Method for extracting lithium from salt lake brine
A salt lake brine and brine technology, applied in chemical instruments and methods, lithium compounds, alkali metal compounds, etc., can solve the problems of unfavorable actual production, low safety, low adsorption capacity, etc., and achieve easy industrialization promotion and wide source of raw materials. , the effect of simple process
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Embodiment 1
[0020] Brine composition (g / L): Li + 0.32, Na + 52.15,K + 8.58, Cl - 68.41, SO 4 2- 6.95, CO 3 2- 11.07, B 4 o 7 2- 2.77.
[0021] Calcined kaolin at 700 °C for 1 h, weighed 10.0 g of calcined kaolin and added it to 20% hydrochloric acid to control Al 2 o 3 The molar ratio with HCl is 1:7, and the temperature is 90 ℃ in a water bath for 2.5 hours. After solid-liquid separation, the aluminum content in the obtained filtrate is 0.97mol / L;
[0022] Add the aluminum-containing filtrate and 2 mol / L NaOH solution to 200 ml of brine, control the molar ratio of aluminum in the filtrate to lithium in the brine to be 3.5, and the molar ratio of sodium in the NaOH solution to aluminum in the filtrate to be 2.7. After reacting at 55 °C for 1 h, solid-liquid separation was performed again to obtain a lithium-containing precipitate, and the lithium precipitation rate was 52.42%.
Embodiment 2
[0024] Brine composition (g / L): Li + 0.66, Mg 2+ 20.76, K + 0.95, Cl - 49.95, SO 4 2- 5.12, B 4 o 7 2- 1.57.
[0025] Kaolin was calcined at 700 °C for 1 h, and 10.0 g of calcined kaolin was weighed and added to 20% hydrochloric acid to control Al 2 o 3 The molar ratio with HCl is 1:6, and the temperature is 95 ℃ in a water bath for 2.5 h. After solid-liquid separation, the aluminum content in the obtained filtrate is 0.97mol / L;
[0026] Add the aluminum-containing filtrate and 2 mol / L NaOH solution to 200 ml brine, control the molar ratio of aluminum in the filtrate to lithium in the brine to be 3.5, and the molar ratio of sodium in the NaOH solution to aluminum in the filtrate is 2.8, and the temperature is After reacting at 65 °C for 1 h, solid-liquid separation was performed again to obtain a lithium-containing precipitate, and the lithium precipitation rate was 85.36%.
Embodiment 3
[0028] Brine composition (g / L): Li + 0.94, Mg 2+ 21.72, Ca 2+ 44.62,K + ,2.87, Cl - 155.15, B 4 o 7 2- 6.29.
[0029] Calcined kaolin at 750 °C for 2 h, weighed 10.0 g of calcined kaolin and added it to 20% hydrochloric acid to control Al 2 o 3 The molar ratio with HCl is 1:6, and the temperature is 95 ℃ in a water bath for 2.5 hours. After solid-liquid separation, the aluminum content in the obtained filtrate is 0.94mol / L;
[0030] Add the aluminum-containing filtrate and 2 mol / L NaOH solution to 200 ml brine, control the molar ratio of aluminum in the filtrate to lithium in the brine to be 3.0, and the molar ratio of sodium in the NaOH solution to aluminum in the filtrate is 2.9. After reacting at 55 °C for 1 h, solid-liquid separation was performed again to obtain a lithium-containing precipitate, and the lithium precipitation rate was 89.6%.
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