Hollow positive electrode material, precursor thereof, and preparation method of precursor
A cathode material and precursor technology, which is applied in the field of hollow cathode material precursor and its preparation, can solve the problem of difficulty in large-scale and efficient production of hollow material precursor, and the inability to meet the high output power and high cycle of power batteries. The requirements of characteristics, etc., to achieve the effect of high tap density, low cost and simple process
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Embodiment 1
[0043] Prepare a ternary metal salt solution of nickel sulfate, cobalt sulfate, and manganese sulfate with a total metal concentration of 2mol / L. The molar ratio of nickel, cobalt, and manganese is 60:20:20, and prepare a 2mol / L sodium hydroxide solution. Add pure water to the reaction kettle with a volume of 100L, control the temperature at 55°C, add ammonia water to adjust the concentration of ammonia water in the reaction kettle to 7g / L, add lye to adjust the pH to 11.80, and add 1.3L / The flow rate of min is continuously fed into the air.
[0044] In the reaction process of stage I, inject the ternary metal salt solution with the flow rate of 3.6L / h in the reactor, control reaction temperature to be 55 ℃, regulate the flow of the ammoniacal liquor and the sodium hydroxide solution injected in the reactor, make the reactor The pH inside was maintained at 11.80, the concentration of ammonia water was maintained at 7g / L, the pH was adjusted to 11.40 after 1 hour of reaction, ...
Embodiment 2
[0048] Prepare a ternary metal salt solution of nickel sulfate, cobalt sulfate, and manganese sulfate with a total metal concentration of 2mol / L. The molar ratio of nickel, cobalt, and manganese is 60:20:20, and prepare a 2mol / L sodium hydroxide solution. Add pure water to the reactor with a volume of 100L, control the temperature at 55°C, add ammonia to adjust the ammonia concentration in the reactor to 7g / L, add lye to adjust the pH to 12.0, and add 0.75L / The flow rate of min is continuously fed into the air.
[0049] In the reaction process of stage I, inject ternary metal salt solution with the flow rate of 2.4L / h in the reactor, control reaction temperature to be 55 ℃, regulate the flow of the ammoniacal liquor and the sodium hydroxide solution injected in the reactor, make the reactor The pH inside was maintained at 12.0, the concentration of ammonia water was maintained at 7g / L, the pH was adjusted to 11.40 after 0.5h of reaction, the air flow rate was reduced to 0.1L / ...
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