Technology for extracting lithium from lithium-containing alkaline brine based on centrifugal extractor
An extractor and water extraction technology, which is applied in the field of lithium extraction, can solve the problems of emulsification failure of the extractant, large equipment investment, and increased density of the extracted organic phase, so as to avoid the small difference in density between the two phases, high degree of automation, and water-soluble small effect
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Embodiment 1
[0074] The lithium-containing brine is pretreated to remove impurities such as solids, precipitates, and suspended solids.
[0075] to Li + A 2 mol / L sodium hydroxide solution was added to the carbonate brine with a concentration of 2 g / L to adjust its pH value to 11 to obtain an extracted aqueous phase.
[0076] 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.
[0077] The extracted organic phase prepared above is pumped into the light phase inlet of the first centrifugal extractor assembly, and the extracted aqueous phase is pumped into the corresponding heavy phase inlet, and the extraction flow ratio is controlled to be 3:2, so that the two are separated in the first centrifugal extractor assembly. Three-stage countercurrent extraction is carried out inside the extractor assembly, and the phases are separated to obtain the raffinate and the loaded organic phase...
Embodiment 2
[0084] The lithium-containing brine is pretreated to remove impurities such as solids, precipitates, and suspended solids.
[0085] to Li + Add 2 mol / L sodium bicarbonate solution to the carbonate or sulfate type brine with a concentration of 2 g / L to adjust the pH value to 11 to obtain the extracted aqueous phase.
[0086] HFTA, TRPO and kerosene were mixed to obtain an extracted organic phase; wherein, in the extracted organic phase, the concentration of HFTA and TRPO were both 0.4 mol / L.
[0087] The extracted organic phase prepared above is pumped into the light phase inlet of the first centrifugal extractor assembly, and the extracted aqueous phase is pumped into the corresponding heavy phase inlet, and the extraction flow ratio is controlled to be 1:2, so that the two are separated in the first centrifugal extractor assembly. Six-stage countercurrent extraction is carried out inside the extractor assembly, and the phases are separated to obtain the raffinate and the loa...
Embodiment 3
[0094] The lithium-containing brine is pretreated to remove impurities such as solids, precipitates, and suspended solids.
[0095] to Li + Add 2 mol / L sodium bicarbonate solution to 0.5 g / L carbonate or chloride type brine to adjust its pH value to 10.5 to obtain the extracted aqueous phase.
[0096] HFTA, TRPO and kerosene are mixed to obtain an extracted organic phase; wherein, in the extracted organic phase, the concentration of HFTA and TRPO are both 0.2 mol / L.
[0097]The extracted organic phase prepared above is pumped into the light phase inlet of the first centrifugal extractor assembly, and the extracted aqueous phase is pumped into the corresponding heavy phase inlet, and the extraction flow ratio is controlled to be 1:3, so that the two are separated in the first centrifugal extractor assembly. Four-stage countercurrent extraction is carried out inside the extractor assembly, and the phases are separated to obtain the raffinate and the loaded organic phase.
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