IP Library Granted Patent US 10,597,305
Granted Patent B2
US 10,597,305 · App. 15/755,507 · Granted Mar 24, 2020

Methods for treating lithium-containing materials

Inventors: Jean-François Magnan (Neuville, CA); Guy Bourassa (Québec, CA); Nicolas Laroche (Pont-Rouge, CA); Gary Pearse (Ottawa, CA); Stephen Charles Mackie (Peterborough, CA); Mykolas Gladkovas (Toronto, CA); Peter Symons (Williamsville, NY); J. David Genders (Elma, NY); Geneviève Clayton (Pierrefonds, CA); Pierre Bouchard (Notre-Dame-du-Mont-Carmel, CA); Bertin Ouellet (Bécancour, CA)
Assignee: NEMASKA LITHIUM INC.
C01D15/06B01D61/025B01D61/445B01D61/46B01D61/58C01D15/02C22B1/02C22B3/08C22B3/22C22B7/007C22B26/12C25B1/16C25B9/08C25B15/08Y02P10/234
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,597,305
App. No.
15/755,507
Granted
Mar 24, 2020
Kind
B2
Abstract

The disclosure relates to methods for preparing lithium hydroxide. For example, such methods can comprise mixing a lithium-containing material with an acidic aqueous composition optionally comprising lithium sulfate and thereby obtaining a mixture; roasting the mixture under suitable conditions to obtain a roasted, lithium-containing material; leaching the roasted material under conditions suitable to obtain a first aqueous composition comprising lithium sulfate; submitting the first aqueous composition comprising lithium sulfate to an electromembrane process under suitable conditions for at least partial conversion of the lithium sulfate into lithium hydroxide and to obtain a second aqueous composition comprising lithium sulfate, the electromembrane process involving a hydrogen depolarized anode; optionally increasing concentration of acid in the second aqueous composition; and using the second aqueous composition comprising lithium sulfate as the acidic aqueous composition optionally comprising lithium sulfate for mixing with the lithium-containing material and to obtain the mixture.

Claims (27)

1. A method for preparing lithium hydroxide and recovering lithium sulfate, said method comprising:

mixing a lithium-containing material with an acidic aqueous composition comprising sulfuric acid and optionally comprising lithium sulfate and thereby obtaining a mixture;

roasting said mixture to obtain a roasted, lithium-containing material;

leaching said roasted material under conditions suitable to obtain a first aqueous composition comprising lithium sulfate;

submitting said first aqueous composition comprising lithium sulfate to an electromembrane process under suitable conditions for at least partial conversion of said lithium sulfate into lithium hydroxide and to obtain a second aqueous composition comprising lithium sulfate, said electromembrane process involving a hydrogen depolarized anode;

increasing concentration of acid in said second aqueous composition by removing water from said second aqueous composition by heating said second aqueous composition so as to cause a substantially selective precipitation of lithium sulfate monohydrate and to obtain a third aqueous composition;

recovering said lithium sulfate monohydrate by separating said lithium sulfate monohydrate from said third aqueous composition; and

using said third aqueous composition comprising lithium sulfate as said acidic aqueous composition for mixing with said lithium-containing material and to obtain said mixture.

2. The method of claim 1 , wherein the acid in said acidic aqueous composition is present in a stoichiometric excess of from about 10% to about 100%, based on the amount of lithium in said lithium-containing material.

3. The method of claim 1 , wherein the acid in said acidic aqueous composition is present in a stoichiometric excess of from about 10% to about 40%, based on the amount of lithium in said lithium-containing material.

4. The method of claim 1 , wherein said mixture is roasted at a roasting temperature of from about 200° C. to about 300° C.

5. The method of claim 1 , wherein said lithium-containing material is a lithium-containing ore.

6. The method of claim 5 , wherein said lithium-containing ore comprises β-spodumene.

7. The method of claim 1 , wherein said lithium-containing material further comprises a leachable metal impurity and said first aqueous composition comprising lithium sulfate is further treated under conditions suitable to remove at least a portion of said leachable metal impurity from said first aqueous composition comprising said lithium sulfate.

8. The method of claim 1 , wherein said method further comprises reusing said lithium sulfate monohydrate with said first aqueous composition comprising lithium sulfate in said electromembrane process.

9. The method of claim 1 , wherein said second aqueous composition is heated at a temperature of about 110° C. to about 130° C.

