Method for extracting lithium from brine
An extraction and brine technology, which is applied in the field of lithium extraction from brine, can solve the problems of extraction equipment corrosion, restriction of industrial application, and high concentration of tributyl phosphate, and achieve the effects of reducing corrosion, eliminating emulsification, and reducing application restrictions
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Embodiment 1
[0023] The method for extracting lithium from brine of the present embodiment comprises the following steps:
[0024] (1) Get 70ml tributyl phosphate and 30ml sulfonated kerosene to be configured into an organic solution, and the organic solution and the ferric chloride solution with an iron ion concentration of 70g / L are mixed and extracted according to O / A=1:1, and mixed The time is 3min to obtain the first organic phase containing ferric ions;
[0025] (2) Add 20ml of tributyl phosphate, 40ml of amide extractant (A101N,N'-dinormal acetamide in this example), and 40ml of sulfonated kerosene into the first organic phase to form tributyl phosphate 45% of ester, 20% of amide extractant, 35% of sulfonated kerosene, and the second organic phase of loaded iron 35g / L;
[0026] (3) the second organic phase is taken 50ml and pH is 0.5, Li content is 2.8g / L, Mg content is 115.2g / L, Cl content is the high magnesium lithium ratio salt lake brine of 205.9g / L by comparison O / A=2:1 for ...
Embodiment 2
[0028] The method for extracting lithium from brine of the present embodiment comprises the following steps:
[0029] (1) Get 70ml tributyl phosphate and 30ml sulfonated kerosene to be configured into an organic solution, and the organic solution and the ferric chloride solution with an iron ion concentration of 50g / L are mixed and extracted according to O / A=5:3, and mixed The time is 5min to obtain the first organic phase containing ferric ions;
[0030] (2) Add 20ml of tributyl phosphate, 40ml of amide extractant (N,N-bis(2-ethylhexyl)acetamide is used in this example), and 40ml of sulfonated kerosene to the first organic phase to form a compound containing The second organic phase of 45% tributyl phosphate, 20% amide extractant, 35% sulfonated kerosene, and 25g / L iron loading;
[0031] (3) the second organic phase is taken 50ml and pH is 3, Li content is 3.2g / L, Mg content is 118.9g / L, Cl content is the high magnesium lithium ratio salt lake brine of 213.3g / L by comparison...
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