Method for extracting scandium
An extraction and leaching technology, applied in the field of metallurgy, can solve the problems of failure to realize industrialization, high scandium recovery efficiency and recovery cost, low scandium content, etc., and achieve the effects of low production cost, high scandium recovery rate and high purity.
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Embodiment 1
[0022] Embodiment 1 adopts the inventive method to extract scandium
[0023] The high-titanium slag obtained by smelting scandium-containing vanadium-titanium magnetite concentrate, and the high-titanium slag is chlorinated to obtain titanium tetrachloride and chloride slag. Grind the chlorinated slag with a particle size of ≤325 mesh. Sulfuric acid is used as the leaching reagent, and the concentration of sulfuric acid is controlled at: 40wt%; the mass ratio of leaching solid to liquid is controlled at: 1:3; the leaching temperature is controlled at: 80°C; and the leaching time is controlled at: 8h.
[0024] Filter the leaching liquid, use CA-100 as the extraction reagent, and control the concentration of the extraction agent at: 0.008mol.L -1 ;Comparison is controlled at: O / A=1:2; The concentration of the extraction stock solution is controlled at: 100mg / L -1 .
[0025] The organic phase separated after extraction is back-extracted, and NaOH solution is used as the stripp...
Embodiment 2
[0027] Embodiment 2 adopts the inventive method to extract scandium
[0028] The high-titanium slag obtained by smelting scandium-containing vanadium-titanium magnetite concentrate, and the high-titanium slag is chlorinated to obtain titanium tetrachloride and chloride slag. Grind the chlorinated slag with a particle size of ≤325 mesh. Sulfuric acid is used as the leaching reagent, the concentration of sulfuric acid is controlled at 35wt%, the mass ratio of leaching solid to liquid is 1:4, the leaching temperature is 85°C, and the leaching time is 10h.
[0029] Filter the leaching liquid, use CA-100 as the extraction reagent, and control the concentration of the extraction agent at: 0.009mol.L -1 ;Compared to control: O / A=1 / 3;The concentration of the extraction stock solution is controlled at: 90mg / L -1 .
[0030] The organic phase separated after extraction is back-extracted, and NaOH solution is used as the stripping agent, and the concentration of the stripping agent is ...
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