Carbonate Precursors for Lithium Nickel Manganese Cobalt Oxide Cathode Material and the Method of Making Same

US2017309894A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2017309894-A1
Application numberUS-201515517276-A
CountryUS
Kind codeA1
Filing dateSep 30, 2015
Priority dateOct 8, 2014
Publication dateOct 26, 2017
Grant date

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Abstract

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A method for producing a M-carbonate precursor of a Li-M oxide cathode material in a continuous reactor, wherein M=NixMnyCozAn, A being a dopant, with x>0, y>0, 0≦z≦0.35, 0≦n≦0.02 and x+y+z+n=1, the method comprising the steps of: —providing a feed solution comprising Ni-, Mn-, Co- and A-ions, and having a molar metal content M″ feed, —providing an ionic solution comprising either one or both of a carbonate and a bicarbonate solution, the ionic solution further comprising either one or both of Na- and K-ions, —providing a slurry comprising seeds comprising M′-ions and having a molar metal content M′ seeds, wherein M′=Nix′Mny′Coz′A′n′, A′ being a dopant, with 0≦x′≦1, 0≦y′≦1, 0≦z′≦1, 0≦n′≦1 and x′+y′+z′+n′=1, and wherein the molar ratio M′ seeds/M″ feed is between 0.001 and 0.1, —mixing the feed solution, the ionic solution and the slurry in the reactor, thereby obtaining a reactive liquid mixture, —precipitating a carbonate onto the seeds in the reactive liquid mixture, thereby obtaining a reacted liquid mixture and the M-carbonate precursor, and —separating the M-carbonate precursor from the reacted liquid mixture.

First claim

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1 . A method for producing a M-carbonate precursor of a Li-M oxide cathode material in a continuous reactor, wherein M=Ni x Mn y Co z A n , A being a dopant, with x>0, y>0, 0≦z≦0.35, 0≦n≦0.02 and x+y+z+n=1, the method comprising: providing a feed solution comprising Ni-, Mn-, Co- and A-ions, and having a molar metal content M″ feed , providing an ionic solution comprising either one or both of a carbonate and a bicarbonate solution, the ionic solution further comprising either one or both of Na- and K-ions, providing a slurry comprising seeds comprising M′-ions and having a molar metal content M′ seeds , wherein M′=Ni x′ Mn y′ Co z′ A′ n′ , A′ being a dopant, with 0≦x′≦1, 0≦y′≦1, 0≦z′≦1, 0≦n′≦1 and x′+y′+z′+n′=1, and wherein the molar ratio M′ seeds /M″ feed is between 0.001 and 0.1, mixing the feed solution, the ionic solution and the slurry in the reactor, thereby obtaining a reactive liquid mixture, precipitating a carbonate onto the seeds in the reactive liquid mixture, thereby obtaining a reacted liquid mixture and the M-carbonate precursor, and separating the M-carbonate precursor from the reacted liquid mixture. 2 . The method according to claim 1 , wherein the seeds have a median particle size D50 between 0.1 and 3 μm. 3 . The method according to claim 1 , wherein the M′-ions are present in a water insoluble compound that is selected from the group consisting of M′CO 3 , M′(OH) 2 , M′-oxide and M′OOH. 4 . The method according to claim 1 , wherein the Ni-, Mn-, Co- and A-ions are present in a water soluble sulfate compound. 5 . The method according to claim 1 , wherein M′ seeds /M″ feed is between 0.001 and 0.05. 6 . The method according to claim 1 , wherein A and A′ comprise one or more elements selected from the group consisting of Mg, Al, Ti, Zr, Ca, Ce, Cr, Nb, Sn, Zn and B. 7 . The method according to claim 1 , wherein the concentration of NH 3 in the reactor is less than 5.0 g/L. 8 . The method according to claim 1 , wherein M=M′. 9 . The method according to claim 1 , wherein the solid content in the slurry is between 30 and 300 g/L. 10 . The method according to claim 1 , wherein the reactor is a continuous stirred tank reactor (CSTR). 11 . The method according to claim 5 , wherein the median particle size of the M-carbonate precursor is determined by the ratio M′ seeds /M″ feed . 12 . The method according to claim 3 , wherein the water insoluble compound is either MnCO 3 or TiO 2 . 13 . The method according to claim 1 , wherein the ionic solution further comprises a hydroxide solution, and the ratio OH/CO 3 , or OH/HCO 3 , or both these ratios are less than 1/10. 14 . The method according to claim 1 , further comprising the final step of drying and pulverizing the separated M-carbonate precursor, and wherein the ratio M′ seeds /M″ feed is selected to obtain a span <2 of the dried and pulverized M-carbonate precursor. 15 . A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 1 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 16 . A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 4 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 17 . A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 5 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 18 . A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 6 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 19 . A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 8 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 20 . A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 14 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr.

Assignees

Inventors

Classifications

  • H01M4/1391Primary

    of electrodes based on mixed oxides or hydroxides, or on mixtures of oxides or hydroxides, e.g. LiCoOx · CPC title

  • of mixed oxides or hydroxides containing iron, cobalt or nickel for inserting or intercalating light metals, e.g. LiNiO2, LiCoO2 or LiCoOxFy · CPC title

  • Carbonates · CPC title

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

  • Powder tap density · CPC title

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What does patent US2017309894A1 cover?
A method for producing a M-carbonate precursor of a Li-M oxide cathode material in a continuous reactor, wherein M=NixMnyCozAn, A being a dopant, with x>0, y>0, 0≦z≦0.35, 0≦n≦0.02 and x+y+z+n=1, the method comprising the steps of: —providing a feed solution comprising Ni-, Mn-, Co- and A-ions, and having a molar metal content M″ feed, —providing an ionic solution comprising either one or both o…
Who is the assignee on this patent?
Umicore Nv, Umicore Korea Ltd
What technology area does this patent fall under?
Primary CPC classification H01M4/1391. Mapped technology areas include Electricity.
When was this patent published?
Publication date Thu Oct 26 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).