IP Library › Granted Patent US 12,428,740
Granted Patent B2
US 12,428,740 · App. 18/370,666 · Granted Sep 30, 2025

Li recovery processes and onsite chemical production for Li recovery processes

Inventors: Saad Dara (Vancouver, CA); Beniamin Zahiri (Vancouver, CA)
Assignee: Mangrove Water Technologies LTD.
C25B9/23B01D61/463B01D69/02C01D15/02C01D15/04C01D15/08C01F5/24C01F11/181C02F1/46109C02F1/4693C25B1/16C25B9/19C25B9/21C25B11/032C25B11/046C25B11/048C25B11/052C25B11/053C25B13/00C25C1/02C25C7/02C25C7/04B01D2313/345B01D2325/10B01D2325/36B01D2325/38B01D2325/42C02F2001/46142C02F2001/46166C02F2101/10C02F2103/08C02F2103/10
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Quick Facts
Patent No.
US 12,428,740
App. No.
18/370,666
Granted
Sep 30, 2025
Kind
B2
Abstract

In this disclosure, a process of recycling acid, base and the salt reagents required in the Li recovery process is introduced. A membrane electrolysis cell which incorporates an oxygen depolarized cathode is implemented to generate the required chemicals onsite. The system can utilize a portion of the salar brine or other lithium-containing brine or solid waste to generate hydrochloric or sulfuric acid, sodium hydroxide and carbonate salts. Simultaneous generation of acid and base allows for taking advantage of both chemicals during the conventional Li recovery from brines and mineral rocks. The desalinated water can also be used for the washing steps on the recovery process or returned into the evaporation ponds. The method also can be used for the direct conversion of lithium salts to the high value LiOH product. The method does not produce any solid effluent which makes it easy-to-adopt for use in existing industrial Li recovery plants.

Claims (103)

1. A process for producing a lithium product, the process comprising the steps of:

(a) evaporating water from a lithium brine to concentrate a solution comprising lithium chloride and to precipitate sodium chloride;

(b) reacting the solution comprising lithium chloride with sodium carbonate to produce the lithium product;

(c) mixing water with the sodium chloride from step (a) to produce a solution comprising sodium chloride;

(d) receiving, in a membrane electrolysis cell, the solution comprising sodium chloride and a gas comprising O 2 ; and

(e) delivering, from the membrane electrolysis cell, sodium hydroxide and hydrochloric acid.

2. The process of claim 1 , further comprising reacting at least a portion of the sodium hydroxide delivered in step (e) with CO 2 to produce sodium carbonate, and feeding the sodium carbonate to step (b) for reacting the solution comprising lithium chloride to produce the lithium product.

3. The process of claim 1 , further comprising precipitating at least one of calcium and magnesium from the solution comprising lithium chloride.

4. The process of claim 3 , further comprising feeding at least a portion of the sodium hydroxide delivered in step (e) to the step of precipitating at least one of calcium and magnesium from the solution comprising lithium chloride.

5. The process of claim 1 , further comprising a step of removing boron from the solution comprising lithium chloride.

6. The process of claim 5 , further comprising feeding at least a portion of the hydrochloric acid delivered in step (e) to the step of removing boron from the solution comprising lithium chloride.

7. The process of claim 1 , further comprising a step of selective removal of cations from the solution comprising lithium chloride using an ion exchange resin.

8. The process of claim 7 , further comprising feeding at least a portion of the hydrochloric acid delivered in step (e) to the step of selective removal of cations from the solution comprising lithium chloride to regenerate the ion exchange resin.

