IP Library Granted Patent US 9,707,513
Granted Patent B2
US 9,707,513 · App. 14/636,043 · Granted Jul 18, 2017

Alkali enrichment mediated CO

Inventors: Brent R. Constantz (Portola Valley, CA); Chris Camire (Morgan Hill, CA); Jacob Schneider (San Jose, CA); Mark Bewernitz (Los Gatos, CA)
Assignee: Blue Planet, Ltd.
B01D53/62B01D53/229B01D2053/224B01D2251/304B01D2251/402B01D2251/404B01D2251/604B01D2251/606B01D2252/1035B01D2257/504B01D2258/0283Y02C10/04
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Quick Facts
Patent No.
US 9,707,513
App. No.
14/636,043
Granted
Jul 18, 2017
Kind
B2
Abstract

Methods of sequestering CO 2 from a gaseous source of CO 2 are provided. Aspects of the methods include employing an alkali enrichment protocol, such as a membrane mediated alkali enrichment protocol, in a CO 2 sequestration protocol. Also provided are systems for practicing the methods.

Claims (24)

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

a) subjecting an initial liquid to a membrane mediated alkali enrichment protocol to produce an enhanced alkalinity liquid; and

b) employing the enhanced alkalinity liquid in a CO 2 sequestration protocol to sequester CO 2 that comprises producing a carbonate from a LCP that comprises dissolved inorganic carbon (DIC) obtained from the gaseous source of CO 2 ;

wherein the method further comprises recovering CO 2 gas.

2. The method according to claim 1 , wherein the membrane mediated alkali enrichment protocol comprises contacting first and second liquids to opposite sides of a membrane.

3. The method according to claim 1 , wherein the method comprises contacting the enhanced alkalinity liquid with the gaseous source of CO 2 under conditions sufficient to produce an LCP containing liquid.

4. The method according to claim 1 , wherein the method comprises producing the initial liquid by contacting a source liquid with the gaseous source of CO 2 .

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

6. The method according to claim 5 , wherein the gaseous source of CO 2 is a flue gas.

7. The method according to claim 1 , wherein the gaseous source of CO 2 is contacted with a liquid under conditions such that CO 2 is selectively absorbed by the CO 2 absorbing aqueous medium.

8. The method according to claim 1 , wherein the gaseous source of CO 2 is contacted with the liquid using a hollow fiber membrane contactor.

9. The method according to claim 1 , wherein the carbonate is produced by introducing a cation source into an LCP containing liquid under conditions sufficient to produce the carbonate.

10. The method according to claim 9 , wherein the cation source is introduced into a flowing LCP containing liquid under conditions sufficient such that a non-slurry solid phase CO 2 sequestering carbonate material is produced in the flowing LCP containing liquid.

11. The method according to claim 9 , wherein the cation source is introduced into an LCP containing liquid under conditions sufficient such that a slurry CO 2 sequestering carbonate material is produced from the LCP containing liquid.

12. The method according to claim 9 , wherein the cation source is a source of divalent cations.

13. The method according to claim 12 , wherein the divalent cations comprise alkaline earth metal cations.

14. The method according to claim 13 , wherein the divalent alkaline earth metal cations are selected from the group consisting of Ca 2+ and Mg 2+ , and combinations thereof.

15. The method according to claim 1 , wherein the method further comprises producing a fresh water.

16. The method according to claim 1 , wherein the method is a continuous process.

17. A method for purifying CO 2 from a CO 2 containing multi-component gaseous stream, the method comprising:

a) subjecting an initial liquid to a membrane mediated alkali enrichment protocol to produce an enhanced alkalinity liquid; and

b) employing the enhanced alkalinity liquid in a carbonate production protocol that produces a carbonate and pure CO 2 gas to purify CO 2 from the CO 2 containing multi-component gaseous stream.

18. The method according to claim 17 , wherein the membrane mediated alkali enrichment protocol comprises contacting first and second liquids to opposite sides of a membrane.

19. The method according to claim 17 , wherein the gaseous source of CO 2 is a flue gas.

Assignments (5)
SECURITY INTEREST Recorded Oct 11, 2021
From: BLUE PLANET SYSTEMS CORPORATION
To: SUSTAINABLE WATER TREATMENT LLC
Reel/Frame 057911/0075 →
CHANGE OF NAME Recorded Aug 14, 2020
From: BLUE PLANET, LTD.
To: BLUE PLANET SYSTEMS CORPORATION
Reel/Frame 053496/0760 →
SECURITY INTEREST Recorded Feb 22, 2019
From: BLUE PLANET, LTD
To: SUSTAINABLE WATER TREATMENT LLC
Reel/Frame 048405/0711 →
SECURITY INTEREST Recorded Jan 15, 2019
From: BLUE PLANET, LTD
To: SUSTAINABLE HYDRO, BLUE PLANET, LLC
Reel/Frame 048015/0020 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 24, 2015
From: CONSTANTZ, BRENT R.; CAMIRE, CHRIS; SCHNEIDER, JACOB; BEWERNITZ, MARK
To: BLUE PLANET, LTD.
Reel/Frame 035240/0794 →
Continuity (8)
Provisional Application 61947372 · Mar 3, 2014
Provisional Application 62041568 · Aug 25, 2014
Provisional Application 62051100 · Sep 16, 2014
Provisional Application 61990486 · May 8, 2014
Provisional Application 62056377 · Sep 26, 2014
Provisional Application 62062084 · Oct 9, 2014
Provisional Application 62096340 · Dec 23, 2014
Related Publication 20150246314A1 · Sep 3, 2015