Process for extracting and separating rare-earth elements
A rare earth element and extraction technology, applied in the field of rare earth solvent extraction and separation, can solve the problems of slow solid-liquid reaction, affecting product quality, incompleteness, etc., and achieve the effects of reducing production costs, saving three waste treatment costs, and eliminating pollution
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Embodiment 1
[0046] The light-burned magnesia obtained by roasting magnesite at 850-900°C for 2 hours is dissolved by adding glutaric acid, the liquid-solid weight ratio is 80:1, and the amount of glutaric acid is 110% of the theoretical amount. After reacting for 40 minutes, a pure magnesium glutarate aqueous solution (MgO: 1.2%) was obtained through clarification and filtration.
[0047] Add magnesium glutarate aqueous solution with a flow rate of 3.73L / min, lanthanum cerium chloride solution (0.928mol / L) with a flow rate of 0.8L / min, and 1.5mol / L P507 organic phase with a flow rate of 4L / min. Co-flow extraction is carried out in the extraction tank, the mixing time is 25 minutes, and the clarification is 20 minutes to obtain a loaded organic phase containing refractory rare earth ions lanthanum and cerium. The rare earth content REO is 0.185mol / L, and the pH value of the raffinate aqueous phase is 2.8. The content is less than 0.001mol / L.
[0048] The loaded organic phase is directly u...
Embodiment 2
[0050] The light-burned magnesia and calcium oxide mixture obtained by roasting dolomite at 800-850°C for 2 hours is dissolved by adding formic acid, the liquid-solid weight ratio is 100:1, the amount of formic acid is 120% of the theoretical amount, and the reaction is carried out at 20°C After 40 minutes, after clarification and filtration, pure aqueous solution of magnesium bicarbonate and calcium bicarbonate (MgO+CaO: 0.92%) was obtained.
[0051] Add magnesium formate and calcium formate aqueous solution at a flow rate of 6.4L / min, lanthanum cerium chloride solution (0.665mol / L) at a flow rate of 1.5L / min, and 1.3mol / L P204 organic phase at a flow rate of 6L / min into the 12th grade Extraction is carried out in the pre-extraction tank, the mixing time is 25 minutes, and after 6 stages of co-current and 6 stages of countercurrent extraction, the loaded organic phase containing lanthanum and cerium is obtained, the rare earth content REO is 0.165mol / L, and the pH value of the...
Embodiment 3
[0054] Calcium oxide obtained by calcining limestone at 800-850°C for 2 hours, was dissolved by adding butyric acid, the liquid-solid weight ratio was 16:1, the amount of butyric acid was 160% of the theoretical amount, reacted at 70°C for 30 minutes, after clarification Filter to obtain a pure aqueous solution of calcium butyrate (CaO: 6.25%).
[0055] Add the calcium butyrate aqueous solution at a flow rate of 1.12L / min, the lanthanum nitrate solution (0.744mol / L) at a flow rate of 1.5L / min, and the 1.5mol / L P507 organic phase at a flow rate of 6L / min into the 8-stage pre-extraction tank Carry out extraction, the mixing time is 25 minutes, after 5 stages of co-current and 3 stages of countercurrent extraction, a loaded organic phase containing refractory rare earth ion lanthanum is obtained, the rare earth content REO is 0.185mol / L, and the pH value of the raffinate aqueous phase is 4.5. REO content 0.0016mol / L.
[0056] The loaded organic phase was directly used for La / Ce ...
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