Process for preparing high density spherical nickel-cobalt lithium manganate as anode material of lithium ion cell
A technology for nickel cobalt lithium manganate and lithium ion batteries, which is applied in the field of energy material preparation, can solve the problems of low bulk density, low bulk density, and insufficient and uniform mixing of elements, and achieves high bulk density and improved performance.
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[0020] The invention provides a method for preparing high-density spherical nickel-cobalt lithium manganese oxide, which is composed of spherical or quasi-spherical particles, has high packing density and high specific capacity. The method is to first react nickel salt, cobalt salt, manganese salt with sodium hydroxide and ammonia in aqueous solution to synthesize spherical or quasi-spherical nickel hydroxide cobalt manganese Ni 1 / 3 co 1 / 3 mn 1 / 3 (OH) 2 The precursor is uniformly mixed with lithium carbonate after washing and drying, and subjected to high-temperature heat treatment at 750-950° C. for 8-48 hours in the air to obtain spherical nickel-cobalt lithium manganese oxide. The specific implementation method of the present invention comprises the following steps:
[0021] 1) Prepare a mixed aqueous solution of nickel salt, cobalt salt and manganese salt with a total metal ion concentration of 0.6-3 mol / liter, wherein Ni:Co:Mn=1:1:1 (molar ratio).
[0022] 2) Prepare ...
Embodiment 1
[0032] The concentration of nickel nitrate is 1 mol / liter, the concentration of cobalt nitrate is 1 mol / liter, and the mixed aqueous solution of nickel-cobalt-manganese salt is 1 mol / liter of manganese nitrate, and the concentration of sodium hydroxide is 10 mol / liter. 10 mol / L ammonia solution. The nickel-cobalt-manganese salt mixed aqueous solution, the sodium hydroxide aqueous solution, and the ammonia aqueous solution were respectively input into a reactor with a capacity of 3 liters filled with deionized water with a metering pump for reaction. Control the flow of nickel-cobalt-manganese salt mixed aqueous solution to be 120 ml / hour, control the flow of ammonia solution, make the NH in the reactor 3 / (Ni+Co+Mn)=0.5. Regulate the flow rate of the aqueous sodium hydroxide solution to control the pH value of the reaction solution in the reactor to 11.5. The temperature inside the reactor was controlled to be 45°C. The mixed material in the reactor naturally overflows into...
Embodiment 2
[0034] The concentration of nickel sulfate is 0.6 mol / liter, the concentration of cobalt sulfate is 0.6 mol / liter, and the mixed aqueous solution of nickel cobalt manganese salt is 0.6 mol / liter in manganese sulfate concentration, and the sodium hydroxide aqueous solution with concentration of 3.6 mol / liter is prepared. 5 mol / L ammonia solution. The nickel-cobalt-manganese salt mixed aqueous solution, the sodium hydroxide aqueous solution, and the ammonia aqueous solution were respectively input into a reactor with a capacity of 3 liters filled with deionized water with a metering pump for reaction. Control the flow of nickel-cobalt-manganese salt mixed aqueous solution to be 120 ml / hour, control the flow of ammonia solution, make the NH in the reactor 3 / (Ni+Co+Mn)=0.8. Regulate the flow rate of the aqueous sodium hydroxide solution to control the pH value of the reaction solution in the reactor to 11.0. The temperature inside the reactor was controlled to be 45°C. The mix...
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