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.

Active Publication Date: 2017-02-08
永州市湘江稀土有限责任公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The main disadvantage of the above process is that when the P350-hydrochloric acid system separates the chloride solution containing U, Th, RE, and Fe, the raffinate containing thorium and rare earth is first obtained, and the acidity is generally about 2.5mol / L. The liquid is extracted and separated by P350, and the rare earth-containing raffinate and the organic material loaded with pure thorium are obtained
The main problem of the above process is that, due to the relatively low acidity of the operation, the tetravalent titanium in the system is easily hydrolyzed to generate titanium hydroxy complexes and titanium oxide, etc., and it is easy to form three-phase substances during the extraction process, resulting in poor extraction and phase separation. , leading to continuous operation can not be carried out, the feed liquid must be hydrolyzed to remove Ti, adjust the pH value and multiple filtration, clarification and washing treatment, which brings difficulties in operation, and consumes hydrochloric acid at the same time, which brings difficulties in operation; and in the case of low acidity, In the P350 system, the RE and Th separation coefficients are small, and the process needs to be adjusted by increasing the number of extraction and washing stages and the amount of acid used for washing, which greatly increases the operating cost.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention provides a technology for extraction and separation of thorium and rare earth, wherein the technology comprises the steps: firstly, dissolving prior dissolved slag produced in a monazite treatment alkaline-process technology by using hydrochloric acid to obtain a material liquid containing thorium, rare earth and uranium; taking P350 as an extractant, extracting and separating thorium and rare earth in the material liquid containing thorium and rare earth in a high-acidity hydrochloric acid system, to obtain a thorium-loaded organic phase and a raffinate; washing the thorium-loaded organic phase with high-acidity HCl, then carrying out back extraction by using a solution containing HNO3 and NaNO3 to obtain Th(NO3)4 back-extracted solution; and allowing the raffinate containing rare earth and high-concentration hydrochloric acid and obtained from extraction and separation to return to a prior dissolving process. The separation coefficient of thorium and rare earth can be effectively improved in the high-acidity extraction system, the separation efficiency is improved, the separation effect of rare earth and thorium is improved, high-purity thorium nitrate is obtained, rare earth and other valuable elements in the raffinate are comprehensively recycled, the hydrochloric acid in the raffinate is comprehensively utilized, the utilization rate of resources is improved, the postprocessing process is reduced, environment pollution is reduced, and the comprehensive utilization of the resources is achieved.

Description

technical field [0001] The invention relates to a process for extracting and separating thorium and rare earths. Specifically, P350 is used as an extractant to extract and separate thorium and rare earths from a solution containing thorium and rare earths in a high-concentration hydrochloric acid system, which belongs to the field of hydrometallurgical separation. Background technique [0002] Monazite is one of the important rare earth ores. The caustic soda decomposition method is widely used in industry to process monazite concentrate to obtain alkali decomposition slurry, and the rare earth hydroxide solid and sodium phosphate solution are obtained through solid-liquid separation; the rare earth hydrogen obtained by hydrochloric acid is Oxide solids are subjected to refractory treatment to obtain RECl 3 Solution and excellent slag; ("Rare Earth", first edition volume, Metallurgical Industry Press 1978, P221-237), excellent slag after extracting rare earth, that is, urani...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B60/02C22B59/00C22B3/26
CPCY02P10/20
Inventor 俞正明李效平王凯严炳琛陈伯华李金叶徐学道
Owner 永州市湘江稀土有限责任公司
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