim 40 words
The process of claim 1, further comprising, providing a flow of an oxygen-containing gas to react with carbon in the fly ash to maintain the reaction of step (b) at a temperature of from about 850° C. to 1100° C.
Claim 7
Dependent Claim 30 words
The process of claim 1, wherein the temperature of the particulates comprising CaO in step (b) is about the same as the temperature of the fluidized-bed combustion in step (a).
Claim 8
Dependent Claim 34 words
The process of claim 1, further comprising recovering the carbonaceous material as a finely divided solid, and then mixing the said solid with the solid particulates comprising CaSO 4 in the step (b) reaction.
Claim 9
Dependent Claim 16 words
The process of claim 1, wherein the fluidized-bed combustor is at 800° C. to 950° C.
Claim 10
Dependent Claim 21 words
The process of claim 2, wherein the fluidized-bed particulates of step (a) are fed directly to the kiln of step (b).

References Cited (Backward Citations)

US3784676A Cited
US4060588A Cited
US4081522A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-08 1983-10-08 1984-04-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-08 1987-10-08 1988-04-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-08 1991-10-08 1992-04-08 $7700.00 Window Closed / Lapsed

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