Improved lithium metal oxide cathode materials and method to make them

Patent metadata

Field	Value
Publication number	US-2016254540-A1
Application number	US-201415028081-A
Country	US
Kind code	A1
Filing date	Oct 16, 2014
Priority date	Oct 24, 2013
Publication date	Sep 1, 2016
Grant date	—

Abstract

An improved method of forming a precipitated transition metal salt useful to make a lithium transition metal oxide useful for making a lithium ion battery comprises the following. A transition metal solution comprised of a dissolved transition metal salt in water and an alkali solution comprised of an alkali salt dissolved in water are introduced into a reactor having an inlet and an outlet connected by a tubular member having therein packing. The rate in which said solutions are introduced are such that the pH of the overall solution in the reactor has pH of 5 to 12 and the time of reaction (mere seconds to several minutes) in the reactor is sufficient to form a precipitated transition metal salt in an effluent liquid. The transition metal salt precipitate in the effluent is discharged from the reactor and the salt separated from the effluent, where it can be purified by washing and dried and subsequently heated with a lithium compound to form a lithium metal oxide useful for making lithium ion batteries.

First claim

1 . A method of forming a precipitated transition metal salt useful to make a lithium transition metal oxide useful for making a lithium ion battery comprising:
(a) providing (i) a transition metal solution comprised of a dissolved transition metal salt in water, and (ii) an alkali solution comprised of an alkali salt dissolved in water, (b) providing a reactor having an inlet and an outlet connected by a tubular member having therein packing, (c) introducing the transition metal solution and alkali solution into the inlet of the plug flow reactor each at a rate to realize a pH (5-12) within the plug flow reactor and a reaction time sufficient to form a precipitated transition metal salt in an effluent liquid; (d) discharging the precipitated transition metal salt in the effluent liquid from the outlet of the reactor; and (e) separating the precipitated transition metal salt from the effluent.

2 . The method of claim 1 , wherein the transition metal solution is comprised of at least two transition metals dissolved therein.

3 . The method of claim 1 , wherein the transition metal solution is comprised of at least three transition metals dissolved therein.

4 . The method of claim 1 , wherein the transition metal salts are a sulfate, chlorite, nitrate, fluorite or combination thereof.

5 . The method of claim 1 , wherein the method is performed in the absence of ammonium.

6 . The method of claim 1 , wherein the plug flow reactor is comprised of two or more plug flow reactors interconnected in series, parallel or a combination thereof.

7 . The method of claim 1 , wherein the plug flow reactor is comprised of at least two plug flow reactors interconnected in parallel in which the alkali solution and transition metal solution are separately introduced into the inlet of each said plug flow reactors such that the effluent are combined to make a combined precipitated transition metal salt and the precipitated transition metal salt from each said plug flow reactor has at least one characteristic dissimilar to the precipitated transition metal salt from each of the other plug flow reactors.

8 . The method of claim 7 , wherein the combined precipitated transition metal salt has a bimodal size distribution.

9 . The method of claim 1 , wherein the packing of the plug flow reactor is comprised of beads.

10 . The method of claim 9 , wherein the packing is beads having a bimodal distribution.

11 . The method of claim 6 , wherein the beads are packed such that the packing results in a void fraction of the plug flow reactor that is 20% to 60%.

12 . The method of claim 1 , wherein the alkali solution, transition metal solution and water are separately pumped into a premixing chamber that is in direct communication with inlet of the plug flow reactor such that said transition metal solution, water, and alkali are contacted with each other prior to introducing into the plug flow reactor.

13 . The method of claim 1 , wherein the transition metal solution has a total molar concentration of transition metal salt from 0.1 to 10 M.

14 . The method of claim 1 , wherein the alkali solution has a total salt concentration of from 0.1 to 20 M.

15 . The method of claim 1 wherein the temperature of the precipitation is from 10° C. to 90° C.

16 . The method of claim 1 , wherein the reaction time is from 5 seconds to 10 minutes.

17 . The method of claim 1 , wherein the precipitated transition metal salt has a secondary particle size distribution that is bi-modal.

18 . A method of forming a lithium metal oxide comprising,
(a) mixing the precipitated transition metal oxide of claim 1 with a source of lithium to form a mixture; and (b) heating the mixture to a temperature and time sufficient to form the lithium metal oxide.

19 . The method of claim 1 , wherein the effluent is recycled by introducing the effluent into the plug flow reactor in step (c).

20 . A lithium ion battery comprised of the lithium metal oxide of claim 18 .

Assignees

• Dow Global Technologies Llc

Inventors

• Lee Edward L
• Zhou Fu

Classifications

• C01G53/82 Primary

  Compounds containing nickel, with or without oxygen or hydrogen, and containing two or more other elements · CPC title

• C01G53/50

  of the type (MnO2)n-, e.g. Li(NixMn1-x)O2 or Li(MyNixMn1-x-y)O2 · CPC title

• C01P2006/40

  Electric properties · CPC title

• H01M4/505 Primary

  of mixed oxides or hydroxides containing manganese for inserting or intercalating light metals, e.g. LiMn2O4 or LiMn2OxFy · CPC title

• H01M4/485

  of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy (H01M4/505, H01M4/525 take precedence) · CPC title