Preparation method of continuous nickel-cobalt-manganese ternary precursor
A precursor, nickel-cobalt-manganese technology, applied in chemical instruments and methods, nickel compounds, inorganic chemistry, etc., can solve the problems of over-burning of crystal nucleus, rising cost, material loss, etc. The effect of the manufacturer's cost
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[0023] A method for preparing a continuous nickel-cobalt-manganese ternary precursor, using metal salt solution, liquid caustic soda and ammonia solution as raw materials, using four liquid inlet pipes to continuously flow into the reactor for reaction, and injecting the solution by controlling Speed, PH value, reaction temperature, stirring speed and other parameters can effectively control the chemical impurities and crystal crystallinity, particle size, density, etc. of the lithium battery ternary precursor. Precursor lithium nickel cobalt manganese oxide.
[0024] It should be noted that the flow ratio of the upper and lower liquid inlet pipes in the invention is 1:0.1~10, here the flow ratio of the upper liquid inlet pipe and the lower liquid inlet pipe can be 1:0.1~10; The flow ratio between the liquid inlet pipe and the upper liquid inlet pipe is 1:0.1~10, which can achieve the effect of reducing the number of crystal nuclei and increasing the particle size of the cryst...
Embodiment 1
[0028] Embodiment 1: the preparation concentration is the metal salt solution of 120g / L, the liquid caustic soda with the concentration of 32g / L, and the ammonia solution with the concentration of 12g / L; Tube join size 5m 3 reaction in the reaction kettle; the liquid caustic soda flows into the reaction kettle in parallel by two liquid inlet pipes up and down, the flow of the upper liquid inlet pipe is 60L / h, and the flow of the lower liquid inlet pipe is 20L / h; control the pH in the reaction kettle 10. The temperature of the reactor is 40°C, and the average residence time of the materials in the reactor is 5 hours. Nitrogen is continuously fed into the reactor, and the stirring paddle is turned on to realize stirring. The two ends of the stirring paddle are divided into The upper stirring paddle at the upper end and the lower stirring paddle at the lower end, the stirring speed of the stirring paddle is controlled to be 50r / min, and the lower liquid inlet pipe of the liquid c...
Embodiment 2
[0030] Embodiment two: the preparation concentration is the metal salt solution of 120g / L, the liquid caustic soda of 32g / L, the ammoniacal solution of 25g / L; Tube join size 5m 3 Reaction in the reactor; The liquid caustic soda flows into the reactor in parallel by two liquid inlet pipes up and down, the flow of the upper liquid inlet pipe is 40L / h, and the flow of the lower liquid inlet pipe is 20L / h; the pH in the control reactor 11.5, the temperature of the reactor is 80°C, and the average residence time of the materials in the reactor is 20 hours. Nitrogen is continuously fed into the reactor, and the stirring paddle is turned on to realize stirring. The two ends of the stirring paddle are divided into The upper stirring paddle at the upper end and the lower stirring paddle at the lower end, the stirring speed of the stirring paddle is controlled to be 200r / min, and the lower liquid inlet pipe of the liquid caustic soda is arranged at the same horizontal position as the me...
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