Process for extracting rare earth element by non-saponifiable phosphorous mixing extractant

A technology of mixing extractants and rare earth elements, applied in the direction of improving process efficiency, can solve the problems of high nitric acid concentration, large acid consumption and high production cost, and achieve the advantages of improving stripping efficiency, improving production capacity and reducing acid consumption. Effect

Active Publication Date: 2006-07-19
GRIREM ADVANCED MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The first and second methods have good separation effects and are widely used, but they must be saponified with ammonia water, sodium hydroxide, ammonium bicarbonate, etc., which will produce a large amount of ammonia nitrogen wastewater and cause great pollution to the environment.
The third method is the process adopted by France Rhodia and American Molybdenum Company. It is derived from the rare earth nitrate solution obtained when processing monazite ore to separate rare earth. The concentration of nitric acid in the extraction system of this process is high, so the production cost is high. stop state
The fourth process was invented by Beijing General Research Institute of Nonferrous Metals. It is applied to the extraction and separation of rare earth elements from the sulfuric acid rare earth solution obtained when treating Baotou rare earth mines with sulfuric acid method. Less consumption, but due to the low concentration of rare earth in the sulfuric acid system (<45g / L), the investment in equipment extraction agent is large; P204 has a strong extraction ability under acidic conditions, and it is easy to emulsify when the acidity of the feed liquid is low, so a certain amount of acid needs to be added during extraction , while medium and heavy rare earth stripping is very difficult, the residual acid in the stripping liquid is high, and the acid consumption is large

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] 1000 grams of bastnaesite and monazite mixed rare earth ore (REO 50%) are roasted with sulfuric acid, soaked in water, neutralized and removed to obtain 11.5 liters of pure rare earth sulfate solution, the acidity is pH 4, and the main component is REO 40g / L, Fe<0.05g / L, P<0.005g / L, ThO2<0.001g / L, directly use 60% non-saponifiable P204 (1.0mol / L) and 40% non-saponifiable P507 (1.0mol / L) Nd / Sm extraction grouping with the mixed extraction agent, using 7-stage extraction, 13-stage washing, 8-stage back extraction, compared: organic / material liquid / washing liquid is 0.25 / 1 / 0.015, and the washing liquid is 210g containing samarium, europium and gadolinium / l, acidity 1.5N rare earth chloride back-extraction liquid (consumption of concentrated hydrochloric acid 110ml, about 121 grams), the rare earth concentration in the washing section is 245g / l, and the loaded rare earth organic phase contains rare earth 18g / l, back-extracted with 6N hydrochloric acid to obtain Containing...

Embodiment 2

[0042] 1000 grams of bastnaesite and monazite mixed rare earth ore (REO 50%) are roasted with sulfuric acid, soaked in water, neutralized and removed to obtain 12.5 liters of pure rare earth sulfate solution, the acidity is pH 4, and the rare earth concentration REO is 36.5 g / L, without adjusting acidity, directly use 70% non-saponifiable P204 (1.0mol / L) and 30% non-saponifiable P507 (1.0mol / L) mixed extractant for Nd / Sm extraction grouping, using 7-stage extraction, 13-stage washing, 8-stage stripping, compared: organic / material liquid / washing liquid is 0.25 / 1 / 0.014, and the washing liquid adopts rare earth chloride solution containing samarium, europium and gadolinium 215g / l, acidity 1.2N (consumption of concentrated hydrochloric acid 111ml , about 122 grams), the concentration of rare earths in the washing section is 255g / l, and the organic phase of loaded rare earths contains 18g / l of rare earths, and back-extracted with 6N hydrochloric acid to obtain 225g / l of REO and an a...

Embodiment 3

[0047] 1000 grams of bastnaesite and monazite mixed rare earth ore were roasted with sulfuric acid, soaked in water, neutralized and removed to obtain a pure rare earth sulfate solution with an acidity of pH 4.5 and a REO concentration of 43g / L. A mixed extractant of 70% 1.2 mol / L non-saponifiable P204 and 30% 1.2 mol / L non-saponifiable P507 was used for fractional extraction and separation of cerium / praseodymium. The last stage of the stripping section enters 5.5N hydrochloric acid to strip the rare earth-loaded organic phase, and the first stage of stripping the aqueous phase (the stripping liquid REO 230g / l, 1.2N, Nd2O3 / REO45%) through concentrated crystallization .

[0048] Compared with Comparative Example 3, this process does not need to add sulfuric acid to adjust the acidity of the feed liquid, and also saves a magnesium oxide neutralization and filtration process. One fractionation extraction can produce three marketable products, and the rare earth recovery rate is h...

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Abstract

The extraction and separation method for rare-earth element comprises: with rare-earth solution contained a plurality of rare-earth elements as material, preparing mixed extractant with the non-saponifiable P204 and one or two from P507, P229, P350, TBP, C272, C301, C302 and HEOPPA; in the mixed solution with rare-earth sulfate solution, or rare-earth sulfate and rare-earth chloride solution and rare-earth nitrate solution, extracting and separating rare-earth elements. This invention eliminates saponification to overcome pollution, reduces acidity to improve rare-earth concentration, and decreases the main material consumption more than 30% compared with the technique with NH4HCO3 and P507.

Description

technical field [0001] The invention relates to a process for extracting and separating rare earth elements. Specifically, the rare earth solution containing various rare earth elements obtained from the treatment of rare earth ores is used as raw material, and one or both of non-saponifiable P204 and non-saponifiable P507, P229, P350, TBP, C272, C301, C302, and HEOPPA are used. The invention relates to a process for extracting and separating rare earth elements in rare earth sulfuric acid solution or a mixed solution of rare earth sulfuric acid solution, rare earth chloride solution and rare earth nitrate solution with a prepared mixed extractant. Background technique [0002] Lanthanum, cerium, praseodymium, neodymium, promethium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium, lutetium, yttrium, and scandium are collectively called rare earth elements. Their properties are very similar, except for promethium. Except for non-exist...

Claims

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Application Information

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IPC IPC(8): C22B3/26
CPCY02P10/20
Inventor 黄小卫李建宁彭新林龙志奇朱兆武崔大立赵娜刘营李红卫张国成
Owner GRIREM ADVANCED MATERIALS CO LTD
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