Technology for extraction and separation of thorium and rare earth
An extraction and rare earth technology, applied in the field of hydrometallurgical separation, can solve the problems of inability to carry out continuous operation, increase operating costs, and poor extraction and phase separation, and achieve the effects of reducing operating costs, ensuring continuity, and improving separation efficiency.
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Embodiment 1
[0021] Use 9mol / L hydrochloric acid to dissolve monazite and decompose it by alkali method-the excellent slag produced by the excellent dissolution of hydrochloric acid to obtain a feed liquid containing [RE+Th+U+Fe+Ti], and control the [RE+Th+U+ Fe+Ti] concentration is 180g / L, [TiO 2 ]=3.5g / L (calculated as oxide), [H + ]=2.5mol / L, adopt 30%P 350 - The kerosene extraction system is used for UFe / ThRE separation, using countercurrent extraction, the ratio is organic phase:water phase = 4:1, and the number of extraction stages is 15, and the organic phase loaded with U and Fe and the raffinate containing Th and RE are obtained.
[0022] Use P350 to extract and separate Th and RE raffinate, control the total concentration of [RE+Th] in the feed liquid to 100g / L (calculated as oxides), [TiO 2 ]=3g / L (calculated as oxide), [H + ]=5.0mol / L, the P350 extractant is diluted to P350 concentration of 30% with sulfonated kerosene, countercurrent extraction is adopted, the extraction ra...
Embodiment 2
[0027] Use P350 to extract and separate Th and RE raffinate, control the total concentration of [RE+Th] in the feed liquid to 120g / L (calculated as oxides), [TiO 2 ]=1g / L (calculated as oxide), [H + ]=5.5mol / L, the P350 extractant is diluted with sulfonated kerosene to a P350 concentration of 35%, countercurrent extraction is used, the extraction phase is organic phase:water phase=4:1, and the number of extraction stages is 20. The thorium-loaded organic phase is countercurrently washed with 8 mol / L HCl, and the ratio is organic phase:water phase=15:1, and the number of stages is 10. Then use 0.1mol / LHNO 3 and 0.1mol / L NaNO 3 The solution is carried out countercurrent stripping, compared to organic phase: water phase=10:1, order of 20, obtains Th(NO 3 ) 4 Solution, which contains rare earth 0.15% REO. The obtained rare earth-containing raffinate is returned to the step of alkali treatment of hydrochloric acid in monazite. During the extraction process, it has been contin...
Embodiment 3
[0029] Use P350 to extract and separate Th and RE raffinate, control the total concentration of [RE+Th] in the feed liquid to 80g / L (calculated as oxides), [TiO 2 ]=2g / L (calculated as oxide), [H + ]=4.8mol / L, the P350 extractant is diluted to P350 concentration of 50% with sulfonated kerosene, countercurrent extraction is adopted, the extraction ratio is organic phase:water phase=8:1, and the number of extraction stages is 18. The thorium-loaded organic phase is countercurrently washed with 4.8 mol / L HCl, and the ratio is organic phase:water phase=20:1, and the number of stages is 18. Then use 0.05mol / LHNO 3 and 0.05mol / L NaNO 3 The solution is carried out counter-current stripping, compared to organic phase: water phase=8:1, order of 18, obtains Th(NO 3 ) 4 The solution, wherein the rare earth-containing raffinate obtained by containing 0.26% REO of rare earth, is returned to the hydrochloric acid excellent dissolving step in the alkaline treatment of monazite. During t...
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