Method for selectively leaching nitric acid from lithium element in aluminum electrolyte
An aluminum electrolyte and selective technology, which is applied in the purification of aluminate/alumina/aluminum hydroxide and the improvement of process efficiency, etc., can solve the difficulty of separating lithium salt from other components, increase acid consumption, and increase production costs To achieve the effect of expanding the supply of lithium salt resources, reducing production costs, and improving the overall level
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Embodiment 1
[0046] Take 10g of aluminum electrolyte (the content of LiF in the electrolyte is 5%), and obtain aluminum electrolyte powder by crushing, grinding, and sieving through an 80-120 mesh sieve, and prepare 100ml of acid solution with nitric acid and distilled water, and the pH of the acid solution is 3. The potential is 0.05V, put the aluminum electrolyte powder into the above acid solution, heat to 60°C, stir with a magnetic stirrer, control the solution potential, pH value and fluoride ion concentration, when the solution pH value is 4, When the fluoride ion concentration is 2g / L, the leaching ends. The reacted mixed solution is filtered and washed to obtain the reacted primary filtrate and primary filtrate.
[0047] After analysis and detection, the dissolution rate of LiF converted from lithium salt in the electrolyte is 99%, and the dissolution rate of the electrolyte is 8%.
Embodiment 2
[0049] Take 500g of aluminum electrolyte (the content of LiF in the electrolyte is 7%), after crushing, grinding, and sieving through an 80-120 mesh sieve, aluminum electrolyte powder is obtained, and 1L of acid solution is prepared with nitric acid and distilled water, and the pH of the acid solution is 2. The potential is 0.1V. Put the aluminum electrolyte powder into the above acid solution, heat to 70°C, stir with a magnetic stirrer, and control the solution potential, pH value and fluoride ion concentration. When the solution pH value is 1, When the fluoride ion concentration is 50g / L, the leaching ends. The reacted mixed solution is filtered and washed to obtain the reacted primary filtrate and primary filtrate.
[0050] After analysis and detection, the dissolution rate of LiF converted to lithium salt in the electrolyte is 90%, and the dissolution rate of the electrolyte is 10%.
Embodiment 3
[0052] Take 10kg of aluminum electrolyte (the content of LiF in the electrolyte is 4%), obtain aluminum electrolyte powder by crushing, grinding, and sieving through an 80-120 mesh sieve, and prepare 100L acid solution with nitric acid and distilled water. The pH of the acid solution is 2. The potential is 0.015V. Put the aluminum electrolyte powder into the above acid solution, heat to 85°C, stir with a magnetic stirrer, and control the solution potential, pH value and fluoride ion concentration. When the solution pH value is 4, When the fluoride ion concentration is 30g / L, the leaching ends. The reacted mixed solution is filtered and washed to obtain the reacted primary filtrate and primary filtrate.
[0053] After analysis and detection, the dissolution rate of LiF converted to lithium salt in the electrolyte is 80%, and the dissolution rate of the electrolyte is 6%.
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