Drying method for lithium iron phosphate precursor slurry
A technology of lithium iron phosphate and drying method, applied in chemical instruments and methods, phosphorus compounds, inorganic chemistry, etc., can solve the problems of high energy consumption, long drying time, expensive equipment, etc. Production cost, effect of shortening drying time
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Embodiment 1
[0022] The slurry ① mixed with the iron phosphate process water system has a solid content of 40%, and the D50 of the slurry particle size is 500 nanometers. After standing still for 36 hours, the slurry ① was separated. The water in the upper layer is discharged and recovered, and the solid content of the slurry 2 in the lower layer is increased to 70%. Turn on the stirring of the storage tank, and stir and disperse the slurry ② for 4 hours. The dispersed slurry ② is dried by crawler drying equipment, and the drying time is shortened from 10 hours for direct drying of slurry ① to 5 hours for slurry ②. And because of the continuity of production, the time required for standing is negligible. Greatly save drying time and reduce drying energy consumption, thereby improving production efficiency and reducing production costs.
Embodiment 2
[0024] The slurry ① mixed with the iron red process water system has a solid content of 30%, and the D50 of the slurry particle size is 2 microns. After adding a small amount of ethanol as a demulsifier and standing for 24 hours, the slurry ① separated. The supernatant of the upper layer is discharged and recovered, and the solid content of the slurry ② of the lower layer is increased to 80%. Turn on the stirring of the storage tank, and stir and disperse the slurry ② for 24 hours. The dispersed slurry ② is dried with double-cone equipment, and the drying time is shortened from 10 hours for direct drying of slurry ① to 4 hours for slurry ②. And because of the continuity of production, the time required for standing is negligible. Greatly save drying time and reduce drying energy consumption, thereby improving production efficiency and reducing production costs.
Embodiment 3
[0026] The slurry ① mixed with the ferrous oxalate process ethanol system has a solid content of 20%, and the D50 of the slurry particle size is 4 microns. After adding a small amount of water as a demulsifier and standing for 12 hours, the slurry ① separated. The supernatant of the upper layer is discharged and recovered, and the solid content of the slurry ② of the lower layer is increased to 80%. Turn on the stirring of the storage tank, and stir and disperse the slurry ② for 12 hours. The dispersed slurry ② is dried by rake drying equipment, and the drying time is shortened from 16 hours required for direct drying of slurry ① to 4 hours required for slurry ② drying. And because of the continuity of production, the time required for standing is negligible. Greatly save drying time and reduce drying energy consumption, thereby improving production efficiency and reducing production costs.
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