Granted Patent B2

US 12,606,456 · App. 18/655,232 · Granted Apr 21, 2026

Inventors: Guy Bourassa (Québec, CA); Jean-François Magnan (Neuville, CA); Nicolas Laroche (Pont-Rouge, CA); Thomas Bibienne (Montréal, CA); Mathieu Charbonneau (Montréal, CA); Mickaël Dollé (Outremont, CA)

Assignee: NEMASKA LITHIUM INC.

C01G53/04B01D61/445C01D1/28C01D15/02C01G51/04C01G51/50C01G53/50C01G53/82H01M4/505H01M4/525H01M10/0525H01M10/54B01D2311/2642B01D2311/2673C01P2002/54C01P2002/72C01P2006/40

Abstract

Claims (30)

1 . A process for preparing a metal oxide comprising (i) at least one metal chosen from nickel and cobalt and optionally (ii) at least one metal chosen from manganese, lithium and aluminum, said process comprising:

reacting a metal sulfate comprising (i) at least one metal chosen from nickel and cobalt and optionally (ii) at least one metal chosen from manganese, lithium and aluminum with lithium hydroxide and optionally a chelating agent to obtain a solid comprising a metal hydroxide comprising (i) at least one metal chosen from nickel and cobalt and optionally (ii) at least one metal chosen from manganese, lithium and aluminum, and a liquid comprising lithium sulfate;

separating said liquid and said solid from one another to obtain said metal hydroxide;

submitting said liquid comprising lithium sulfate to an electromembrane process for converting said lithium sulfate into lithium hydroxide; and

reusing at least a first portion of said lithium hydroxide obtained by said electromembrane process for reacting with said metal sulfate;

reacting at least a second portion of said lithium hydroxide obtained by said electromembrane process with said obtained metal hydroxide to obtain a mixture of metal hydroxides; and

roasting said mixture of metal hydroxides to obtain said metal oxide, wherein said metal oxide is chosen from LiNi 0.33 Mn 0.33 Co 0.33 O 2 , LiNi 0.5 Mn 0.3 Co 0.2 O 2 , LiNi 0.6 Mn 0.2 Co 0.2 O 2 , LiNi 0.8 Mn 0.1 Co 0.1 O 2 and LiNi 0.8 Co 0.15 Al 0.05 O 2 .

2 . The process of claim 1 , wherein LiOH is substantially selectively crystallized and removed from said electromembrane process by evaporative crystallization.

3 . The process of claim 1 , wherein said metal sulfate comprises (i) at least one metal chosen from nickel and cobalt and (ii) at least one metal chosen from manganese, lithium and aluminum.

4 . The process of claim 1 , wherein said solid is a precipitate comprising said metal hydroxide, said precipitate being obtained at a pH of about 9 to about 14.

5 . The process of claim 1 , wherein said solid is a precipitate comprising said metal hydroxide, said precipitate being obtained at a pH of about 10.5 to about 12.5.

6 . The process of claim 1 , wherein said metal sulfate is reacted with lithium hydroxide and a chelating agent that is ammonia.

7 . The process of claim 1 , wherein roasting said mixture of metal hydroxides comprises roasting at a first temperature of at least 350° C. for a period of time of at least 4 hours.

8 . The process of claim 7 , further comprising roasting said mixture of metal hydroxides comprises roasting at a second temperature of at least 600° C. for a period of time of at least 6 hours.

9 . A process for preparing a metal oxide comprising (i) at least one metal chosen from nickel and cobalt and optionally (ii) at least one metal chosen from manganese, lithium and aluminum, said process comprising:

reacting a metal sulfate comprising (i) lithium; (ii) at least one metal chosen from nickel and cobalt and optionally (iii) at least one metal chosen from manganese and aluminum with sodium hydroxide and optionally a chelating agent in order to obtain a solid comprising said metal hydroxide and a liquid comprising sodium sulfate and lithium sulfate;

separating said liquid and said solid from one another to obtain said metal hydroxide;

submitting said liquid comprising sodium sulfate and lithium sulfate to an electromembrane process for converting said sodium sulfate and said lithium sulfate into sodium hydroxide and lithium hydroxide;

separating said lithium hydroxide and said sodium hydroxide from one another;

reusing at least a first portion of said sodium hydroxide obtained by said electromembrane process for reacting with said metal sulfate;

reacting at least a first portion of said lithium hydroxide obtained by said electromembrane process with said obtained metal hydroxide to obtain a mixture of metal hydroxides; and

roasting said mixture of metal hydroxides to obtain said metal oxide, wherein said metal oxide is chosen from LiNi 0.33 Mn 0.33 Co 0.33 O 2 , LiNi 0.5 Mn 0.3 Co 0.2 O 2 , LiNi 0.6 Mn 0.2 Co 0.2 O 2 , LiNi 0.8 Mn 0.1 Co 0.1 O 2 and LiNi 0.8 Co 0.15 Al 0.05 O 2 .

10 . The process of claim 9 , wherein LiOH is substantially selectively crystallized and removed from said electromembrane process by evaporative crystallization.

11 . The process of claim 9 , wherein said metal sulfate comprises (i) lithium;

(ii) at least one metal chosen from nickel and cobalt and (iii) at least one metal chosen from manganese and aluminum.

12 . The process of claim 9 , wherein said solid is a precipitate comprising said metal hydroxide, said precipitate being obtained at a pH of about 9 to about 14.

13 . The process of claim 9 , wherein said solid is a precipitate comprising said metal hydroxide, said precipitate being obtained at a pH of about 10.5 to about 12.5.

14 . The process of claim 9 , wherein said metal sulfate is reacted with lithium hydroxide and a chelating agent that is ammonia.

15 . The process of claim 9 , wherein roasting said mixture of metal hydroxides comprises roasting at a first temperature of at least 350° C. for a period of time of at least 4 hours.

16 . The process of claim 15 , further comprising roasting said mixture of metal hydroxides comprises roasting at a second temperature of at least 600° C. for a period of time of at least 6 hours.

Assignments (3)

Continuity (6)

References Cited (222)