9. The process of claim 1 , wherein the membrane electrolysis cell comprises:

an inlet through which the solution comprising sodium chloride is received into an interior of the membrane electrolysis cell;

an anode positioned to extend within the interior of the membrane electrolysis cell and positioned in an anode compartment;

a cathode comprising a gas diffusion electrode positioned to extend within the interior of the membrane electrolysis cell and positioned in a cathode compartment, the gas diffusion electrode comprising a diffusion layer configured to diffuse the gas comprising O 2 and a catalyst layer disposed on a surface of the diffusion layer, the catalyst layer having a hydrophilicity greater than that of the diffusion layer and the catalyst layer being configured to transport negative ions;

a gas inlet positioned in the cathode compartment through which the gas comprising O 2 is introduced into contact with the gas diffusion electrode;

a first ion exchange membrane interposed between the anode compartment and the catalyst layer of the gas diffusion electrode, the first ion exchange membrane being configured to exchange ions received from the anode to an opposed surface of the first ion exchange membrane; and

at least one outlet through which the sodium hydroxide and/or hydrochloric acid are removed from the interior of the membrane electrolysis cell;

wherein in performing the process:

the gas comprising O 2 is reduced at the cathode to form OH − ions;

the solution comprising sodium chloride is received into the anode compartment;

sodium ions are exchanged through the first ion exchange membrane to the opposed surface of the first ion exchange membrane; and

the sodium ions and the OH − ions together form sodium hydroxide.

10. The process of claim 9 , wherein the membrane electrolysis cell further comprises:

a second ion exchange membrane, the second ion exchange membrane being disposed on the catalyst layer of the gas diffusion electrode and being configured to exchange ions received from the catalyst layer of the gas diffusion electrode to an opposed surface of the second ion exchange membrane; wherein the first and second ion exchange membranes define a base build-up compartment interposed between the cathode compartment and the anode compartment;

wherein in performing the process:

the OH − ions are exchanged through the second ion exchange membrane to the opposed surface of the second ion exchange membrane into the base build-up compartment; and

the OH − ions and the sodium ions in the base build-up compartment together form sodium hydroxide.

11. The process of claim 1 , wherein the membrane electrolysis cell comprises:

an inlet through which the solution comprising sodium chloride is received into an interior of the membrane electrolysis cell;

an anode positioned to extend within the interior of the membrane electrolysis cell and positioned in an anode compartment;

a cathode comprising a gas diffusion electrode positioned to extend within the interior of the membrane electrolysis cell and positioned in a cathode compartment, the gas diffusion electrode comprising a diffusion layer configured to diffuse the gas comprising O 2 and a catalyst layer disposed on a surface of the diffusion layer, the catalyst layer having a hydrophilicity greater than that of the diffusion layer and the catalyst layer being configured to transport negative ions;

a gas inlet positioned in the cathode compartment through which the gas comprising O 2 is introduced into contact with the gas diffusion electrode;

a first ion exchange membrane interposed between the anode compartment and the catalyst layer of the gas diffusion electrode, the first ion exchange membrane being configured to exchange ions to an opposed surface of the first ion exchange membrane;

a second ion exchange membrane, the second ion exchange membrane being disposed on the catalyst layer of the gas diffusion electrode and being configured to exchange ions received from the catalyst layer of the gas diffusion electrode to an opposed surface of the second ion exchange membrane, wherein the first and second ion exchange membranes define a base build-up compartment interposed between the cathode compartment and the anode compartment;

a third ion exchange membrane, the third ion exchange membrane being interposed between the first ion exchange membrane and the anode compartment, wherein the first and third ion exchange membranes define a salt depletion compartment interposed between the anode compartment and the base build-up compartment, the third ion exchange membrane being configured to exchange ions received from the salt depletion compartment to an opposed surface of the third ion exchange membrane; and

at least one outlet through which the sodium hydroxide and/or hydrochloric acid are removed from the interior of the membrane electrolysis cell;

wherein in performing the process:

the gas comprising O 2 is reduced at the cathode to form OH − ions;

the OH − ions are exchanged through the second ion exchange membrane to the opposed surface of the second ion exchange membrane into the base build-up compartment;

the solution comprising sodium chloride is received into the salt depletion compartment;

sodium ions are exchanged through the first ion exchange membrane to the opposed surface of the first ion exchange membrane into the base build-up compartment;

the sodium ions and the OH − ions in the base build-up compartment together form the sodium hydroxide; and

chloride ions are exchanged from the salt depletion compartment to the opposed surface of the third ion exchange membrane.

