MIXED LITHIUM TRANSITION METAL OXIDE COATED WITH PYROGENICALLY PRODUCED ZIRCONIUM-CONTAINING OXIDES
20220289589 · 2022-09-15
Assignee
Inventors
Cpc classification
C01P2004/64
CHEMISTRY; METALLURGY
H01M4/525
ELECTRICITY
C01P2004/62
CHEMISTRY; METALLURGY
C01G53/006
CHEMISTRY; METALLURGY
H01M4/505
ELECTRICITY
H01M4/131
ELECTRICITY
Y02E60/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
H01M10/0525
ELECTRICITY
International classification
Abstract
Process for producing a coated mixed lithium transition metal oxide, wherein a mixed lithium transition metal oxide and a pyrogenically produced zirconium dioxide and/or a pyrogenically produced mixed oxide comprising zirconium are subjected to dry mixing by means of an electric mixing unit having a specific electrical power of 0.05-1.5 kW per kg of the mixed lithium transition metal oxide; coated mixed lithium transition metal oxide obtainable by this process; cathode for a lithium battery and lithium battery comprising such coated particles.
Claims
1. A process for producing a coated mixed lithium transition metal oxide, the process comprising: dry mixing a mixed lithium transition metal oxide and a zirconium source which is at least one selected from the group consisting of a pyrogenically produced zirconium dioxide and a pyrogenically produced mixed oxide comprising zirconium, wherein the dry mixing is performed using an electric mixing unit having a specific electrical power of 0.05 to 1.5 kW per kg of the mixed lithium transition metal oxide.
2. The process of claim 1, wherein: the specific electrical power of the electric mixing unit is 0.1 to 1000 kW.
3. The process of claim 1, wherein: a volume of the electric mixing unit used is 0.1 L to 2.5 m.sup.3.
4. The process of claim 1, wherein: a speed of a mixing tool in the electric mixing unit is 5 to 30 m/s.
5. The process of claim 1 to, wherein: the zirconium source has a BET surface area of 5 to 200 m.sup.2/g.
6. The process of claim 1, wherein: the zirconium source is in the form of aggregated primary particles, the primary particles having a numerical mean diameter of 5 to 100 nm, as determined by transition electron microscopy (TEM).
7. The process of claim 1, wherein: the zirconium source has a mean particle diameter d.sub.50 of 10 to 150 nm, as determined by static light scattering (SLS).
8. The process of claim 1, wherein: the zirconium source has a particle size span (d.sub.90-d.sub.10)/d.sub.50 of 0.4 to 1.2, as determined by static light scattering (SLS).
9. The process of claim 1, wherein: the pyrogenically produced mixed oxide comprising zirconium further comprises lithium and optionally comprises at least one selected from the group consisting of lanthanum and aluminium.
10. The process of claim 1, wherein: the mixed lithium transition metal oxide is at least one selected from the group consisting of a lithium-cobalt oxide, a lithium-manganese oxide, a lithium-nickel-cobalt oxide, a lithium-nickel-manganese-cobalt oxide, a lithium-nickel-cobalt-aluminium oxide, and a lithium-nickel-manganese oxides, or a mixture thereof.
11. The process of claim 1, wherein: the zirconium source is present in an amount of 0.05% to 5% by weight, based on a total weight of the mixed lithium transition metal oxide and the zirconium source.
12. A coated mixed lithium transition metal oxide comprising a zirconium material which is at least one selected from the group consisting of a pyrogenically produced zirconium dioxide and a pyrogenically produced mixed oxide comprising zirconium, the zirconium material having a number average particle size d.sub.50 of 10 nm to 150 nm, and being present on thea surface of the mixed lithium transition metal oxide.
13. An active positive electrode material for a lithium battery comprising the coated mixed lithium transition metal oxide of claim 12.
14. A lithium battery comprising the coated mixed lithium transition metal oxide of claim 12.
15. (canceled)
Description
EXAMPLES
[0078] Starting Materials
[0079] Fumed ZrO.sub.2 with a specific surface area (BET) of 40-60 m.sup.2/g, was produced by flame spray pyrolysis according to Example 1 of WO 2009053232 A1.
