Method for extracting scandium from scandium-containing iron-rich acid liquor through P507
An iron-rich and acid solution technology, applied in the field of scandium extraction, can solve the problems of difficult scandium extraction and high extraction rate, and achieve the effects of low cost, high yield and high recovery rate of scandium
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Embodiment 1
[0024] (1) The scandium content in the scandium-containing ferric acid solution is 18mg / L, the iron content is 19.6g / L, and the H + The concentration is 3.2mol / L, and the N235 organic phase with a composition of N235: isooctyl alcohol: kerosene = 25:5:70 is used to extract and remove iron. After liquid separation, an aqueous phase containing scandium and an organic phase containing iron are obtained, and the iron removal rate is 99.4 %;
[0025] (2) Back-extract the iron-containing organic phase with water, the volume ratio is O / W=1:1, back-extract twice, filter the water phase to obtain iron hydroxide precipitation, and recycle the organic phase.
[0026] (3) The scandium-containing aqueous phase is extracted with the P507 organic phase, and the weight composition of the extracted organic phase is controlled to be P507:kerosene=25:75, and the scandium-containing organic phase and the acid-containing aqueous phase are obtained after liquid separation;
[0027] (4) Back-extrac...
Embodiment 2
[0030] (1) The scandium content in the scandium-containing ferric acid solution is 28mg / L, the iron content is 44.2g / L, and the H + The concentration is 2.7mol / L, and the N235 organic phase extraction and iron removal with a weight composition of N235: isooctyl alcohol: kerosene = 28:5:67, after liquid separation, a scandium-containing aqueous phase and an iron-containing organic phase are obtained, and the iron removal rate is 99.6%;
[0031] (2) Back-extract the iron-containing organic phase with water, the volume ratio is O / W=1:1, back-extract twice, and filter the water phase to obtain iron hydroxide precipitation; the organic phase is recycled.
[0032] (3) The scandium-containing aqueous phase is extracted with the P507 organic phase, and the weight composition of the extracted organic phase is controlled to be P507:kerosene=23:77, and the scandium-containing organic phase and the acid-containing aqueous phase are obtained after liquid separation;
[0033] (4) Back-extr...
Embodiment 3
[0036] (1) The scandium content in the scandium-containing ferric acid solution is 26mg / L, the iron content is 35.2g / L, and the H + Concentration is 4.3mol / L, use weight composition to be N235: Isooctyl alcohol: kerosene=24:1:75 N235 organic phase extracts and removes iron, obtains scandium-containing aqueous phase and iron-containing organic phase after liquid separation, and iron removal rate is 99.2%;
[0037] (2) Back-extract the iron-containing organic phase with water, the volume ratio is O / W=1:1, back-extract twice, and filter the water phase to obtain iron hydroxide precipitation; the organic phase is recycled.
[0038] (3) The scandium-containing aqueous phase is extracted with the P507 organic phase, and the weight composition of the extracted organic phase is controlled to be P507:kerosene=22:78, and the scandium-containing organic phase and the acid-containing aqueous phase are obtained after liquid separation;
[0039] (4) Back-extract the scandium-containing org...
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