12. The process of claim 11 , wherein the membrane electrolysis cell further comprises:

a fourth ion exchange membrane, the fourth ion exchange membrane being interposed between the third ion exchange membrane and the anode compartment, wherein the third and the fourth ion exchange membranes define an acid build-up compartment interposed between the anode compartment and the salt depletion compartment, the fourth ion exchange membrane being configured to exchange ions received from the anode compartment to an opposed surface of the fourth ion exchange membrane and into the acid build-up compartment;

wherein in performing the process:

H + ions are formed in the anode compartment and the H + ions are exchanged from the anode compartment to the opposed surface of the fourth ion exchange membrane into the acid build-up compartment; and

the H + ions and the chloride ions together form hydrochloric acid.

13. A process for producing a lithium product, the process comprising the steps of:

(a) evaporating water from a lithium brine to concentrate a solution comprising lithium chloride and to precipitate sodium chloride;

(b) refining the solution comprising lithium chloride comprising one or more steps of:

(i) removing boron from the solution comprising lithium chloride;

(ii) precipitating at least one of calcium and magnesium from the solution comprising lithium chloride; and

(iii) removing cations from the solution comprising lithium chloride using an ion exchange resin;

(c) reacting the solution comprising lithium chloride with sodium carbonate to produce the lithium product;

(d) mixing water with the sodium chloride from step (a) to produce a solution comprising sodium chloride;

(e) receiving, in a membrane electrolysis cell, the solution comprising sodium chloride and a gas comprising O 2 ; and

(f) delivering, from the membrane electrolysis cell, sodium hydroxide and hydrochloric acid.

14. The process of claim 13 , wherein the lithium product is lithium carbonate.

15. The process of claim 14 , further comprising reacting the lithium carbonate with sodium hydroxide.

16. The process of claim 13 , wherein the membrane electrolysis cell comprises:

an inlet through which the solution comprising sodium chloride is received into an interior of the membrane electrolysis cell;

an anode positioned to extend within the interior of the membrane electrolysis cell and positioned in an anode compartment;

a cathode comprising a gas diffusion electrode positioned to extend within the interior of the membrane electrolysis cell and positioned in a cathode compartment, the gas diffusion electrode comprising a diffusion layer configured to diffuse the gas comprising O 2 and a catalyst layer disposed on a surface of the diffusion layer, the catalyst layer having a hydrophilicity greater than that of the diffusion layer and the catalyst layer being configured to transport negative ions;

a gas inlet positioned in the cathode compartment through which the gas comprising O 2 is introduced into contact with the gas diffusion electrode;

a first ion exchange membrane interposed between the anode compartment and the catalyst layer of the gas diffusion electrode, the first ion exchange membrane being configured to exchange ions received from the anode to an opposed surface of the first ion exchange membrane; and

at least one outlet through which the sodium hydroxide and/or hydrochloric acid are removed from the interior of the membrane electrolysis cell;

wherein in performing the process:

the gas comprising O 2 is reduced at the cathode to form OH − ions;

the solution comprising sodium chloride is received into the anode compartment;

sodium ions are exchanged through the first ion exchange membrane to the opposed surface of the first ion exchange membrane; and

the sodium ions and the OH − ions together form sodium hydroxide.

17. The process of claim 16 , wherein the membrane electrolysis cell further comprises:

a second ion exchange membrane, the second ion exchange membrane being disposed on the catalyst layer of the gas diffusion electrode and being configured to exchange ions received from the catalyst layer of the gas diffusion electrode to an opposed surface of the second ion exchange membrane; wherein the first and second ion exchange membranes define a base build-up compartment interposed between the cathode compartment and the anode compartment;

wherein in performing the process:

the OH − ions are exchanged through the second ion exchange membrane to the opposed surface of the second ion exchange membrane into the base build-up compartment; and

the OH − ions and the sodium ions in the base build-up compartment together form sodium hydroxide.

