Two-stage fluorine removal method for fluorine-containing material
A technology for materials and fluorine removal agents, which is applied in the fields of hydrometallurgy and resource recovery, can solve the problems of not being suitable for handling solutions with high fluorine content, long time for fluorine removal, and no method for efficient fluorine removal has been reported. The effect of high fluorine efficiency, avoiding large dosage and easy operation
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Embodiment 1
[0031]The fluorine-containing solid powder used in this embodiment is waste battery powder, and its main components are shown in Table 1:
[0032]Table 1 Main element content of raw materials (%)
[0033] element Co Ni Mn F content 16.0937.4116.581.40
[0034]1. Mix water and raw materials into a slurry according to the liquid-to-solid ratio of 3:1~10:1, and react for 0.5~3.5h under the conditions of 60~90℃ and stirring speed of 250rpm~400rpm. Add 10~18.4mol / during the reaction. L sulfuric acid adjusts the pH to control the end point pH of the reaction to be 0.5-2.5. After the reaction is over, the leachate and filter residue are obtained by vacuum suction filtration, and then the content of related elements in the leachate is measured. The content of the main elements is shown in Table 2:
[0035]Table 2 Main element content of leaching solution (g / L)
[0036] element Co Ni Mn F content 15.4631.8124.201.50
[0037]2. Take a certain volume of the leaching solution, add a calcium carbonate solu...
Embodiment 2
[0047]The fluorine-containing solid powder used in this embodiment is waste battery powder, and its main components are shown in Table 5:
[0048]Table 5 Main element content of raw materials (%)
[0049] element Co Ni Mn F content 16.0937.4116.581.40
[0050]1. Mix water and raw materials into a slurry according to the liquid-to-solid ratio of 3:1~10:1, and react for 0.5~3.5h under the conditions of 60~90℃ and stirring speed of 250rpm~400rpm. Add 10~18.4mol / during the reaction. L sulfuric acid adjusts the pH to control the end point pH of the reaction to be 0.5-2.5. After the reaction is over, the leachate and filter residue are obtained by vacuum filtration, and then the content of related elements in the leachate is measured. The content of the main elements is shown in Table 6:
[0051]Table 6 Main element content of leaching solution (g / L)
[0052] element Co Ni Mn F content 15.4631.8124.201.50
[0053]2. Take a certain volume of leaching solution, add 10%-30% calcium hydroxide solution a...
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