Method for recovering rare earth, aluminum and silicon from rare earth-containing aluminum-silicon waste
A rare earth, aluminum and silicon technology, applied in chemical instruments and methods, preparation/processing of rare earth metal compounds, rare earth metal nitrates, etc. , the effect of reducing the dosage
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Embodiment 1
[0051] After slurrying the rare earth-containing aluminum-silicon waste, the liquid-solid ratio is 3:1, add 1mol / L hydrochloric acid to treat the rare-earth-containing aluminum-silicon waste, control the pH value of the reaction process to 2.5, and mechanically stir at 10°C (200rad / min) After leaching for 12 hours, control the pH of the solution at the end of the reaction to 2.0; filter to obtain the acid leaching solution containing rare earth and aluminum and silicon-rich slag. The leaching rates of aluminum, rare earth and silicon (all as oxides) in the acid leaching solution containing rare earth and aluminum were 66.9%, 85.3% and 3.5%, respectively.
Embodiment 2
[0055] Before the acid leaching reaction, the rare earth-containing aluminum-silicon waste is crushed, ground, and slurried. After sizing, the liquid-solid ratio is 4:1. Add 3mol / L hydrochloric acid to treat rare earth-containing aluminum-silicon waste, control the pH value of the reaction process to 2.0, leaching with mechanical stirring (180rad / min) at 20°C for 8h, and control the pH of the solution at the end of the reaction=1.8; filter to obtain rare earth and aluminum-containing pickling solution and silicon-rich slag. The leaching rates of aluminum, rare earth and silicon in the acid leaching solution containing rare earth and aluminum (all calculated as oxides) were 73.6%, 89.2% and 4.2%, respectively.
Embodiment 3
[0057] The liquid-solid ratio is 5:1 after slurrying the rare earth-containing aluminum-silicon waste. Add 5mol / L hydrochloric acid to treat the aluminum-silicon waste containing rare earth, control the pH value of the reaction process to 1.8, leaching with mechanical stirring (220rad / min) at 40°C for 6h, and control the pH of the solution at the end of the reaction=1.5; filter to obtain the rare earth and aluminum-containing pickling solution and silicon-rich slag. The leaching rates of aluminum, rare earth and silicon (calculated as oxides) in the acid leaching solution containing rare earth and aluminum were 77.2%, 91.5% and 4.5%, respectively.
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