Method for preparing high-density spherical ferric lithium phosphate as anode material of lithium-ion battery
A technology for lithium ion batteries and cathode materials, applied in the field of energy materials, can solve the problems of low packing density of lithium iron phosphate, hindering the practical application of materials, etc.
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Embodiment 1
[0039] Prepare a ferric nitrate aqueous solution with a concentration of 2 mol / liter, a phosphoric acid aqueous solution with a concentration of 2 mol / liter, and an ammonia solution with a concentration of 6 mol / liter. Use the metering pump to input ferric nitrate aqueous solution, phosphoric acid aqueous solution and ammonia solution into a reactor with a volume of 3 liters filled with deionized water in advance to react, control the flow rate of ferric nitrate aqueous solution and phosphoric acid aqueous solution to be 120 ml / hour, adjust The flow rate of the ammonia solution is to control the pH value of the reaction solution in the reactor to be 4.0±0.1. The temperature in the reactor was controlled to be 50°C. The mixed material in the reactor naturally overflows into the receiving tank. After feeding continuously for 20 hours, stop feeding, discharge the material in the reactor, and carry out solid-liquid separation with a centrifuge. Wash the solid product with deioni...
Embodiment 2
[0041] Prepare an aqueous solution of ferric chloride with a concentration of 1 mol / liter, an aqueous solution of ammonium dihydrogen phosphate with a concentration of 1 mol / liter, and an aqueous solution of sodium hydroxide with a concentration of 3 mol / liter. Use a metering pump to respectively input ferric trichloride aqueous solution, ammonium dihydrogen phosphate aqueous solution, and sodium hydroxide aqueous solution into a reactor with a capacity of 3 liters filled with deionized water in advance for reaction, and control the ferric trichloride aqueous solution and diphosphate diphosphate The flow rate of the ammonium hydrogen aqueous solution is 120 milliliters / hour, regulates the flow rate of the sodium hydroxide aqueous solution, and the pH value of the reaction solution in the control reactor is 4.0 ± 0.1. The temperature in the reactor was controlled to be 50°C. The mixed material in the reactor naturally overflows into the receiving tank. After feeding continuous...
Embodiment 3
[0043] Prepare an aqueous ferric sulfate solution with a concentration of 0.5 mol / liter, an aqueous solution of trisodium phosphate with a concentration of 1 mol / liter, and an aqueous ammonia solution with a concentration of 6 mol / liter. Use a metering pump to respectively input ferric sulfate aqueous solution, trisodium phosphate aqueous solution, and ammonia aqueous solution into a reactor with a volume of 3 liters filled with deionized water for reaction, and control the flow rate of ferric sulfate aqueous solution and trisodium phosphate aqueous solution to 120 ml / hour, adjust the flow rate of the ammonia solution, and control the pH value of the reaction solution in the reactor to 4.0±0.1. The temperature in the reactor was controlled to be 50°C. The mixed material in the reactor naturally overflows into the receiving tank. After feeding continuously for 20 hours, stop feeding, discharge the material in the reactor, and carry out solid-liquid separation with a centrifu...
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