Method of preparing material for lithium secondary battery of high performance
View Patent ↗Provided is a method for preparing a lithium mixed transition metal oxide, comprising subjecting Li 2 CO 3 and a mixed transition metal precursor to a solid-state reaction under an oxygen-deficient atmosphere with an oxygen concentration of 10 to 50% to thereby prepare a powdered lithium mixed transition metal oxide having a composition represented by Formula I of Li x M y O 2 wherein M, x and y are as defined in the specification. Therefore, since the high-Ni lithium mixed transition metal oxide having a given composition can be prepared by a simple solid-state reaction in air, using a raw material that is cheap and easy to handle, the present invention enables industrial-scale production of the lithium mixed transition metal oxide with significantly decreased production costs and high production efficiency. Further, the thus-produced lithium mixed transition metal oxide is substantially free of impurities, and therefore can exert a high capacity and excellent cycle stability, in conjunction with significantly improved storage stability and high-temperature stability.
1. A method for preparing a lithium mixed transition metal oxide for a cathode active material, comprising subjecting a mixture of Li 2 CO 3 and a mixed transition metal precursor to a solid-state reaction under an oxygen-deficient atmosphere having an oxygen concentration of 10 to 50% by volume; and forming a powdered lithium mixed transition metal oxide having a composition represented by Formula I:
Li x M y O 2 (I)
wherein:
M=M′ 1−k A k , wherein M′ is Ni 1−a−b (Ni 1/2 Mn 1/2 ) a Co b , 0.65≦a+b≦0.85 and 0.1≦b≦0.4;
A is a dopant;
0≦k<0.05; and
x+y=2 and 0.95≦x≦1.05,
wherein the lithium mixed transition metal oxide has a Li 2 Co 3 content of less than 0.07% by weight of the cathode active material, the lithium mixed transition metal oxide being substantially free of water soluble bases such that less than 20 ml of 0.1M HCl is necessary to titrate 200 ml of a solution containing substantially all of the soluble bases present in 10 g of the lithium mixed transition metal oxide to a pH less than 5, the solution being prepared by repeated soaking and decanting of the lithium mixed transition metal oxide, and the solid-state reaction is a single heat treatment of the mixture.
2. The method according to claim 1 , wherein the oxygen concentration is 10% to 30% by volume.
3. The method according to claim 2 , wherein the atmosphere is air.
4. The method according to claim 1 , wherein the mixed transition metal precursor is at least one selected from the group consisting of M(OH) 2 and MOOH.
5. The method according to claim 4 , wherein the mixed transition metal precursor is MOOH, and is prepared by an ammonia-free process.
6. The method according to claim 1 , wherein the mixed transition metal precursor has a tap density of 1.1 to 1.6 g/cm 3 .
7. The method according to claim 1 , wherein a mixing ratio of Li 2 CO 3 and the mixed transition metal precursor is 0.95 to 1.04:1 wherein the ratio of Li 2 CO 3 :mixed transition metal precursor is a w/w ratio.
8. The method according to claim 1 , wherein the single heat treatment is a sintering process at 600° C. to 1,100° C. for 3 to 20 hours.
9. The method according to claim 8 , wherein an amount of air exceeding 2 m 3 /kg of LiMO 2 during the sintering process is supplied to a reaction vessel equipped with a heat exchanger for pre-warming of the air.
10. The method according to claim 1 , wherein the lithium mixed transition metal oxide is prepared by a large-scale process of 5 kg or more, wherein at least 2 m 3 of air per 1 kg of the lithium mixed transition metal oxide is pumped into or out of a reaction vessel, wherein the at least 2 m 3 of air is the volume measured at room temperature.
11. The method according to claim 10 , wherein at least 10 m 3 of air per 1 kg of the lithium mixed transition metal oxide is pumped into or out of the reaction vessel, wherein the at least 10 m 3 of air is the volume measured at room temperature.
12. The method according to claim 9 , wherein the heat exchanger pre-warms in-flowing air before the in-flowing air enters the reaction vessel, while cooling out-flowing air.