Method for stripping lithium from loaded organic phase extracted from lithium-containing brine
An organic phase and brine technology, applied in the field of lithium stripping, can solve the problems of difficulty in obtaining high-purity lithium products, high cost, and difficult implementation, and achieve the effects of reducing process costs, avoiding equipment corrosion, and simplifying the recovery process.
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Embodiment 1
[0031] Using 40% TBP+20% P507 as extraction agent, kerosene as diluent, the concentration of loaded Li in the extraction system is 0.3g / L, and the concentration of Fe is 5.2g / L. Using water as the stripping agent, at the ratio of O / A=50:1, two-stage countercurrent stripping; adding the stripping agent in the second stage, the first stage Cl - The concentration is 2.1mol / L, the second grade Cl - The concentration is 1.8mol / L; the stripping rate of lithium is 99%, the concentration of lithium in the aqueous phase is 14.8g / L, and the stripping rate of iron is negligible. Lithium carbonate with a purity of 98% was obtained after sodium carbonate precipitation.
Embodiment 2
[0033] Using 40% TBP+20% P204 as extraction agent, kerosene as diluent, the concentration of loaded Li in the extraction system is 0.35g / L, and the concentration of Fe is 5.2g / L. Using water as the stripping agent, at the ratio of O / A=100:1, the five-stage countercurrent stripping; adding the stripping agent in the fifth stage, the first stage Cl - The concentration is 4.6mol / L, the second to fifth grade Cl - The concentration is 3.8-0.5mol / L; the stripping rate of lithium is 93%, the concentration of lithium in the aqueous phase is 32.6g / L, and the stripping rate of iron is negligible. Lithium carbonate with a purity of 98.5% was obtained after sodium carbonate precipitation.
Embodiment 3
[0035] Using 40% TBP+20% N503 as extraction agent, kerosene as diluent, the concentration of loaded Li in the extraction system is 0.28g / L, and the concentration of Fe is 4.7g / L. Using 1mol / L LiCl+0.4mol / L HCl as the stripping agent, at the ratio of O / A=20:1, three-stage countercurrent stripping; adding stripping agent in the third stage, the first stage Cl - The concentration is 1.9mol / L, the second to third grade Cl - The concentration is 1.8-1.2mol / L; the stripping rate of lithium is 85%, the concentration of lithium in the aqueous phase is 11.8g / L, and the stripping rate of iron is negligible. Lithium carbonate with a purity of 99% was obtained after sodium carbonate precipitation.
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