10. The method of claim 9 , wherein said second aqueous composition is heated under reduced pressure or under vacuum.

11. The method of claim 1 , wherein an acid in said acidic aqueous composition is H 2 SO 4 .

12. The method of claim 1 , wherein said electromembrane process comprises a two-compartment monopolar or bipolar membrane electrolysis process and during said two-compartment monopolar or bipolar membrane electrolysis process LiOH current efficiency is at least substantially maintained at a value of about 65% to about 85%.

13. The method of claim 1 , wherein said partial conversion occurs at a conversion of about 30 to about 60%.

14. The method of claim 1 , wherein said partial conversion occurs at a conversion of about 45 to about 55%.

15. The method of claim 1 , wherein said electromembrane process is a two-compartment membrane electrolysis process.

16. The method of claim 15 , wherein said electromembrane process comprises generating hydrogen at a cathode thereof and recovering said hydrogen for feeding said hydrogen depolarized anode.

17. The method of claim 1 , wherein said roasted lithium-containing material is leached with water to obtain said first aqueous composition comprising said lithium sulfate.

18. The method of claim 1 , wherein said lithium sulfate monohydrate is separated from said third aqueous composition by a solid-liquid separation carried out at a temperature of about 15° C. to about 130° C.

19. The method of claim 1 , wherein during said electromembrane process, the pH of said first aqueous composition is acidic.

20. The method of claim 1 , wherein during said electromembrane process, the pH of said first aqueous composition is basic.

Assignments (13)
CHANGE OF ADDRESS FOR ASSIGNEE Recorded May 18, 2023
From: NEMASKA LITHIUM INC.
To: NEMASKA LITHIUM INC.
Reel/Frame 063903/0303 →
RELEASE OF SECURITY INTEREST Recorded Jul 24, 2020
From: NORDIC TRUSTEE AS, AS SECURITY TRUSTEE
To: NEMASKA LITHIUM INC.
Reel/Frame 053310/0334 →
SECURITY INTEREST Recorded Nov 26, 2018
From: NEMASKA LITHIUM INC.
To: OMF FUND II (N) LTD.
Reel/Frame 047578/0664 →
SECURITY INTEREST Recorded Oct 19, 2018
From: NEMASKA LITHIUM INC.
To: NORDIC TRUSTEE AS, AS SECURITY TRUSTEE
Reel/Frame 047236/0560 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: BOUCHARD, PIERRE
To: CENTRE NATIONAL EN ÉLECTROCHIMIE ET EN TECHNOLOGIES ENVIRONNEMENTALES
Reel/Frame 045059/0251 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: CENTRE NATIONAL EN ÉLECTROCHIMIE ET EN TECHNOLOGIES ENVIRONNEMENTALES
To: NEMASKA LITHIUM INC.
Reel/Frame 045059/0463 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: MACKIE, STEPHEN CHARLES; GLADKOVAS, MYKOLAS
To: SGS CANADA INC.
Reel/Frame 045059/0610 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: SGS CANADA INC.
To: NEMASKA LITHIUM INC.
Reel/Frame 045059/0755 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: SYMONS, PETER; GENDERS, J. DAVID
To: ELECTROSYNTHESIS COMPANY
Reel/Frame 045059/0880 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: ELECTROSYNTHESIS COMPANY
To: NEMASKA LITHIUM INC.
Reel/Frame 045059/0961 →
NUNC PRO TUNC ASSIGNMENT Recorded Feb 28, 2018
From: CLAYTON, GENEVIÈVE
To: MET-CHEM CANADA INC.
Reel/Frame 045059/0035 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 28, 2018
From: MAGNAN, JEAN-FRANÇOIS; BOURASSA, GUY; LAROCHE, NICOLAS; PEARSE, GARY; OUELLET, BERTIN
To: NEMASKA LITHIUM INC.
Reel/Frame 045058/0946 →
NUNC PRO TUNC ASSIGNMENT Recorded Feb 28, 2018
From: MET-CHEM CANADA INC.
To: NEMASKA LITHIUM INC.
Reel/Frame 045059/0096 →
Continuity (2)
Provisional Application 62210977 · Aug 27, 2015
Related Publication 20180244531A1 · Aug 30, 2018
Cited By (4)
US 12,275,650 US 12,410,531 US 12,606,456 US 12,636,593