← Back to Patent Explorer
US4649034A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalyzed flue gas desulfurization

Assignee: C0NSOLIDATION COAL Co
•
Filing: 1985-06-14
•
Granted: 1987-03-10
•
Expires: 2005-06-14
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract Flue gas resulting from combustion of sulfur-containing fuel is treated for reduction of its sulfur dioxide content by creating in it a suspension of finely divided sorbent such as lime, and then contacting it at elevated temperature in a vertical contacting zone with a descending shower of sulfur dioxide oxidation catalyst. The resulting sulfur trioxide is captured as a powdered sulfate.

Inventors

  • 👤 Gerald D. Rutledge

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 10:42
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/08; B01J8/12; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01D53/74; B01D53/86; B01D53/8603; B01D53/8609

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 177 words
The method of reducing sulfur dioxide content of flue gas generated by combustion of sulfur-containing fuel which comprises: (a) passing said flue gas containing molecular oxygen at a temperature of at least about 415° C. into a first end of a vertically elongated boiler convection zone; (b) introducing into an upper end of said boiler convection zone a shower of dry particulate oxidation catalyst, said catalyst passing through said boiler convection zone co-currently with exiting gases; (c) removing from a lower end of said boiler convection zone a stream comprising said oxidation catalyst; (d) returning a portion of the removed stream of step (c) to the step of introducing in step (b); (e) providing finely divided dry lime, quicklime, limestone or dolomite sulfur trioxide getter to said flue gas at a point proximate to said first end of said boiler convection zone; and (f) removing from a second end of said boiler convection zone a stream comprising flue gas of diminished sulfur dioxide content carrying a suspension of finely divided reaction product of getter and sulfur trioxide.
Claim 2
Independent Claim 177 words
The method of reducing sulfur dioxide content of flue gas generated by combustion of sulfur-containing fuel which comprises: (a) passing said flue gas containing molecular oxygen at a temperature of at least about 415° C. into a first end of a vertically elongated boiler convection zone; (b) introducing into an upper end of said boiler convection zone a shower of dry particulate oxidation catalyst, said catalyst passing through said boiler convection zone co-currently with exiting gases; (c) removing from a lower end of said boiler convection zone a stream comprising said oxidation catalyst; (d) returning a portion of the removed stream of step (c) to the step of introducing in step (b); (e) providing finely divided dry lime, quicklime, limestone or dolomite sulfur trioxide getter to said flue gas at a point proximate to said first end of said boiler convection zone; and (f) removing from a second end of said boiler convection zone a stream comprising flue gas of diminished sulfur dioxide content carrying a suspension of finely divided reaction product of getter and sulfur trioxide.
Claim 3
Dependent Claim 21 words
The method of claim 1 wherein said first end comprises said upper end, and said second end comprises said lower end.
Claim 4
Dependent Claim 21 words
The method of claim 1 wherein said first end comprises said lower end, and said second end comprises said upper end.
Claim 5
Dependent Claim 21 words
The method of claim 2 wherein said providing of step (e) comprises injecting getter into said flue gas at said point.
Claim 6
Dependent Claim 22 words
The method of claim 2 wherein said providing of step (e) comprises injecting calcium carbonate into a region proximate to said combustion.
Claim 7
Dependent Claim 34 words
The method of claim 2 wherein said oxidation catalyst is of a size consist primarily larger than about 16 mesh, and said getter is of a size consist primarily smaller than about 200 mesh.

References Cited (Backward Citations)

US4330512A Cited
GB2010793A Cited
JPS5645748A Cited
US4356670A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-03-09 1990-09-08 1991-03-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-03-09 1994-09-08 1995-03-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-03-09 1998-09-08 1999-03-10 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag