Claims
- 1. A method of capturing sulfur in a fluidized bed boiler comprising the steps of passing air through a bed of particulate material containing fuel and supported in a housing to fluidize said particulate material, establishing an area to one side of said fluidized bed and isolated from said fluidized bed, introducing into said area a raw acceptor for the sulfur produced as a result of combustion of said fuel, said area being in a heat transfer relation to the heat generated by said fluidized bed to calcine said acceptor, then introducing said calcined acceptor from said area into said bed where it reacts with said sulfur and discharging the sulfated acceptor from said housing.
- 2. The method of claim 1 comprising the step of passing air through said area to fluidize the acceptor in said area to promote the introduction of said acceptor into said bed.
- 3. The method of claim 1 further comprising the step of adding particulate fuel material to said area to add additional heat to said area.
- 4. The method of claim 3 further comprising the step of passing air through said area to promote the combustion of said fuel material in said area.
- 5. The method of claim 1 further comprising the step of introducing carbon dioxide-rich gas to said area to promote the calcining of said acceptor.
- 6. The method of claim 5 further comprising the steps of removing any excess carbon dioxide from said area.
- 7. The method of claim 1 wherein said acceptor is limestone.
- 8. A method of capturing sulfur in a fluidized bed boiler comprising the steps of passing air through a bed of particulate material containing fuel and supported in a housing to fluidize said particulate material, establishing a freeboard space in said housing above said bed of particulate material for receiving heat from said bed of particulate material, introducing into said freeboard space a raw acceptor for the sulfur produced as a result of combustion of said fuel, said freeboard space being in a heat transfer relation to the heat generated by said fluidized bed to calcine said acceptor, then permitting said calcined acceptor to discharge by gravity onto said bed where it reacts with said sulfur and discharging said sulfated acceptor from said bed.
- 9. The method of claim 8 further comprising the step of disposing at least one distribution unit in said freeboard space, said unit adapted to receive said raw acceptor and discharge same after the acceptor is calcined.
- 10. The method of claim 9 wherein two distribution units are disposed in said freeboard space, one of said units adapted to receive said raw acceptor and discharge the acceptor to the other unit, the other unit adapted to discharge the acceptor to the fluidized bed.
- 11. The method of claim 10 wherein said other distribution unit is disposed underneath said one unit and wherein said units are slanted so that said acceptor cascades down said units before discharging into said fluidized bed.
- 12. The method of claim 10 further comprising the steps of sizing said distribution units and regulating the flow rate of said acceptor through said units so that the residence time of said acceptor within said unit is sufficient to enable said acceptor to receive sufficient heat from said bed to calcine said acceptor.
- 13. The method of claim 12 further comprising the step of introducing carbon dioxide-rich gas to said distribution unit to promote the calcining of said acceptor.
- 14. The method of claim 13 further comprising the steps of removing any excess carbon dioxide from said distribution unit.
- 15. The method of claim 8 further comprising the step of positioning an enclosure above said bed in a manner to receive heat from said bed, said enclosure having an inlet for receiving said raw acceptor and an outlet for discharging said calcined acceptor towards said bed.
- 16. The method of claim 15 further comprising the steps of selecting the dimensions of said enclosure, said inlet and said outlets so that the residence time of said acceptor within said enclosure is sufficient to enable said acceptor to receive sufficient heat from said fluidized bed to calcine said acceptor.
- 17. The method of claim 15 further comprising the step of introducing carbon dioxide-rich gas to said enclosure unit to promote the calcining of said acceptor.
- 18. The method of claim 17 further comprising the steps of removing any excess carbon dioxide from said enclosure unit.
- 19. The method of claim 7 wherein said limestone is converted to lime as a result of said calcining.
Parent Case Info
This application is a divisional of application Ser. No. 148,339, filed May 9, 1980, now U.S. Pat. No. 4,333,909.
US Referenced Citations (11)
Divisions (1)
|
Number |
Date |
Country |
Parent |
148339 |
May 1980 |
|