Preparation method of high-density lithium iron phosphate cathode material
A technology of lithium iron phosphate and positive electrode materials, which is applied in the field of preparation of high-density lithium iron phosphate positive electrode materials, can solve the problems of insufficient drying of precursors, poor performance of lithium iron phosphate, and low solid content of slurry, and achieve excellent electrochemical performance. performance, promotion of uniform distribution, effect of low liquid content
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[0029] The present invention provides a method for preparing a high-density lithium iron phosphate cathode material. The method includes the following steps:
[0030] A. Mechanical activation: Add a certain amount of deionized water to the ball mill, and then add the lithium source, composite iron source, phosphorus source, carbon source and surfactant in proportion, where the molar ratio of Li:Fe:P is (1 ~1.2): (0.96~1.2): 1. The weight of the carbon source is 8-12% by weight of the theoretical production of lithium iron phosphate, and the weight of the surfactant is 8-20% by weight of the added amount of the lithium source; the composite iron source is It is obtained by mixing reducing iron powder with D50 of 1-2μm and iron orthophosphate with primary particles of 50-200nm in a molar ratio of 1:10 to 1:1 (preferably 1:5 to 1:1), high-speed ball milling 4~ 8 hours later, a mixed slurry is formed, and the solid content of the slurry is 52-68%;
[0031] B. Solid-liquid separation: ...
Embodiment 1
[0037] The primary particles are 50nm iron orthophosphate (FePO 4 ) 300.00 kg and 11.14 kg of metallic iron powder with a particle size D50 of 2um are mixed to obtain a composite iron source. 400 kg of deionized water is added to the ball mill, and then 73.52 kg of lithium carbonate, composite iron source, 20.68 kg of lithium dihydrogen phosphate, hard Fatty acid 41.47 kg, surfactant cetyl trimethyl ammonium bromide 18.84 kg were placed in a ball mill and ball milled to form a slurry. The milling time was 4 hours, and the slurry particle size was controlled at 1.5 microns to obtain a solid content of 65 % Homogeneously mixed slurry. Then the ball mill slurry is pumped into the diaphragm filter press with a diaphragm pump for pressure filtration, and the pressure filtration time is 1.5 hours to obtain a precursor with a moisture content of less than 15%; then the precursor is transported into the flash dryer for pressure filtration. Dry and mix, dry the inlet air temperature is ...
Embodiment 2
[0041] The primary particles are 100nm iron orthophosphate (FePO 4 ) 150.00 kg and 11.14 kg of metal iron powder with a particle size D50 of 1um are mixed to obtain a composite iron source. Add 250 kg of deionized water to the ball mill, and then add 44.33 kg of lithium carbonate, composite iron source, and 15.78 kg of stearic acid. 6.65 kilograms of alkyltrimethylammonium bromide were placed in a ball mill and ball milled to prepare a slurry. The milling time was 6 hours, and the slurry particle size was controlled at 1.0 micron to obtain a homogeneous mixed slurry with a solid content of 60%. Then the ball mill slurry was pumped into a diaphragm filter press with a diaphragm pump for pressure filtration. The pressure filtration time was 2.0 hours to obtain a precursor with a liquid content of 12%; then the precursor was transported into the flash dryer for pressure filtration. Dry and mix, dry the inlet air temperature is 150°C, the outlet air temperature is 70°C, after drying...
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