Comprehensive recovery method of waste electrolyte containing lithium and aluminum
A recovery method and electrolyte technology, applied in the direction of aluminum fluoride, aluminum halide, lithium carbonate; Low element leaching rate and other problems, to achieve efficient resource utilization, realize harmless, and solve the effect of low leaching rate
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Embodiment 1
[0037] The comprehensive recovery method of waste lithium-containing aluminum electrolyte of the present invention, the detailed steps of this recovery method are as follows:
[0038] a. Sequentially crush and finely grind 100 g of the discarded lithium-containing aluminum electrolyte (the content of lithium element is 1.9%) to obtain 100-200 mesh electrolyte powder;
[0039]b. Use hydrochloric acid and water to prepare an acid solution with a concentration of 1.0 mol / L, and add 200 g of a leaching enhancer aluminum chloride hexahydrate to the prepared acid solution; then add the electrolyte powder obtained in step a into 1000 mL of the prepared acid solution , heating and stirring leaching in a constant temperature water bath under normal pressure for 2 hours, during the heating and stirring leaching process, the temperature was controlled at room temperature 25°C, and filtered after leaching to obtain filter residue A and filtrate A;
[0040] c. Wash the obtained filter resi...
Embodiment 2
[0047] The comprehensive recovery method of waste lithium-containing aluminum electrolyte of the present invention, the detailed steps of this recovery method are as follows:
[0048] a. Sequentially crush and finely grind 500 g of the waste lithium-containing aluminum electrolyte (the lithium element content is 1.5%) to obtain 200-400 mesh electrolyte powder;
[0049] b. Use hydrochloric acid to add water to prepare an acid solution with a concentration of 1.0 mol / L, and add 100 g of a leaching enhancer aluminum chloride hexahydrate to the prepared acid solution; then add the electrolyte powder obtained in step a to 700 mL of the prepared acid solution , heating and stirring leaching in a constant temperature water bath under normal pressure for 2 hours, the temperature during the heating and stirring leaching process was controlled at 80°C, and filtering was carried out after leaching to obtain filter residue A and filtrate A;
[0050] c. Wash the obtained filter residue A, ...
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