A method for harmless and resourceful treatment of waste aluminum electrolyte
A technology of aluminum electrolyte and treatment method, which is applied in the direction of aluminum fluoride, aluminum halide, alkali metal chloride, etc., can solve the problem of resource utilization of waste aluminum electrolyte that cannot be processed with fluoride salt, and achieves cheap price, single process, and reduced cost effect
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Embodiment 1
[0026] Take 50g of waste aluminum electrolyte (molecular ratio 2.5) from a factory, crush and sieve to obtain aluminum electrolyte particles with a particle size of less than 100 mesh, take 200ml of 1mol / L sulfuric acid solution, heat it in a beaker and use electromagnetic stirring, use a pH meter and fluoride ion selective electrode to monitor the change of acidity and fluoride ion concentration during the neutralization process. The leaching temperature is 80°C, the stirring speed is 300r / min, the pH value is 2.5, and the leaching time is 3 hours. Add 1mol / L aluminum sulfate solution for fluorine precipitation, the temperature is 70°C, the pH value is reduced to 1, and the fluoride ion concentration of the solution is controlled. When the fluoride ion concentration is lower than 0.01g / L, the solution is filtered, and the filter residue is washed. Dry to obtain the basic aluminum fluoride product. The filtrate is adjusted and sent to the leaching process for recycling.
Embodiment 2
[0028] Take 5000g of waste aluminum electrolyte (molecular ratio 2.3) from a factory, crush and sieve to obtain aluminum electrolyte particles with a particle size below 50 mesh, take 15L of 1mol / L sulfuric acid solution, put it into a reaction vessel, heat and stir, and use a pH meter and A fluoride ion selective electrode monitors changes in acidity and fluoride ion concentration during the neutralization process. The leaching temperature is 50°C, the stirring speed is 300r / min, the pH value is 4, and the leaching time is 4 hours. Add 1mol / L aluminum sulfate solution for fluorine precipitation, the temperature is 90°C, the pH value is reduced to 0.5, and the fluoride ion concentration of the solution is controlled. When the fluoride ion concentration is lower than 0.01g / L, the solution is filtered, and the filter residue is washed. Dry to obtain the basic aluminum fluoride product. The filtrate is adjusted and sent to the leaching process for recycling.
Embodiment 3
[0030] Take 50kg of waste aluminum electrolyte (molecular ratio 2.6) from a factory, crush and sieve to obtain aluminum electrolyte particles with a particle size below 50 mesh, take 400L 1mol / L sulfuric acid solution, heat and stir in a reaction vessel, use a pH meter and A fluoride ion selective electrode monitors changes in acidity and fluoride ion concentration during the neutralization process. The leaching temperature is 30°C, the stirring speed is 300r / min, the pH value is 4.5, and the leaching time is 5 hours. Add 1mol / L aluminum sulfate solution for fluoride precipitation, the temperature is 85°C, the pH value is reduced to 1, and the fluoride ion concentration of the solution is controlled. When the fluoride ion concentration is lower than 0.01g / L, the solution is filtered, and the filter residue is washed. Dry to obtain the basic aluminum fluoride product. The filtrate is adjusted and sent to the leaching process for recycling.
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