IP Library Granted Patent US 11,542,175
Granted Patent B2
US 11,542,175 · App. 17/477,553 · Granted Jan 3, 2023

Processes for preparing hydroxides and oxides of various metals and derivatives thereof

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.
C01G53/04B01D61/445C01D1/28C01D15/02C01G51/04C01G51/50C01G53/006C01G53/50H01M4/505H01M4/525H01M10/0525H01M10/54B01D2311/2642B01D2311/2673C01P2002/54C01P2002/72C01P2006/40
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Quick Facts
Patent No.
US 11,542,175
App. No.
17/477,553
Granted
Jan 3, 2023
Kind
B2
Abstract

There are provided processes for preparing 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, the 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, sodium hydroxide and/or potassium hydroxide and optionally a chelating agent in order to obtain a solid comprising the metal hydroxide and a liquid comprising lithium sulfate, sodium sulfate and/or potassium sulfate; separating the liquid and the solid from one another to obtain the metal hydroxide; submitting the liquid comprising lithium sulfate, sodium sulfate and/or potassium sulfate to an electromembrane process for converting the lithium sulfate, sodium sulfate and/or potassium sulfate into lithium hydroxide, sodium hydroxide and/or potassium hydroxide respectively; reusing the sodium hydroxide obtained by the electromembrane process for reacting with the metal sulfate; and reusing the lithium hydroxide obtained by the electromembrane process for reacting with the metal sulfate and/or with the metal hydroxide.

Claims (26)

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 and/or a metal nitrate comprising at least one of nickel and cobalt, and optionally at least one metal chosen from manganese, lithium and aluminum with a base chosen from LiOH, NaOH, KOH, RbOH, CsOH, Mg(OH) 2 , Ca(OH) 2 , Sr(OH) 2 , or Ba(OH) 2 and optionally a chelating agent in order to obtain a solid comprising metal hydroxide and a liquid comprising at least one of Li 2 SO 4 Na 2 SO 4 , K 2 SO 4 , Rb 2 SO 4 , Cs 2 SO 4 , MgSO 4 , CaSO 4 , SrSO 4 , BaSO 4 , LiNO 3 NaNO 3 , KNO 3 , RbNO 3 , CsNO 3 , Mg(NO 3 ) 2 , Ca(NO 3 ) 2 , Sr(NO 3 ) 2 and Ba(NO 3 ) 2

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

submitting said liquid comprising at least one of Li 2 SO 4 Na 2 SO 4 , K 2 SO 4 , Rb 2 SO 4 , Cs 2 SO 4 , MgSO 4 , CaSO 4 , SrSO 4 , BaSO 4 , LiNO 3 NaNO 3 , K 2 NO 3 , RbNO 3 , CsNO 3 , Mg(NO 3 ) 2 , Ca(NO 3 ) 2 , Sr(NO 3 ) 2 and Ba(NO 3 ) 2 to an electromembrane process for converting at least one of Li 2 SO 4 Na 2 SO 4 , K 2 SO 4 , Rb 2 SO 4 , Cs 2 SO 4 , MgSO 4 , CaSO 4 , SrSO 4 , BaSO 4 , LiNO 3 NaNO 3 , KNO 3 , RbNO 3 , CsNO 3 , Mg(NO 3 ) 2 , Ca(NO 3 ) 2 , Sr(NO 3 ) 2 and Ba(NO 3 ) 2 into at least one of LiOH, NaOH, KOH, RbOH, CsOH, Mg(OH) 2 , Ca(OH) 2 , Sr(OH) 2 , or Ba(OH) 2 ; and

reusing at least a first portion of said at least one of LiOH, NaOH, KOH, RbOH, CsOH, Mg(OH) 2 , Ca(OH) 2 , Sr(OH) 2 , or Ba(OH) 2 obtained by said electromembrane process for reacting with said metal sulfate and/or metal nitrate;

reacting at least a second portion of said at least one of LiOH, NaOH, KOH, RbOH, CsOH, Mg(OH) 2 , Ca(OH) 2 , Sr(OH) 2 , or Ba(OH) 2 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.

