Preparation method for high-density spherical lithium iron phosphate material
A lithium iron phosphate, high-density technology, applied in the direction of electrical components, battery electrodes, circuits, etc., can solve the problems of insignificant improvement in material conductivity, low capacity, uneven element doping, etc., and achieve the goal of doping metal ions Uniform distribution, good conductivity and rate performance, reducing the effect of ion diffusion process
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Embodiment 1
[0019] Prepare a mixed aqueous solution with ferrous sulfate and phosphoric acid concentrations of 1.0mol / L, and add nickel sulfate therein, and the concentration of nickel sulfate in the mixed aqueous solution with nickel sulfate added is 0.03mol / L; the prepared concentration is 2mol / L NaOH solution; prepare a hydrogen peroxide solution with a concentration of 1mol / L. Under continuous stirring conditions, the above-mentioned raw material solutions are continuously added to the reactor respectively, and the flow rate of the mixed aqueous solution of phosphoric acid and ferrous sulfate is controlled to be 0.02L / min, and the flow ratio of the mixed aqueous solution of phosphoric acid and ferrous sulfate to hydrogen peroxide is V M :V H2O2 =3:1; adjust the flow of lye, control the pH value of the reaction system to 2.50±0.05, and the temperature of the reaction system to be 45°C. After the overflowed slurry is filtered, it is washed with pure water at 40°C until the pH of the wa...
Embodiment 2
[0022] Preparation of ferrous sulfate and phosphoric acid concentration is a mixed aqueous solution of 1.5mol / L, and magnesium sulfate is added therein, the concentration of magnesium sulfate in the mixed aqueous solution of adding magnesium sulfate is 0.02mol / L; the preparation concentration is 3mol / L NaOH solution; prepare a hydrogen peroxide solution with a concentration of 1.5mol / L. Under continuous stirring conditions, the above-mentioned raw material solutions are continuously added to the reactor respectively, and the flow rate of the mixed aqueous solution of phosphoric acid and ferrous sulfate is controlled to be 0.1L / min, and the flow ratio of the mixed aqueous solution of phosphoric acid and ferrous sulfate to hydrogen peroxide is V M :V H2O2 =3:1; adjust the flow rate of lye, control the pH value of the reaction system to 1.80±0.05, and the temperature of the reaction system to be 50°C. After the overflowed slurry is filtered, it is washed with pure water at 40°C ...
Embodiment 3
[0025] Preparation of ferrous chloride and phosphoric acid concentration is a mixed aqueous solution of 1.5mol / L, and aluminum chloride is added therein, and the concentration of aluminum chloride in the mixed aqueous solution of adding aluminum chloride is 0.02mol / L; The preparation concentration is 4mol / L NaOH solution; prepare a hydrogen peroxide solution with a concentration of 1.5mol / L. Under the condition of continuous stirring, the above-mentioned raw material solution is continuously added in the reactor respectively, and the flow velocity of the mixed aqueous solution of controlling phosphoric acid and ferrous chloride is 2L / min, and the flow ratio of the mixed aqueous solution of phosphoric acid and ferrous chloride to hydrogen peroxide is V M :V H2O2 =3:1; adjust the flow rate of lye, control the pH value of the reaction system to 2.00±0.05, and the temperature of the reaction system to be 60°C. After the overflowed slurry is filtered, it is washed with pure water ...
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