A method for enriching scandium from titanium dioxide wastewater
A titanium dioxide wastewater, enrichment technology, applied in the direction of improving process efficiency, can solve the problems of wasting titanium dioxide wastewater scandium resources, increasing production costs, etc., to solve scandium loss, reduce production costs, reduce consumption and pollutant discharge. Effect
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Embodiment 1
[0027] A method for enriching scandium from titanium dioxide wastewater, comprising the following steps:
[0028] (1) Primary extraction: 20.41 m of titanium dioxide wastewater 3 , Sc 2 o 3 12.10 mg / L, add the organic phase to the titanium dioxide wastewater for one extraction, the first extraction is a three-stage countercurrent extraction, the ratio is O:A=1:10, and the Sc in the extraction raffinate 2 o 3 0.90 mg / L, the scandium extraction rate is 92.60%, and the Sc in the organic phase is loaded once 2 o 3 326.42 mg / L,;
[0029] (2) One-time back-extraction: One-time back-extraction is carried out with one extraction-loaded organic phase. The operating conditions are O:A = 1:1, the content of sodium hydroxide is 10%, the temperature is 60 ℃, and the time of one-time back-extraction is After 20 min, the organic phase was recovered after the reaction was completed, and the lye was filtered to obtain a back-extraction filter cake, and the lye was recovered, and the pri...
Embodiment 2
[0036] A method for enriching scandium from titanium dioxide wastewater, comprising the following steps:
[0037] (1) Primary extraction: 30.20 m of titanium dioxide wastewater 3 , Sc 2 o 3 11.20 mg / L, add the organic phase to the titanium dioxide wastewater for one extraction, the first extraction is a three-stage countercurrent extraction, the ratio is O:A=1:10, and the Sc in the extraction raffinate 2 o 3 0.93 mg / L, the scandium extraction rate is 91.73%, and the Sc in the organic phase is loaded once 2 o 3 346.5 mg / L,;
[0038] (2) One-time back-extraction: One-time back-extraction is carried out with one-time extraction loaded organic phase. The operating conditions are O:A = 1:1, the content of sodium hydroxide is 10%, the temperature is 70 ℃, and the time of one-time back-extraction is After 20 min, the organic phase was recovered after the reaction was completed, and the lye was filtered to obtain a back-extraction filter cake, and the lye was recovered, and the...
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