Process for preparing a high-purity nickel sulphate solution

Patent metadata

Field	Value
Publication number	US-2025263306-A1
Application number	US-202319105072-A
Country	US
Kind code	A1
Filing date	Aug 23, 2023
Priority date	Aug 24, 2022
Publication date	Aug 21, 2025
Grant date	—

Abstract

The present invention provides a process for preparing a high-purity nickel sulphate solution, comprising the steps of: i. forming an aqueous mixed metal sulphate solution by reacting sulphuric acid with a raw material feed comprising nickel, manganese, cobalt, and magnesium in an aqueous medium; ii. extracting manganese from said aqueous mixed metal sulphate solution, thereby obtaining a first aqueous raffinate comprising nickel, cobalt and magnesium, and a manganese-rich organic phase; iii. extracting cobalt from said first aqueous raffinate, thereby obtaining a second aqueous raffinate comprising nickel and magnesium, and a cobalt-rich organic phase; and iv. extracting magnesium from said second aqueous raffinate solution, thereby obtaining a high-purity nickel sulphate solution, and a magnesium-rich organic phase.

First claim

1 - 17 . (canceled)

18 . Process for preparing a high-purity nickel sulphate solution, comprising the steps of:
i. forming an aqueous mixed metal sulphate solution by reacting sulphuric acid with a raw material feed comprising nickel, manganese, cobalt and magnesium in an aqueous medium; ii. extracting manganese from said aqueous mixed metal sulphate solution at a temperature between 2° and 45° C. using a first organic phase comprising a first alkylphosphorus-based extractant (I) and a first diluent, wherein said first alkylphosphorus-based extractant (I) comprises an alkylphosphoric acid and/or nickel salts thereof, thereby obtaining a first aqueous raffinate comprising nickel, cobalt and a magnesium content, and a manganese-rich organic phase; iii. extracting cobalt from said first aqueous raffinate at a temperature between 45 and 65° C. using a second organic phase comprising a second alkylphosphorus-based extractant (II) and a second diluent, wherein said second alkylphosphorus-based extractant (II) comprises an alkylphosphinic acid, and/or nickel salts thereof, thereby obtaining a second aqueous raffinate comprising nickel and a residual magnesium content and a cobalt-rich organic phase; and iv. extracting magnesium from said second aqueous raffinate solution using a third organic phase comprising a third alkylphosphorus-based extractant (III) and a third diluent, wherein said third alkylphosphorus-based extractant (III) comprises an alkylphosphinic acid, and/or nickel thereof, thereby obtaining a high-purity nickel sulphate solution and a magnesium-enriched organic phase.

19 . The process according to claim 18 , wherein said raw material feed further comprises iron and/or aluminium, and wherein prior to step ii. a base is added to said aqueous mixed metal sulphate solution formed in step i., thereby forming a precipitate comprising iron and/or aluminium, respectively, and wherein said precipitate is filtered off.

20 . The process according to claim 19 , wherein said base comprises a calcium base, a magnesium base, a cobalt base, a nickel base, or a combination of two or more of the aforementioned bases.

21 . The process according to claim 18 , wherein at least part of said high-purity nickel sulphate solution obtained in step iv. is subjected to crystallization without further purification, and wherein the formed nickel sulphate crystals are used for preparing a cathode precursor material for lithium-ion batteries.

22 . The process according to claim 18 , wherein at least part of said high-purity nickel sulphate solution obtained in step iv. is used without further purification for directly preparing a cathode precursor material for lithium-ion batteries.

23 . The process according to claim 18 , comprising the step of stripping said magnesium-enriched organic phase obtained in step iv. with an aqueous solution comprising a mineral acid.

24 . The process according to claim 18 , wherein said extraction in step iv. is performed at a temperature between 45 and 65° C.

25 . The process according to claim 18 , wherein said first, second and third extractants are preloaded with nickel, i.e., converted to their nickel salts, to a concentration of at least 20% of the available extractant capacity.

26 . The process according to claim 18 , wherein at least part of said high-purity nickel sulphate solution obtained in step iv. is subjected to crystallization, wherein at least part of the mother liquor formed during crystallization is bled, and wherein at least part of the crystallizer bleed is used for the preloading of one or more the organic phases used in steps i., ii., and iii.

27 . The process according to claim 18 , further comprising the step of removing, at least in part, lithium from said aqueous mixed metal sulphate solution prior to step ii.

28 . The process according to claim 18 , comprising step v., step v. comprising stripping said manganese-rich organic phase obtained in step ii. with an aqueous solution comprising a mineral acid.

29 . The process according to claim 18 , comprising step vi., step vi. comprising stripping said cobalt-rich organic phase obtained in step iii. with an aqueous solution comprising a mineral acid.

30 . The process according to claim 18 , wherein said first, second and third organic phase provided in steps ii., iii. and iv. comprise said first, second and third extractant, respectively, in an amount of 5 to 50 vol. %, relative to the total volume of said solvents, and said diluents in an amount of 50 to 95 vol. %, relative to the total volume of said solvents.

31 . The process according to claim 18 , wherein nickel is scrubbed from said manganese-rich organic phase, from said cobalt-rich organic phase and/or from said magnesium-enriched organic phase.

32 . The process according to claim 18 , wherein cobalt is scrubbed from said manganese-rich organic phase.

33 . The process according to claim 18 , wherein said aqueous mixed metal sulphate solution formed in step i. comprises nickel and/or cobalt in an amount of at least 60 at. %, relative to the total metal content of said aqueous mixed metal sulphate solution, and wherein said aqueous mixed metal sulphate solution formed in step i. comprises calcium, magnesium, zinc, copper, and cadmium in an amount of at most 40 at. %, relative to the total metal content of said aqueous mixed metal sulphate solution.

34 . The process according to claim 28 , wherein said first and/or second organic phase, after stripping with said mineral acid, is washed with sulphuric acid.

Assignees

• Umicore Nv

Inventors

• Verdickt Werner
• Roosen Joris
• De Moor Wannes
• Luyten Jan

Classifications

• C22B47/00

  Obtaining manganese · CPC title

• C22B26/22

  Obtaining magnesium · CPC title

• C22B23/0484

  in acidic type solutions · CPC title

• C22B23/0453

  Treatment or purification of solutions, e.g. obtained by leaching (C22B23/0407 takes precedence) · CPC title

• C22B23/043

  Sulfurated acids or salts thereof · CPC title