Seawater electrolysis enables mg(oh)2 production and co2 mineralization

Patent metadata

Field	Value
Publication number	US-2024360567-A1
Application number	US-202418592870-A
Country	US
Kind code	A1
Filing date	Mar 1, 2024
Priority date	Oct 18, 2021
Publication date	Oct 31, 2024
Grant date	—

Abstract

A method for producing one or more hydroxide solids includes providing a catholyte comprising an electrolyte solution; contacting the catholyte with an electroactive mesh cathode to electrolytically generate hydroxide ions, thereby precipitating the one or more hydroxide solid(s); and removing the one or more hydroxide solids from the surface of the mesh where they may deposit.

First claim

1 . A method for producing one or more hydroxide solids, the method comprising:
providing:
a basic catholyte solution comprising an electrolyte;
an acidic anolyte solution; and
a neutralization pool comprising an alkaline material;
contacting the basic catholyte solution with a cathode to electrolytically generate hydroxide ions, thereby precipitating the one or more hydroxide solids; and circulating the acidic anolyte solution into the neutralization pool, thereby forming a neutral anolyte solution.

2 . The method of claim 1 , wherein in the electrolyte comprises divalent metal cations.

3 . The method of claim 2 , wherein the divalent cations comprise Mg 2+ , Ca 2+ , or both Mg 2+ and Ca 2+ ions.

4 . The method of claim 3 , wherein the divalent cations comprise Mg 2+ ions.

5 . The method of claim 1 , wherein the basic catholyte solution comprises a brine or sea water.

6 . The method of claim 5 , wherein the basic catholyte solution comprises sea water.

7 . The method of claim 5 , wherein the concentration of NaCl in the brine or sea water is about 1,000 ppm or more, about 2,000 ppm or more, about 3,000 ppm or more, about 4,000 ppm or more, about 5,000 ppm or more, about 6,000 ppm or more, about 7,000 ppm or more, about 8,000 ppm or more, about 9,000 ppm or more, about 10,000 ppm or more, about 15,000 ppm or more, about 20,000 ppm or more, about 25,000 ppm or more, or about 30,000 ppm or more, about 35,000 ppm or more, about 40,000 ppm or more, about 45,000 ppm or more, about 50,000 ppm or more, about 55,000 ppm or more, or about 60,000 ppm or more.

8 . The method of claim 1 , wherein the electrolyte solution has a Ca-equivalent or Mg-equivalent concentration of about 2 ppm or more, about 10 ppm or more, about 50 ppm or more, about 100 ppm or more, about 200 ppm or more, about 300 ppm or more, about 400 ppm or more, about 500 ppm or more, about 600 ppm or more, about 700 ppm or more, about 800 ppm or more, about 900 ppm or more, about 1000 ppm or more, about 11 ppm or more, about 1200 ppm or more, about 1300 ppm or more, about 1400 ppm or more, or about 1500 ppm or more.

9 . (canceled)

10 . The method of claim 1 , wherein the one or more hydroxide solids comprise Mg(OH) 2 and Ca(OH) 2 .

11 . The method of claim 1 , wherein the one or more hydroxide solids comprise Mg(OH) 2 .

12 . (canceled)

13 . The method of claim 1 , further comprising removing the one or more hydroxide solids from the surface of the cathode.

14 - 19 . (canceled)

20 . The method of claim 1 , further comprising forming alkalized effluents having a pH greater than 9.

21 . The method of claim 20 , further comprising forming alkalized effluents having a pH greater than 10.

22 . The method of claim 1 , wherein the acidic anolyte solution comprises an acid.

23 . The method of claim 22 , wherein the acidic anolyte solution has a pH of less than about 6.

24 . The method of claim 1 , further comprising providing a barrier to separate the basic catholyte solution and the acidic anolyte solution.

25 . The method of claim 24 , wherein the barrier comprises a polymer.

26 . (canceled)

27 . (canceled)

28 . The method of claim 27 , wherein the alkaline material comprises mafic materials, ultramafic materials, calcium-rich fly ash, slag, or any combination thereof.

29 . (canceled)

30 . The method of claim 1 , wherein the one or more hydroxide solids comprise Ca(OH) 2 .

31 . A system for the production of one or more hydroxide solids, the system comprising:
an electrolysis reactor comprising:
an electrode assembly disposed within the electrolysis reactor, the electrode assembly comprising:
an anode; and
a cathode
wherein the anode and the cathode are disposed within the electrode assembly and the anode is in ionic communication with the cathode;

a catholyte chamber in fluid and ionic communication with the cathode;
an anolyte inlet and an anolyte outlet in fluid and ionic communication with the anode; and
a neutralization pool, comprising an alkaline material and coupled to the anolyte outlet.

32 . The system of claim 31 , wherein the electrolysis reactor is a multi-compartment reactor.

33 . The system of claim 31 , wherein the system further comprises a single-compartment continuous stirred-tank reactor.

34 . The system of claim 31 , wherein the cathode is a rotating disk cathode.

35 . The system of claim 31 , wherein the electrolysis reactor is a membrane-less electrolysis reactor.

36 . The system of claim 31 , wherein the cathode comprises a metallic composition, non-metallic composition, or hybrid metallic and non-metallic composition.

37 . The system of claim 31 , wherein the cathode comprises stainless steel, titanium oxide, carbon nanotubes, one or more polymers, graphite, or combinations thereof.

Assignees

• Univ California

Inventors

• Chen Xin
• La Plante Erika Callagon
• Sant Gaurav
• Jassby David
• Simonetti Dante Adam
• Traynor Thomas

Classifications

• C25B11/046

  Alloys · CPC title

• C25B13/08

  based on organic materials · CPC title

• C25B9/19

  with diaphragms · CPC title

• C25B15/081

  Supplying products to non-electrochemical reactors that are combined with the electrochemical cell, e.g. Sabatier reactor · CPC title

• C25B11/03 Primary

  perforated or foraminous · CPC title