Method for purifying and refining high-purity scandium oxide from scandium hydroxide intermediate product
A technology of scandium hydroxide and scandium oxide, which is applied in the direction of scandium oxide/scandium hydroxide, rare earth metal oxides/hydroxides, rare earth metal compounds, etc. High-purity scandium oxide process is cumbersome and other problems, to achieve the effect of shortening the process flow, simple operation, and short process
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Embodiment 1
[0031] Calcining 1000g scandium hydroxide intermediate product at 800°C for 2h to obtain crude scandium oxide.
[0032] Slurry the crude scandium oxide with water to obtain a slurry, add hydrochloric acid to the slurry to adjust the pH to 1.5, maintain the pH at 1.5 and react for 3 hours, filter to obtain the first filter residue, wash the first filter residue with pure water to obtain a leaching residue.
[0033] Put the first-stage leaching residue into a hydrochloric acid solution with a hydrogen ion concentration of 6 mol / L, react at 90°C for 5 hours, and filter to obtain a scandium-rich second-stage leaching solution.
[0034] The second-stage leachate is extracted and phase-separated with extractant P350 to obtain a scandium-rich organic phase; the volume concentration of the extractant P350 is 40%, and the second-stage leachate is extracted with extractant P350 and the diluent used for phase separation is sulfur kerosene. The extraction ratio is O / A=1:1, and the extrac...
Embodiment 2
[0039] Calcining 1000g scandium hydroxide intermediate product at 800°C for 1.5h to obtain crude scandium oxide.
[0040]Slurry the crude scandium oxide with water to obtain a slurry, add hydrochloric acid to the slurry to adjust the pH to 2.0, maintain the pH at 2.0 and react for 4 hours, filter to obtain the first filter residue, wash the first filter residue with pure water to obtain a leaching residue.
[0041] Put the first-stage leaching residue into a hydrochloric acid solution with a hydrogen ion concentration of 8 mol / L, react at 90°C for 3 hours, and filter to obtain a scandium-rich second-stage leaching solution.
[0042] The second-stage leachate is extracted and phase-separated with extractant P350 to obtain a scandium-rich organic phase; the volume concentration of the extractant P350 is 30%, and the second-stage leachate is extracted with extractant P350 and the diluent used for phase separation is sulfur kerosene. The extraction ratio is O / A=2:1, and the numbe...
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