IP Library Granted Patent US 12,420,232
Granted Patent B2
US 12,420,232 · App. 18/604,015 · Granted Sep 23, 2025

Ammonia mediated carbon dioxide (CO

Inventors: Brent R. Constantz (Portola Valley, CA); Jacob Schneider (San Jose, CA); Mark Bewernitz (Los Gatos, CA)
Assignee: Blue Planet Systems Corporation
B01D53/62B01D3/10B01D3/34B01D53/1425B01D53/18B01D53/22B01D53/229B01D53/78B01D53/96B01D53/1475B01D2053/224B01D53/343B01D2251/2062B01D2251/402B01D2251/404B01D2251/602B01D2252/102B01D2252/602B01D2257/504B01D2258/0233B01D2258/0283Y02A50/20Y02C20/40Y02P70/10
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Quick Facts
Patent No.
US 12,420,232
App. No.
18/604,015
Granted
Sep 23, 2025
Kind
B2
Abstract

Methods of sequestering carbon dioxide (CO 2 ) are provided. Aspects of the methods include contacting an aqueous capture ammonia with a gaseous source of CO 2 under conditions sufficient to produce an aqueous ammonium carbonate. The aqueous ammonium carbonate is then combined with a cation source under conditions sufficient to produce a solid CO 2 sequestering carbonate and an aqueous ammonium salt. The aqueous capture ammonia is then regenerated from the from the aqueous ammonium salt. Also provided are systems configured for carrying out the methods.

Claims (24)

1. A method of sequestering CO 2 from a gaseous source of CO 2 , the method comprising:

a) contacting an aqueous capture ammonia with a gaseous source of CO 2 in a combined capture and alkali enrichment reactor under conditions sufficient to produce an aqueous ammonium carbonate;

b) combining a cation source and the aqueous ammonium carbonate under conditions sufficient to produce a CO 2 sequestering carbonate and an aqueous ammonium salt; and

c) regenerating aqueous capture ammonia from the aqueous ammonium salt;

to sequester CO 2 from the gaseous source of CO 2 .

2. The method according to claim 1 , wherein the aqueous capture ammonia comprises ammonia at a concentration ranging from 4.0 to 20.0 M.

3. The method according to claim 1 , wherein the gaseous source of CO 2 is a multi-component gaseous stream.

4. The method according to claim 3 , wherein the gaseous source of CO 2 is a flue gas.

5. The method according to claim 4 , wherein the flue gas is obtained from an industrial source.

6. The method according to claim 1 , wherein the gaseous source of CO 2 is contacted with the aqueous capture ammonia using membrane contactor.

7. The method according to claim 6 , wherein the membrane contactor is a hollow fiber membrane contactor.

8. The method according to claim 1 , wherein the aqueous ammonium carbonate comprises at least one of ammonium carbonate and ammonium bicarbonate.

9. The method according to claim 1 , wherein the aqueous ammonium carbonate comprises both ammonium carbonate and ammonium bicarbonate.

10. The method according to claim 1 , wherein regenerating comprises contacting the aqueous ammonium salt with a mineral alkalinity source.

11. The method according to claim 10 , wherein the mineral alkalinity source comprises a rock.

12. The method according to claim 1 , wherein regenerating the aqueous capture ammonia from the aqueous ammonium salt comprises electrolysis.

13. The method according to claim 1 , wherein the method further comprises contacting the regenerated aqueous capture ammonia with the gaseous source of CO 2 under conditions sufficient to produce the aqueous ammonium carbonate.

14. The method according to claim 1 , wherein the cation source comprises an alkaline earth metal cation.

15. The method according to claim 14 , wherein the cation source is a source of divalent cations.

16. The method according to claim 15 , wherein the divalent cations comprise alkaline earth metal cations.

17. The method according to claim 16 , wherein the divalent alkaline earth metal cations are selected from the group consisting of Ca 2+ and Mg 2+ , and combinations thereof.

18. The method according to claim 1 , wherein the method further comprises producing a building material from the solid CO 2 sequestering carbonate material.

19. The method according to claim 18 , wherein the building material comprises an aggregate.

20. The method according to claim 10 , wherein the mineral alkalinity source comprises a silicate, a carbonate, fly ash, slag, lime or cement kiln dust.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 20, 2024
From: CONSTANTZ, BRENT R.; SCHNEIDER, JACOB; BEWERNITZ, MARK
To: BLUE PLANET, LTD.
Reel/Frame 066840/0419 →
CHANGE OF NAME Recorded Mar 20, 2024
From: BLUE PLANET, LTD.
To: BLUE PLANET SYSTEMS CORPORATION
Reel/Frame 066840/0421 →
Continuity (7)
Continuation 17882830 · Aug 8, 2022
Continuation 17176812 · Feb 16, 2021
Continuation 16397682 · Apr 29, 2019
Continuation 15469405 · Mar 24, 2017
Provisional Application 62451506 · Jan 27, 2017
Provisional Application 62313613 · Mar 25, 2016
Related Publication 20240238723A1 · Jul 18, 2024
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