Preparation method of lithium-rich manganese-based positive electrode material precursor
A positive electrode material, lithium-rich manganese-based technology, applied in chemical instruments and methods, battery electrodes, inorganic chemistry, etc., can solve the problems of precursor difficulties, cation mixing, and capacity retention rate reduction, so as to reduce Li/Ni mixing Discharge, reduce irreversible phase transition, reduce the effect of development cost
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[0027] A method for preparing a lithium-rich manganese-based cathode material precursor, the steps comprising:
[0028] (1) Nickel sulfate, manganese sulfate are x according to the molar ratio 1 :1-x 1 Mix and prepare a mixed salt solution A with a metal ion concentration of 2.5-4.5mol / L, where 0.10≤x 1 ≤0.20; the molar ratio of manganese sulfate, nickel sulfate and cobalt sulfate is x 2 :y 2 :z 2 Configure mixed salt solution B with a metal ion concentration of 2.5-4.5mol / L, where 0.10≤x 2 ≤0.20, 0.20≤y 2 ≤0.30, 0.50≤z 2 ≤0.70,x 2 +y 2 +z 2 = 1;
[0029] (2) Pass inert gas 1h-5h into the reaction kettle containing the bottom liquid earlier as protective gas to prevent the oxidation of Mn in the reaction process, when the pH of the bottom liquid is 9.0-10.5 and the ammonia concentration is 8-10g / L, Add mixed salt solution A, ammonia water with a concentration of 7-14g / L and 3mol / L alkaline solution into the reaction kettle and stir, control the pH of the reaction sy...
Embodiment 1
[0035] Step 1, nickel sulfate and manganese sulfate are configured as nickel-manganese metal mixed salt solution A of 15:85 by metal molar ratio, and manganese sulfate, nickel sulfate and cobalt sulfate are configured as 10:20:70 by molar ratio of nickel, cobalt and manganese to mix Salt solution B, the concentration of metal ions is 2.5mol / L, add 500L of pure water, 1kg of sodium carbonate and 40kg of ammonia as the bottom liquid in a 1 cubic reaction kettle, the pH is 9.5, and the ammonia concentration is 8g / L, 3 hours before the reaction, 1m 3 The inert protective gas of / h, then stably add nickel-manganese metal mixed salt solution A in the reactor with the flow rate of 30kg / h with metering pump, add the ammoniacal liquor that concentration is 12g / L and 3mol / L in reactor simultaneously Sodium carbonate solution, the flow rate is 5kg / h and 10kg / h respectively, by controlling the flow rate of ammonia water and sodium carbonate solution during the reaction, the pH of the adju...
Embodiment 2
[0040] Step 1, nickel sulfate and manganese sulfate are configured nickel-manganese mixed salt solution A of 20:80 by metal molar ratio, and manganese sulfate, nickel sulfate and cobalt sulfate are configured mixed salt solution B according to molar ratio of 20:20:60, The concentration of metal ions is 3.0mol / L. Add 300L of pure water, 3kg of sodium hydroxide and 50kg of ammonia water into a 1 cubic reaction kettle as the bottom liquid. The pH is 10.0 and the ammonia concentration is 9g / L. Medium access 5h 1m 3 / h of inert gas to prevent the oxidation of Mn in the reaction process, then use a metering pump to stably add nickel-manganese metal mixed salt solution A to the reactor at a flow rate of 40kg / h, and add a concentration of 14g / L to the reactor at the same time ammonia water and 3mol / L sodium hydroxide solution, the flow rates are 7kg / h and 15kg / h respectively, during the reaction process, the pH of the system is adjusted by controlling the flow rate of ammonia water an...
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