Technology for extracting lithium from lithium-containing alkaline brine based on mixer settlers
A technology for mixing and clarifying tanks to extract lithium, which is applied in the field of lithium extraction, can solve the problems of emulsification failure of the extractant, difficult maintenance, high cost, etc., and achieve the effect of avoiding the small difference in density between the two phases, high degree of automation, and high reliability
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Embodiment 1
[0078] The lithium-containing brine is pretreated to remove impurities such as solids, precipitates, and suspended solids.
[0079] to Li + The concentration is 2g / L, Na + The concentration is less than 80g / L, Ca 2+ The concentration is less than 0.1g / L, Mg 2+ Add 2 mol / L sodium hydroxide solution to the carbonate-type brine with concentration less than 0.1 g / L, adjust its pH value to 11, and obtain the extracted aqueous phase.
[0080] Mix HBTA, TOPO and kerosene to obtain an extracted organic phase; wherein, in the extracted organic phase, the concentration of HBTA and TOPO are both 0.3 mol / L.
[0081] Pump the extracted organic phase prepared above into the light phase inlet of the first mixing and settling tank assembly, and pump the extracted water phase into the corresponding heavy phase inlet, and control the extraction flow ratio to 3:2, so that the two are mixed in the first mixing and settling tank assembly. Three-stage countercurrent extraction is carried out in...
Embodiment 2
[0089] The lithium-containing brine is pretreated to remove impurities such as solids, precipitates, and suspended solids.
[0090] to Li + The concentration is 2g / L, Na + The concentration is less than 80g / L, Ca 2+ Concentration less than 0.05g / L, Mg 2+ Add 2 mol / L sodium carbonate solution to the carbonate or sulfate type brine with concentration less than 0.05g / L, adjust its pH value to 11, and obtain the extracted aqueous phase.
[0091] Mix HBTA, TOPO and kerosene to obtain an extracted organic phase; wherein, in the extracted organic phase, the concentration of HBTA and TOPO are both 0.3 mol / L.
[0092] Pump the extracted organic phase prepared above into the light phase inlet of the first mixing and settling tank assembly, and pump the extracted water phase into the corresponding heavy phase inlet, and control the extraction flow ratio to 1:1, so that the two are mixed in the first mixing and settling tank assembly. Three-stage countercurrent extraction is carried o...
Embodiment 3
[0100] The lithium-containing brine is pretreated to remove impurities such as solids, precipitates, and suspended solids.
[0101] to Li + The concentration is 0.5g / L, Na + The concentration is less than 80g / L, Ca 2+ Concentration less than 0.05g / L, Mg 2+ Add 2 mol / L sodium carbonate solution to the carbonate or sulfate type brine with concentration less than 0.05g / L, adjust its pH value to 12, and obtain the extraction water phase.
[0102] Mix HBTA, TOPO and kerosene to obtain an extracted organic phase; wherein, in the extracted organic phase, the concentration of HBTA and TOPO are both 0.3 mol / L.
[0103] Pump the extracted organic phase prepared above into the light phase inlet of the first mixing and settling tank assembly, and pump the extracted water phase into the corresponding heavy phase inlet, and control the extraction flow ratio to 2:3, so that the two are mixed in the first mixing and settling tank assembly. Three-stage countercurrent extraction is carried ...
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