High-purity lithium hexafluorophosphate continuous dynamic crystallization process device and method
A technology of lithium hexafluorophosphate and a process method, which is applied in the field of high-purity lithium hexafluorophosphate continuous dynamic crystallization process devices, can solve problems such as inability to meet production processes, and achieve the effects of reducing frequent manual operations, ensuring product quality, and improving cooling rate.
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Embodiment 1
[0037] This example is used to illustrate the lithium hexafluorophosphate crystal provided by the present invention and its production method.
[0038]The lithium hexafluorophosphate raw material liquid with a concentration of 19% and a temperature of 15 °C is pumped into the primary crystallization circulation pipeline by the raw material pump for cooling and cooling, and the temperature difference between the primary circulating feed liquid and the cooling medium is kept at 2 °C, and the circulation amount is 2 °C of the feeding amount. 50 times, maintain the temperature of the lithium hexafluorophosphate liquid in the first-stage crystallizer at -21 °C, keep the solid content of the crystal slurry in the first-stage crystallizer at 5%, circulate and cool in the crystallizer for 2 hours, and pump it into the second-stage through the first-stage discharge pump. The crystallization system is further cooled and cooled, the temperature difference between the secondary circulating...
Embodiment 2
[0040] The lithium hexafluorophosphate raw material liquid with a concentration of 15% and a temperature of 10 °C is pumped into the primary crystallization circulation pipeline by the raw material pump for cooling and cooling, and the temperature difference between the primary circulating feed liquid and the cooling medium is kept at 1 °C, and the circulation amount is 1 °C of the feeding amount. 80 times, maintain the temperature of the lithium hexafluorophosphate liquid in the first-stage crystallizer at -18 °C, and keep the solid content of the crystal slurry in the first-stage crystallizer at 8%. The crystallization system was further cooled to keep the temperature difference between the secondary circulating feed liquid and the cooling medium at 3 °C, the circulation amount was 60 times the feed amount, the temperature of the lithium hexafluorophosphate feed liquid in the secondary crystallizer was maintained at -42 °C, and the secondary crystallizer was kept at a temperat...
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