2. 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.

3. 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.

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

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

6. The process of claim 5 , wherein roasting said mixture of metal hydroxides further comprises roasting at a second temperature of at least about 700° C. for a period of time of at least about 8 hours.

7. The process of claim 1 , wherein said electromembrane process comprises an electrolysis membrane process.

8. The process of claim 1 , wherein the chelating agent is chosen from NH 3 , NH 4 OH, acetylacetone, 5-sulfosalicylic acid, and oxalic acid.

9. The process of claim 1 , wherein the chelating agent is chosen from EDTA (ethylenediaminetetraacetic acid) NTA (nitrilotriacetic acid), DCTA (trans-1,2-diaminocyclohexanetetraacetic acid), DTPA (diethylenetriaminepentaacetic acid), and EGTA (ethylene glycol bis(2-aminoethyl ether)-N,N,N′,N′-tetraacetic acid).

10. The process of claim 9 , wherein said chelating agent is present.

11. The process of claim 1 , wherein said metal hydroxide is NiCoAl(OH) 2 or NiMnCo(OH) 2 .

12. The process of claim 1 , wherein said metal hydroxide is chosen from Ni 0.8 Co 0.15 Al 0.05 (OH) 2 , Ni 0.8 Mn 0.1 Co 0.1 (OH) 2 and Ni 0.6 Mn 0.2 Co 0.2 (OH) 2 .

13. The process of claim 1 , wherein said metal oxide is of formula LiMO 2 , wherein M is at least one metal chosen from nickel and cobalt, and optionally further comprises at least one metal chosen from manganese, lithium and aluminum.

14. The process of claim 1 , wherein said lithium hydroxide obtained by said electromembrane process is crystallized before being reacted with said obtained metal hydroxide to obtain a mixture of metal hydroxides.

15. The process of claim 1 , wherein the metal sulfate is a transition metal sulfate.

16. The process of claim 1 , wherein the metal sulfate is obtained from a metal source.

17. The process of claim 16 , wherein the metal source is a transition metal source.

18. The process of claim 1 , wherein purification of the sulfate and/or the hydroxide is carried out by selective precipitation by addition of O 2 , SO 2 or H 2 SO 5 , persulfates, ammonium oxalate, chlorine, HCl, ClO 2 , HClO 3 , O 3 , NaOCl, CoS, Na 2 S, NaHS, CaCO 3 or Na 3 PO 4 .

19. The process of claim 1 , wherein the metal sulfate and/or the metal nitrate is obtained by leaching a metal source, and the leaching is carried out with at least one of H 2 SO 4 , H 2 O 2 , HNO 3 , HCl, nitric acid, citric acid, oxalic acid, aspartic acid, ascorbic acid and glucose.

20. The process of claim 1 , wherein the metal sulfate M(SO 4 ) (with M=Ni, Co, Mn) and optionally Al 2 (SO 4 ) 3 are optionally crystallized before being used as precursor in the synthesis of the metal hydroxide.

Assignments (4)
CHANGE OF ADDRESS FOR ASSIGNEE Recorded May 18, 2023
From: NEMASKA LITHIUM INC.
To: NEMASKA LITHIUM INC.
Reel/Frame 063903/0303 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 31, 2021
From: BOURASSA, GUY; MAGNAN, JEAN-FRANÇOIS; LAROCHE, NICOLAS; BIBIENNE, THOMAS
To: NEMASKA LITHIUM INC.
Reel/Frame 058513/0185 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 31, 2021
From: CHARBONNEAU, MATHIEU; DOLLÉ, MICKAËL
To: UNIVERSITÉ DE MONTRÉAL
Reel/Frame 058513/0203 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 31, 2021
From: UNIVERSITÉ DE MONTRÉAL
To: NEMASKA LITHIUM INC.
Reel/Frame 058513/0256 →
Continuity (4)
Continuation 16766287
Provisional Application 62590260 · Nov 22, 2017
Provisional Application 62735013 · Sep 21, 2018
Related Publication 20220002168A1 · Jan 6, 2022
Cited By (1)
US 12,606,456