IP Library Granted Patent US 10,765,994
Granted Patent B2
US 10,765,994 · App. 15/672,446 · Granted Sep 8, 2020

System and method of recovering carbon dioxide from an exhaust gas stream

Inventors: Douglas Carl Hofer (Clifton Park, NY); Anthony Herbert Neumayer (Oklahoma City, OK); Joseph Philip DiPietro (Oklahoma City, OK)
Assignee: NextStream CO2, LLC
B01D53/229B01D53/002B01D53/226B01D53/62F25J3/0266B01D53/265B01D2256/22F25J2205/32F25J2205/34F25J2205/40F25J2205/80F25J2210/04F25J2210/70F25J2215/04F25J2230/02F25J2230/04F25J2230/20F25J2240/90F25J2245/02F25J2290/70Y02C10/10Y02C10/12
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Quick Facts
Patent No.
US 10,765,994
App. No.
15/672,446
Granted
Sep 8, 2020
Kind
B2
Abstract

A carbon dioxide capture system includes a first heat exchanger that exchanges heat between an exhaust stream and a lean carbon dioxide effluent stream. The carbon dioxide capture system also includes a second heat exchanger in flow communication with the first heat exchanger. The second heat exchanger is configured to cool the exhaust stream such that a condensate is formed, and the second heat exchanger is configured to channel a condensate stream for injection into the lean carbon dioxide effluent stream. A first turboexpander including a first compressor is driven by a first turbine. The first compressor is coupled in flow communication with the first heat exchanger. The first turbine is coupled in flow communication with the first heat exchanger and configured to expand the lean carbon dioxide effluent stream. The carbon dioxide capture system further includes a carbon dioxide membrane unit coupled in flow communication with the first compressor.

Claims (28)

1. A carbon dioxide capture system comprising:

a first heat exchanger configured to exchange heat between an exhaust stream and a lean carbon dioxide effluent stream;

a second heat exchanger coupled in flow communication with said first heat exchanger, said second heat exchanger configured to cool the exhaust stream such that a condensate is formed, and said second heat exchanger configured to channel a condensate stream for injection into the lean carbon dioxide effluent stream;

at least one turboexpander comprising:

a compressor coupled in flow communication with said first heat exchanger and configured to compress the exhaust stream; and

a turbine coupled in flow communication with said first heat exchanger, said compressor driven by said turbine, said turbine configured to expand the lean carbon dioxide effluent stream; and

a carbon dioxide membrane unit coupled in flow communication with said compressor, said carbon dioxide membrane unit configured to separate the exhaust stream into the lean carbon dioxide effluent stream and a rich carbon dioxide effluent stream, said carbon dioxide membrane unit further configured to channel the lean carbon dioxide effluent stream to said first heat exchanger.

2. The carbon dioxide capture system in accordance with claim 1 further comprising a spray column coupled in flow communication with said second heat exchanger, said spray column configured to inject the condensate stream into the lean carbon dioxide effluent stream.

3. The carbon dioxide capture system in accordance with claim 2 , wherein said spray column is configured to atomize the condensate stream prior to injection into the lean carbon dioxide effluent stream.

4. The carbon dioxide capture system in accordance with claim 2 , wherein said spray column is coupled in flow communication with said first heat exchanger, said spray column configured to exchange heat between the exhaust stream and the condensate stream.

5. The carbon dioxide capture system in accordance with claim 1 , wherein said second heat exchanger is positioned between said first heat exchanger and said compressor.

6. The carbon dioxide capture system in accordance with claim 1 , wherein said second heat exchanger is positioned downstream from said compressor, said second heat exchanger configured to cool a compressed exhaust gas stream received from said compressor to form the condensate.

7. The carbon dioxide capture system in accordance with claim 6 further comprising a pump configured to discharge the condensate stream for injection into the lean carbon dioxide effluent stream.

8. A mobile carbon dioxide capture system comprising:

a transport apparatus;

a carbon dioxide capture system disposed on said transport apparatus, said carbon dioxide capture system comprising:

a first heat exchanger configured to exchange heat between an exhaust stream and a lean carbon dioxide effluent stream;

a second heat exchanger coupled in flow communication with said first heat exchanger, said second heat exchanger configured to cool the exhaust stream such that a condensate is formed, and said second heat exchanger configured to channel a condensate stream for injection into the lean carbon dioxide effluent stream;

at least one turboexpander comprising:

a compressor coupled in flow communication with said first heat exchanger and configured to compress the exhaust stream; and

a turbine coupled in flow communication with said first heat exchanger, said compressor driven by said turbine, said turbine configured to expand the lean carbon dioxide effluent stream; and

a carbon dioxide membrane unit coupled in flow communication with said compressor, said carbon dioxide membrane unit configured to separate the exhaust stream into the lean carbon dioxide effluent stream and a rich carbon dioxide effluent stream, said carbon dioxide membrane unit further configured to channel the lean carbon dioxide effluent stream to said first heat exchanger.

9. The carbon dioxide capture system in accordance with claim 8 further comprising a spray column coupled in flow communication with said second heat exchanger, said spray column configured to inject the condensate stream into the lean carbon dioxide effluent stream.

10. The carbon dioxide capture system in accordance with claim 9 , wherein said spray column is configured to atomize the condensate stream prior to injection into the lean carbon dioxide stream.

11. The carbon dioxide capture system in accordance with claim 9 , wherein said spray column is coupled in flow communication with said first heat exchanger, said spray column configured to exchange heat between the exhaust stream and the first condensate stream.

12. The carbon dioxide capture system in accordance with claim 8 , wherein said second heat exchanger is positioned between said first heat exchanger and said compressor.

13. The carbon dioxide capture system in accordance with claim 8 , wherein said second heat exchanger is positioned downstream from said compressor, said second heat exchanger configured to cool a compressed exhaust gas stream received from said compressor to form the condensate.

14. The carbon dioxide capture system in accordance with claim 13 further comprising a pump configured to discharge the condensate stream for injection into the lean carbon dioxide effluent stream.

Assignments (6)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 19, 2020
From: NEXTSTREAM CO2, LLC
To: AIR PRODUCTS AND CHEMICALS, INC.
Reel/Frame 054414/0438 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 22, 2019
From: BHGE VENTURES & GROWTH, LLC
To: NEXTSTREAM CO2, LLC
Reel/Frame 048093/0965 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 16, 2019
From: BAKER HUGHES, A GE COMPANY, LLC
To: GE OIL & GAS, LLC
Reel/Frame 048029/0165 →
NUNC PRO TUNC ASSIGNMENT Recorded Jan 4, 2019
From: GE OIL & GAS LLC
To: BHGE VENTURES & GROWTH LLC
Reel/Frame 047905/0134 →
NUNC PRO TUNC ASSIGNMENT Recorded Jan 3, 2019
From: GENERAL ELECTRIC COMPANY
To: BAKER HUGHES, A GE COMPANY, LLC
Reel/Frame 047886/0011 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 9, 2017
From: HOFER, DOUGLAS CARL; NEUMAYER, ANTHONY HERBERT; DIPIETRO, JOSEPH PHILIP
To: GENERAL ELECTRIC COMPANY
Reel/Frame 043240/0926 →
Continuity (2)
Continuation In Part 15171775 · Jun 2, 2016
Related Publication 20170368499A1 · Dec 28, 2017