[0080] Commercial “nano ZrO.sub.2” powder (particle size 20-30 nm) with BET surface area of ≥35 m.sup.2/g, was supplied by ChemPUR Feinchemikalien and Forschungsbedarf GmbH
[0081] Commercial mixed lithium nickel manganese cobalt oxide powder NMC (7-1.5-1.5) (Type PLB-H7) with a BET surface area of 0.30-0.60 m.sup.2/g, a medium particle diameter d.sub.50=10.6±2 μm (determined by static laser scattering method), was supplied by Linyi Gelon LIB Co.
[0082] Particle Size Distribution of Different ZrO.sub.2 Types
[0083] The samples of a fumed ZrO.sub.2 or a commercial “nano ZrO.sub.2” powder (5 wt %) were dispersed in the solution of sodium pyrophosphate (0.5 g/L) in distilled water and treated at 25° C. for 1 minute in an external ultrasonic bath (160 W).
[0084]
Example 1
[0085] The NMC-powder (217,8 g) was mixed with 2,2 g (1.0 wt %) of the fumed ZrO.sub.2-powder in a high intensity laboratory mixer (Somakon mixer MP-GL with a 0.5 L mixing unit) at first for 1 min at 500 rpm (specific electrical power: 350W/kg NMC) to homogeneously mix the two powders. Afterwards the mixing intensity was increased to 2000 rpm (specific electrical power: 800 W/kg NMC, tip-speed of the mixing tool in the mixing unit: 10 m/s) and the mixing was continued for 5 min to achieve the dry coating of the NMC particles by ZrO.sub.2.
[0086] The coated NMC particles showed a ZrO.sub.2-coating layer thickness of 10-200 nm, as determined by TEM analysis.
Comparative Example 1
[0087] The procedure of Example 1 was repeated exactly with the only difference, that “nano ZrO.sub.2” powder was used instead of fumed ZrO.sub.2.
[0088] Analysis of ZrO.sub.2-coated mixed lithium transition metal oxides by SEM-EDX
[0089] Preparation of Electrodes
[0090] Electrodes for electrochemical measurements were prepared by blending 90 wt % NMC with 5 wt % of a polyvinylidene fluoride binder (PVDF 5130, manufacturer: Solef) and 5 wt % of a conductive carbon black (SUPER PLi, manufacturer: TIMCAL) under inert gas atmosphere. N-Methyl-2-pyrrolidone (NMP) was used as a solvent. The slurry was casted on aluminum foil and dried at 120° C. for 20 min on a heating plate under air. Afterwards, the electrode sheet was dried in a vacuum furnace at 120° C. for 2 h. Circular electrodes with a diameter of 12 mm were punched out of a larger piece and then flattened between 2 rollers with a pressure of 90 psi, and dried again in a vacuum furnace at 120° C. for 12 h to remove any residual water and NMP.
[0091] Assembly of Lithium Batteries
[0092] The lithium battery cells for the cycling tests were assembled as CR2032 type coin cells (MTI Corporation) in an argon-filled glovebox (GLOVEBOX SYSTEMTECHNIK GmbH). Lithium metal (R
[0093] Galvanostatic Cycling Tests
[0094] Galvanostatic cycle performance of the assembled lithium batteries was measured at 25° C. using a MACCOR battery cycler at cut-off voltage of 3.0-4.3 V. The C-rate (charge/discharge) was increased every four cycles, starting from 0.1 C/0.1 C (Charge/Discharge) to 0.3 C/0.3 C, 0.5 C/0.5 C, 1.0 C/1.0 C, 1.0 C/2.0 C and 1.0 C/4.0 C. Afterwards, the cell was cycled at 0.5 C/0.5 C for long term stability test. (0.5 C rate corresponds to current density of 0.7 mAh/cm.sup.2). For the calculation of the capacities and the specific currents, only the mass of the active material was considered. The results are presented in
[0095] In