Method for extracting lithium from salt lake brine
A salt lake brine and extraction technology, applied in the chemical industry and extraction chemistry field, can solve the problems of solvent loss of extraction agent, strong corrosion of extraction equipment, and restrictions on large-scale industrial application, etc., to reduce concentration, improve strong corrosion, and simple operation reliable effect
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Embodiment 1
[0017] The method for extracting lithium in this salt lake brine provided by the present embodiment includes:
[0018] 1) Prepare the organic phase for extraction: take 300mL of tributyl phosphate and 700mL of N,N-bis(2-ethylhexyl)-3-butanoneacetamide to form a composite extractant, take 1000mL of sulfonated kerosene as a diluent and add to the compound in the extractant;
[0019] 2) Extract the water phase: take the salt lake brine of saturated magnesium chloride solution, which is LiCl-MgCl 2 -H 2 O system;
[0020] 3) Add HCl, FeCl to the extracted aqueous phase 3 ·6H 2 O, wherein, the ratio of the amount of substances controlling iron and lithium is 1.3:1, at this moment, the lithium concentration is 1.9604g / L, and the acid concentration is 0.05mol / L;
[0021] 4) Mix the extracted aqueous phase obtained in step 3) with the extracted organic phase obtained in step 1) at a volume ratio of 1:2, fully mix and shake for 6 minutes, then stand still and separate the liquid p...
Embodiment 2
[0023] The method for extracting lithium in this salt lake brine provided by the present embodiment includes:
[0024] 1) Prepare the organic phase for extraction: take 400mL of tributyl phosphate and 600mL of N,N-bis(2-ethylhexyl)-3-butanoneacetamide and mix them into a composite extractant, take 1000mL of sulfonated kerosene as diluent and add to the compound in the extractant;
[0025] 2) Extract the water phase: take the salt lake brine of saturated magnesium chloride solution, which is LiCl-MgCl 2 -H 2 O system;
[0026] 3) Add HCl, FeCl to the extracted aqueous phase 3 ·6H 2 O, wherein, the ratio of the amount of substances controlling iron and lithium is 1.3:1, at this moment, the lithium concentration is 1.9604g / L, and the acid concentration is 0.05mol / L;
[0027] 4) Mix the extracted aqueous phase obtained in step 3) with the extracted organic phase obtained in step 1) at a volume ratio of 1:2, fully mix and shake for 6 minutes, then stand still and separate the ...
Embodiment 3
[0029] The method for extracting lithium in this salt lake brine provided by the present embodiment includes:
[0030] 1) Prepare the organic phase for extraction: take 500mL of tributyl phosphate and 500mL of N,N-bis(2-ethylhexyl)-3-butanoneacetamide and mix them into a composite extractant, take 1000mL of sulfonated kerosene as a diluent and add to the compound in the extractant;
[0031] 2) Extract the water phase: take the salt lake brine of saturated magnesium chloride solution, which is LiCl-MgCl 2 -H 2 O system;
[0032] 3) Add HCl, FeCl to the extracted aqueous phase 3 ·6H 2 O, wherein, the ratio of the amount of substances controlling iron and lithium is 1.3:1, at this moment, the lithium concentration is 1.9604g / L, and the acid concentration is 0.05mol / L;
[0033] 4) Mix the extracted aqueous phase obtained in step 3) with the extracted organic phase obtained in step 1) at a volume ratio of 1:2, fully mix and shake for 6 minutes, then stand still and separate th...
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