Energy efficient removal of CO2 from air by integrating with H2 generation

Patent metadata

Field	Value
Publication number	US-11207643-B2
Application number	US-202016924573-A
Country	US
Kind code	B2
Filing date	Jul 9, 2020
Priority date	Feb 8, 2018
Publication date	Dec 28, 2021
Grant date	Dec 28, 2021

Abstract

A method of removing carbon dioxide from an atmosphere and generating hydrogen includes capturing carbon dioxide from the atmosphere in an alkaline capture solution, sending the alkaline capture solution to a series of electrolyzers in a CO2-rich path, wherein each electrolyzer cell raises the acidity of the input CO2-rich solution to produce an acidified CO2-rich solution, removing carbon dioxide from the acidified CO2-rich solution at a carbon dioxide removal unit operation to produce a CO2-poor solution, sending the CO2-poor solution to the series of electrolyzers in a return path, wherein each electrolyzer raises the alkalinity of the return CO2-poor solution to produce a basified CO2-poor solution, wherein a difference in pH between the CO2-rich solution and the CO2-poor solution within each electrolyzer is less than 3, and returning the basified CO2-poor solution to the carbon dioxide capture unit operation.

First claim

What is claimed is:

1. A method of removing carbon dioxide from an atmosphere, comprising:
capturing carbon dioxide from the atmosphere in an alkaline capture solution;
sending the alkaline capture solution to a series of electrolyzers in a CO 2 -rich path, wherein each electrolyzer raises the acidity of the input CO 2 -rich solution to produce an acidified CO 2 -rich solution;
removing carbon dioxide from the acidified CO 2 -rich solution at a carbon dioxide removal unit operation to produce a CO 2 -poor solution;
sending the CO 2 -poor solution to the series of electrolyzers in a return path, wherein each electrolyzer raises the alkalinity of the return CO 2 -poor solution to produce a basified CO 2 -poor solution, wherein a difference in pH between the CO 2 -rich solution and the CO 2 -poor solution within each electrolyzer is less than 3; and
returning the basified CO 2 -poor solution to a carbon dioxide capture unit operation.

2. The method of claim 1 , further comprising mixing an output of at least one electrolyzer in a mixing vessel to allow more time for reactions before flowing the solution into an input of a next electrolyzer in at least one of the series of electrolyzers in the CO2-rich path or the series of electrolyzers in the return path.

3. The method of claim 1 , wherein the alkaline solution comprises at least one of the group consisting of: KOH; KHCO 3 ; K 2 CO 3 ; NaOH; Na 2 CO 3 ; and NaHCO 3 .

4. The method of claim 1 , further comprising capturing oxygen produced by electrolysis by one ore more of the electrolyzers in the CO 2 -rich path combined with at least one of minimizing or reabsorbing entrained CO 2 .

5. The method of claim 1 , wherein capturing carbon dioxide from the atmosphere in the alkaline carbon solution comprises capturing carbon dioxide from the atmosphere in an alkaline capture solution having a pH of 14 or less, and wherein sending the alkaline capture solution to a series of electrolyzers in a CO 2 -rich path does not reduce the pH in the system to less than 4.

6. The method of claim 1 , further comprising controlling the pressures in the electrolyzers to be higher than a partial pressure of carbon dioxide in the CO 2 -rich output solution.

7. The method of claim 1 , further comprising lowering pressure in the carbon dioxide removal unit operation to drive carbon dioxide out of the CO 2 -rich solution.

8. The method of claim 1 , further comprising adding a salt that is not redox active to the alkaline capture solution.

9. The method of claim 1 , further comprising using the carbon dioxide removed by the carbon dioxide removal unit operation and hydrogen produced by electrolysis by at least one of the electrolyzers to synthesize liquid fuels.

10. The method of claim 1 , further comprising powering one or more of the electrolyzers using renewable electricity.

11. The method of claim 1 , further comprising completing a circuit by conducting at least one of potassium or sodium ions through a cation exchange membrane in at least one of the electrolyzers.

12. The method of claim 1 , wherein sending the CO2-poor solution to the series of electrolyzers in a return path, and sending the alkaline capture solution to a series of electrolyzers in a CO2-rich path comprises sending the CO 2 -poor and alkaline input solutions into each of the electrolyzers as countercurrent flows.

13. The method of claim 1 , further comprising limiting bubbling of CO 2 from the CO 2 -rich solution anywhere but in the carbon dioxide removal unit operation.

14. The method of claim 1 , further comprising reducing pressure in at least one of the electrolyzers to degas the CO 2 and using a flow resulting from reducing the pressure to power regenerators to drive electricity generation in tandem with reducing the pressure.

15. The method of claim 1 , further comprising sequestering at least some of the CO 2 removed at the carbon dioxide removal unit operation.

16. The method of claim 1 , further comprising venting the acidified CO 2 -rich solution under pressure to remove oxygen.

17. The method of claim 1 further comprising using at least part of the acidified CO 2 -rich solution for oxycombustion of oxygen and CO 2.

18. The method of claim 1 , further comprising transferring heat from the carbon capture unit operation to one of more of the electrolyzers.

Assignees

• Palo Alto Res Ct Inc

Inventors

• Torres Francisco E
• Beh Eugene Shin Ming
• Baker Rivest Jessica Louis

Classifications

• B01D2251/606

  Carbonates · CPC title

• B01D2251/306

  of potassium · CPC title

• B01D53/1493

  Selection of liquid materials for use as absorbents · CPC title

• B01D2258/0283

  Flue gases · CPC title

• B01D2256/16

  Hydrogen · CPC title