18. The process of claim 13 , wherein the membrane electrolysis cell comprises:

an inlet through which the solution comprising sodium chloride is received into an interior of the membrane electrolysis cell;

an anode positioned to extend within the interior of the membrane electrolysis cell and positioned in an anode compartment;

a cathode comprising a gas diffusion electrode positioned to extend within the interior of the membrane electrolysis cell and positioned in a cathode compartment, the gas diffusion electrode comprising a diffusion layer configured to diffuse the gas comprising O 2 and a catalyst layer disposed on a surface of the diffusion layer, the catalyst layer having a hydrophilicity greater than that of the diffusion layer and the catalyst layer being configured to transport negative ions;

a gas inlet positioned in the cathode compartment through which the gas comprising O 2 is introduced into contact with the gas diffusion electrode;

a first ion exchange membrane interposed between the anode compartment and the catalyst layer of the gas diffusion electrode, the first ion exchange membrane being configured to exchange ions to an opposed surface of the first ion exchange membrane;

a second ion exchange membrane, the second ion exchange membrane being disposed on the catalyst layer of the gas diffusion electrode and being configured to exchange ions received from the catalyst layer of the gas diffusion electrode to an opposed surface of the second ion exchange membrane, wherein the first and second ion exchange membranes define a base build-up compartment interposed between the cathode compartment and the anode compartment; and

a third ion exchange membrane, the third ion exchange membrane being interposed between the first ion exchange membrane and the anode compartment, wherein the first and third ion exchange membranes define a salt depletion compartment interposed between the anode compartment and the base build-up compartment, the third ion exchange membrane being configured to exchange ions received from the salt depletion compartment to an opposed surface of the third ion exchange membrane;

at least one outlet through which the sodium hydroxide and/or hydrochloric acid are removed from the interior of the membrane electrolysis cell;

wherein in performing the process:

the gas comprising O 2 is reduced at the cathode to form OH − ions;

the OH − ions are exchanged through the second ion exchange membrane to the opposed surface of the second ion exchange membrane into the base build-up compartment;

the solution comprising sodium chloride is received into the salt depletion compartment;

sodium ions are exchanged through the first ion exchange membrane to the opposed surface of the first ion exchange membrane into the base build-up compartment;

the sodium ions and the OH − ions in the base build-up compartment together form the sodium hydroxide; and

chloride ions are exchanged from the salt depletion compartment to the opposed surface of the third ion exchange membrane.

19. The process of claim 18 , wherein the membrane electrolysis cell further comprises:

a fourth ion exchange membrane, the fourth ion exchange membrane being interposed between the third ion exchange membrane and the anode compartment, wherein the third and the fourth ion exchange membranes define an acid build-up compartment interposed between the anode compartment and the salt depletion compartment, the fourth ion exchange membrane being configured to exchange ions received from the anode compartment to an opposed surface of the fourth ion exchange membrane and into the acid build-up compartment;

wherein in performing the process:

H + ions are formed in the anode compartment and the H + ions are exchanged from the anode compartment to the opposed surface of the fourth ion exchange membrane into the acid build-up compartment; and

the H + ions and the chloride ions together form hydrochloric acid.

20. The process of claim 1 , wherein the lithium product is lithium carbonate.

21. The process of claim 20 , further comprising reacting the lithium carbonate with sodium hydroxide to produce lithium hydroxide.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 1, 2023
From: DARA, SAAD; ZAHIRI, BENIAMIN
To: MANGROVE WATER TECHNOLOGIES LTD.
Reel/Frame 065422/0153 →
Continuity (7)
Continuation 18220021 · Jul 10, 2023
Continuation 18130190 · Apr 3, 2023
Continuation 17883983 · Aug 9, 2022
Continuation 17416413
Provisional Application 62907486 · Sep 27, 2019
Provisional Application 62784324 · Dec 21, 2018
Related Publication 20240011167A1 · Jan 11, 2024
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