Process for producing carbonate compound and cathode active material
US-2015318538-A1 · Nov 5, 2015 · US
US2017309894A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017309894-A1 |
| Application number | US-201515517276-A |
| Country | US |
| Kind code | A1 |
| Filing date | Sep 30, 2015 |
| Priority date | Oct 8, 2014 |
| Publication date | Oct 26, 2017 |
| Grant date | — |
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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.
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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.
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