IP Library Granted Patent US 8,398,743
Granted Patent B2
US 8,398,743 · App. 11/801,043 · Granted Mar 19, 2013

Methods and systems for reducing carbon dioxide in combustion flue gases

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,398,743
App. No.
11/801,043
Granted
Mar 19, 2013
Kind
B2
Abstract

A method for processing flue-gas, in an exemplary embodiment, includes providing an absorber unit having a membrane contactor, channeling a combustion flue gas along a first surface of the membrane contactor, and channeling an ammonia-based liquid reagent along a second opposing surface of the membrane contactor. The method also includes partially separating the ammonia-based liquid from the flue gas such that the ammonia-based liquid and the flue gas contact at gas-liquid interface areas, defined by a plurality of pores of the membrane contactor, to separate CO 2 from the flue gas by a chemical absorption of CO 2 within the ammonia-based liquid to produce a CO 2 -rich ammonia-based liquid.

Claims (36)

1. A method for processing flue-gas that contains carbon dioxide (CO 2 ), said method comprising:

providing an absorber unit having a membrane contactor that has a surface area of about 10 to about 100 m 2 /gr and a void volume of about 90% to about 95%;

channeling a combustion flue gas along a first surface of the membrane contactor;

channeling an ammonia-based liquid reagent along a second opposing surface of the membrane contactor;

coupling a desorber unit in flow communication with the absorber unit to receive carbon dioxide (CO 2 )-laden ammonia-based liquid reagent from the absorber unit; and

channeling lean ammonia-based liquid reagent discharged from the desorber unit through a steam generator coupled in flow communication between the desorber unit and the absorber unit.

2. A method in accordance with claim 1 further comprising coupling a desorber unit to the absorber unit.

3. A method in accordance with claim 2 further comprising channeling the CO 2 -rich ammonia-based liquid to the desorber unit.

4. A method in accordance with claim 3 further comprising heating the CO 2 -rich ammonia-based liquid to release CO 2 from the CO 2 -rich ammonia-based liquid.

5. A method in accordance with claim 1 wherein providing an absorber unit having a membrane contactor comprises providing an absorber unit having a hydrophobic membrane contactor.

6. A method in accordance with claim 1 wherein providing an absorber unit having a membrane contactor comprises providing an absorber unit having an expanded polytetrafluoroethylene membrane contactor.

7. A combustion system comprising:

an absorber unit comprising:

a housing for channeling a combustion flue gas that contains carbon dioxide (CO 2 );

an ammonia-based liquid reagent channeled within said housing;

a membrane contactor positioned within said housing, wherein said membrane contactor comprises a first surface, a second opposing surface, and a plurality of pores defining gas-liquid interface areas and having a surface area of about 10 to about 100 m 2 /gr and a void volume of about 90% to about 95%, the combustion flue gas is channeled along said first surface and said ammonia-based liquid reagent is channeled along said second opposing surface; and

a desorber unit coupled to said absorber unit, wherein said desorber unit receives and releases CO 2 from the CO 2 -rich ammonia-based liquid; and

a steam generator coupled between said desorber unit and said absorber unit, such that lean ammonia-based liquid reagent discharged from the desorber unit is channeled through said steam generator prior to entering said absorber unit.

8. A combustion system in accordance with claim 7 wherein said membrane contactor comprises a hydrophobic material.

9. A combustion system in accordance with claim 7 wherein said membrane contactor comprises an expanded polytetrafluoroethylene material.

10. A combustion system in accordance with claim 7 wherein said membrane contactor comprises a plurality of hollow fibers.

11. A combustion system in accordance with claim 10 wherein said plurality of hollow fibers is packaged in a tube-and-shell arrangement.

12. A combustion system in accordance with claim 7 wherein said membrane contactor comprises a substantially planar sheet.

13. A combustion system in accordance with claim 12 wherein said substantially planar sheet is packaged as a spiral-wound module.

14. A flue-gas processing system comprising:

a housing for channeling a combustion flue gas that contains carbon dioxide (CO 2 );

an ammonia-based liquid reagent channeled within said housing; and

a membrane contactor positioned within said housing, wherein said membrane contactor comprises a first surface, a second opposing surface, and a plurality of pores defining gas-liquid interface areas, said membrane contactor having a surface area of about 10 to about 100 m 2 /gr and a void volume of about 90% to about 95%, the combustion flue gas is channeled along said first surface and said ammonia-based liquid reagent is channeled along said second opposing surface;

a desorber unit coupled to said housing for receiving carbon dioxide (CO2)-laden ammonia-based liquid reagent from said housing; and

a steam generator coupled in flow communication with said desorber unit, for receiving a lean ammonia-based liquid reagent discharged from said desorber unit and for channeling the lean ammonia-based liquid reagent to said housing.

15. A flue-gas processing system in accordance with claim 14 wherein said membrane contactor comprises a hydrophobic material.

16. A flue-gas processing system in accordance with claim 14 wherein said membrane contactor comprises an expanded polytetrafluoroethylene material.

17. A flue-gas processing system in accordance with claim 14 wherein said membrane contactor comprises a plurality of hollow fibers.

18. A flue-gas processing system in accordance with claim 17 wherein said plurality of hollow fibers is packaged in a tube-and-shell arrangement.

19. A flue-gas processing system in accordance with claim 14 wherein said membrane contactor comprises a substantially planar sheet.

20. A flue-gas processing system in accordance with claim 19 wherein said substantially planar sheet is packaged as a spiral-wound module.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 3, 2014
From: GENERAL ELECTRIC COMPANY; BHA GROUP, INC.; ALTAIR FILTER TECHNOLOGY LIMITED
To: BHA ALTAIR, LLC
Reel/Frame 031911/0797 →