IP Library › Granted Patent US 10,569,215
Granted Patent B2
US 10,569,215 · App. 15/068,148 · Granted Feb 25, 2020

Systems and methods for reducing the energy requirements of a carbon dioxide capture plant

Inventors: Satish Reddy (Laguna Beach, CA); Joe Yonkoski (Irvine, CA)
Assignee: Fluor Technologies Corporation
B01D53/1425B01D53/1475B01D53/343B01D2252/103B01D2257/504B01D2259/65Y02A50/2342Y02C10/06
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Quick Facts
Patent No.
US 10,569,215
App. No.
15/068,148
Granted
Feb 25, 2020
Kind
B2
Abstract

Systems and methods for reducing the energy requirements for carbon dioxide capture are described. Heat from system processes, such as steam condensation and hot flue gas, is utilized to heat reflux liquid utilized in release of carbon dioxide from absorbent solvent.

Claims (35)

1. A method for reducing an energy requirement of a CO 2 capture process, comprising:

condensing at least a portion of an upper product stream of a stripper to produce a condensed stream;

feeding at least a first portion of the condensed stream to the stripper as a reflux stream;

heating a second portion of the condensed stream in a heat exchanger via heat exchange contact with a heat transfer medium to produce steam;

feeding the steam to the stripper;

withdrawing a solvent stream from the stripper;

heating the solvent stream from the stripper in a reboiler to produce a reboiler stream,

returning the reboiler stream to the stripper; and

cooling and condensing at least a portion of a second heat transfer medium via heat exchange contact with the solvent stream in the reboiler to produce a reboiler condensate, wherein the heat transfer medium comprises the reboiler condensate.

2. The method of claim 1 , wherein the upper product stream comprises CO 2 .

3. The method of claim 2 , wherein the upper product stream further comprises steam.

4. The method of claim 1 , wherein the stripper s configured to receive a CO 2 -rich solvent stream.

5. The method of claim 1 , wherein condensing at least the portion of the upper product stream comprises introducing the upper product stream into a condenser.

6. The method of claim 1 , further comprising:

separating at least a portion of the condensed stream to produce a CO 2 product stream and a condensate stream; and

wherein the at least the portion of the condensed stream comprises at least a portion of the condensate stream.

7. The method of claim 6 , wherein separating at least a portion of the condensed stream comprises introducing the portion of the condensed stream into an accumulator.

8. A method for reducing an energy requirement of a CO 2 capture process, comprising:

condensing at least a portion of an upper product stream of a stripper to produce a condensed stream;

feeding at least a first portion of the condensed stream to the stripper as a reflux stream;

heating a second portion of the condensed stream in a heat exchanger via heat exchange contact with a heat transfer medium to produce steam; and

feeding the steam to the stripper;

withdrawing a solvent stream from the stripper;

heating the solvent stream from the stripper in a reboiler to produce a reboiler stream;

returning the reboiler stream to the stripper, and

cooling and condensing at least a portion of a second heat transfer medium via heat exchange contact with the solvent stream in the reboiler to produce a reboiler condensate, wherein the second heat transfer medium comprises low pressure steam, and wherein the heat transfer medium comprises the reboiler condensate.

9. The method of claim 8 , wherein the upper product stream comprises CO 2 .

10. The method of claim 9 , wherein the upper product stream further comprises steam.

11. The method of claim 8 , wherein the stripper is configured to receive a CO 2 -rich solvent stream.

12. The method of claim 8 , wherein condensing at least the portion of the upper product stream comprises introducing the upper product stream into a condenser.

13. The method of claim 8 , further comprising:

separating at least a portion of the condensed stream to produce a CO 2 product stream and a condensate stream, wherein separating at least a portion of the condensed stream comprises introducing the portion of the condensed stream into an accumulator; and

wherein the at least the portion of the condensed stream comprises at least a portion of the condensate stream.

14. The method of claim 8 , wherein the heat transfer medium comprises an upstream flue gas stream.

15. The method of claim 1 , wherein the heat transfer medium comprises an upstream flue gas stream.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 11, 2016
From: REDDY, SATISH; YONKOSKI, JOE
To: FLUOR TECHNOLOGIES CORPORATION
Reel/Frame 037959/0779 →
Continuity (2)
Division 13737804 · Jan 9, 2013
Related Publication 20160193561A1 · Jul 7, 2016
Cited By (1)
US 12,523,346