A method for enriching scandium and titanium from aluminum-melting slag and recovering silicon-aluminum sodium
A technology for dissolving and enriching aluminum, which is applied in the field of enriching scandium and titanium from aluminum-dissolving slag and recovering silicon-aluminum sodium, can solve the problems of low titanium recovery rate, etc. Effect
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Embodiment 1
[0033] ① Dry and finely grind the aluminum-dissolving slag until it is passed through a sample sieve to obtain a solid powder with a particle size of less than 74 μm. Use dilute sulfuric acid to selectively leach the aluminum-dissolving slag. The leaching conditions are: the mass fraction of the dilute sulfuric acid solution is 12%, and the reaction temperature is The temperature is 25°C, the reaction time is 60min, the liquid-solid ratio is 8:1mL / g, and the stirring speed is 400r / min;
[0034] ② Separating the slurry obtained in step ① into solid and liquid to obtain leaching residue and leaching solution; the leaching rate of silicon in the leaching solution was 92%, the leaching rate of aluminum was 78.22%, and the leaching rate of sodium was 97.33%;
[0035] ③Wash the leached slag obtained in step ② with distilled water, and dry at 120°C to obtain scandium-rich titanium slag; TiO in scandium-rich titanium slag 2 The content of Sc is 44.08%, and the content of Sc is 0.020%....
Embodiment 2
[0041]①Dry and finely grind the aluminum-dissolving slag until it is passed through a sample sieve to obtain a solid powder with a particle size of less than 74 μm, and use dilute sulfuric acid to selectively leach the aluminum-dissolving slag. The leaching conditions are: the mass fraction of the dilute sulfuric acid solution is 8%, and the reaction temperature The temperature is 95°C, the reaction time is 60min, the liquid-solid ratio is 7:1mL / g, and the stirring speed is 500r / min;
[0042] ② Separating the slurry obtained in step ① into solid and liquid to obtain leaching residue and leaching solution; in the leaching solution, the silicon leaching rate was 57.25%, the aluminum leaching rate was 56.22%, and the sodium leaching rate was 93.5%;
[0043] ③Wash the leached slag obtained in step ② with distilled water, and dry at 120°C to obtain scandium-rich titanium slag; TiO in scandium-rich titanium slag 2 The content of Sc is 29.48%, and the content of Sc is 0.014%.
[004...
Embodiment 3
[0049] ①Dry and finely grind the aluminum-dissolving slag until it is passed through a sample sieve to obtain a solid powder with a particle size of less than 74 μm, and use dilute sulfuric acid to selectively leach the aluminum-dissolving slag. The leaching conditions are: the mass fraction of the dilute sulfuric acid solution is 16%, and the reaction temperature The temperature is 35°C, the reaction time is 15min, the liquid-solid ratio is 6:1mL / g, and the stirring speed is 300r / min;
[0050] ② Separating the slurry obtained in step ① into solid and liquid to obtain leaching residue and leaching solution; the leaching rate of silicon in the leaching solution was 94.23%, the leaching rate of aluminum was 82.21%, and the leaching rate of sodium was 97.43%;
[0051] ③Wash the leached slag obtained in step ② with distilled water, and dry at 120°C to obtain scandium-rich titanium slag; TiO in scandium-rich titanium slag 2 The content of Sc is 34.20%, and the content of Sc is 0.01...
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