Method for extracting lithium from spodumene ore and by-product zeolite or kassinite
A technology of spodumene and potassium nepheline, which is applied in the field of hydrometallurgy, can solve the problems of high sealing and dust collection requirements of roasting equipment, environmental pollution, etc., and can meet the environmental protection requirements of clean production, short process flow and simple equipment Effect
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Embodiment 1
[0019] (1) 80g spodumene ore (containing Li 2.6%, particle size-100 mesh) is mixed with 60% sodium hydroxide solution, wherein, the weight ratio of sodium hydroxide and spodumene ore is 4.8:1, at a temperature of Reaction at 270°C for 2h.
[0020] (2) Dilute the pulp after the reaction in step (1) with water, the weight of water used for dilution is 3 times of the weight of spodumene, filter to obtain lithium-containing solution and zeolite product, and the extraction rate of lithium reaches 94.1%.
[0021] (3) the lithium-containing solution that step (2) obtains is added sodium carbonate by precipitation reaction, obtains lithium carbonate product.
Embodiment 2
[0023] (1) 80g spodumene ore (containing Li 0.6%, particle size-100 mesh) is mixed with 70% sodium hydroxide solution, wherein, the weight ratio of sodium hydroxide and spodumene ore is 8:1, at a temperature of React at 330°C for 0.5h.
[0024] (2) Dilute the pulp that has been reacted in step (1) with water, the weight of water used for dilution is 4 times of the weight of spodumene, and filter to obtain lithium-containing solution and zeolite product, wherein the extraction rate of lithium reaches 99.1%.
[0025] (3) The lithium-containing solution obtained in step (2) is added into sodium phosphate to undergo a precipitation reaction to obtain a lithium phosphate product.
Embodiment 3
[0027] (1) 80g spodumene ore (containing Li 1.8%, particle size-200 mesh) is mixed with 85% sodium hydroxide solution, wherein, the weight ratio of sodium hydroxide and spodumene ore is 2.8:1, at a temperature of Reaction at 270°C for 3h.
[0028] (2) Dilute the pulp that has been reacted in step (1) with water, the weight of water used for dilution is 8 times of the weight of spodumene, and filter to obtain lithium-containing solution and zeolite product, wherein the extraction rate of lithium reaches 92.2%.
[0029] (3) The lithium-containing solution obtained in step (2) is added into sodium phosphate to undergo a precipitation reaction to obtain a lithium phosphate product.
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