Method for joint extraction of potassium, boron and lithium from chloride-type potassium-containing underground brine
A combined extraction technology of underground brine, which is applied in lithium carbonate, chloride-type underground brine rich in potassium, boron, and lithium to extract potassium chloride and boric acid, can solve the problems of difficult industrial production, poor product quality, and inability to obtain potassium and boron. Separation and other issues, to achieve the effect of high resource utilization and simple process
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Embodiment 1
[0022] A chloride type underground brine, its composition is K 0.73%, Na 9.16%, Cl 16.82%, Ca 0.35%, B 2 o 3 0.20%, Li 0.005%. The brine is evaporated at 100°C, and the volume is concentrated by 3 times; the concentrated brine is ion-exchanged to extract boron, using D564 as the ion-exchange resin, the boron adsorption rate is 98.79%, when the resin reaches the working exchange capacity, stop adsorption and switch to desorption , the resin was rinsed with dilute sulfuric acid to obtain a boron-containing eluent, and the boron desorption rate was 99.5%. The eluent was concentrated by evaporation and cooled to crystallize to produce boric acid. Under the condition of stirring, add 380 g / L sodium sulfate solution to react, the amount of sodium sulfate is 110% of the theoretical amount, and the calcium salt based on calcium sulfate is precipitated; the mother liquor after calcium precipitation is evaporated for one stage, and the liquid density is controlled to be 1.32g / cm 3 ...
Embodiment 2
[0024] A chloride type underground brine, its composition is K 0.73%, Na 9.16%, Cl 16.82%, Ca 0.35%, B 2 o 3 0.20%, Li 0.005%. The brine is evaporated at 105°C, and the volume is concentrated by 4 times; the concentrated brine is ion-exchanged to extract boron, and D403 is used as the ion-exchange resin, and the boron adsorption rate is 85.40%. When the resin reaches the working exchange capacity, the adsorption is stopped and desorption , the resin was rinsed with dilute sulfuric acid to obtain a boron-containing eluate, and the boron desorption rate was 98.70%. The eluate was concentrated by evaporation and cooled to crystallize to produce boric acid. Under the condition of stirring, add 380 g / L sodium sulfate solution to react, the amount of sodium sulfate is 120% of the theoretical amount, and the calcium salt based on calcium sulfate is precipitated; the mother liquor after calcium precipitation is evaporated for one stage, and the liquid density is controlled to be 1.3...
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