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

A technology of mixing extraction agents and rare earth elements, applied in the direction of improving process efficiency, etc., can solve the problems of large acid consumption, high residual acid in stripping liquid, environmental pollution, etc., and achieve the effect of reducing acid consumption and easy stripping

Active Publication Date: 2008-07-23
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

[0033] 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, Fe2 2 o 3 / REO<0.05%) consumes 30ml of concentrated hydrochloric acid (about 33 grams) to produce samarium europium gadolinium enrichment or further extraction and separation.

[0034] The raffinate obtained (11.7 liters of rare earth sulfate solution containing lanthanum, cerium, praseodymium and neodymium 38.3g / l, Sm 2 o 3 / REO<0.003%) filter after being neutralized to PH4 with 95 grams of magnesia, filtrate adopts 1.5mol / l P2O4 complete extraction, 6mol / L hydrochloric acid back extraction, obtain containing lanthanum cerium praseodymium neodymium 267g / l rare earth chloride solution 1642ml ( Consumption of concentrated hydrochloric acid 1037ml, about 1141 grams), can produce lanthanum cerium praseodymium neody...

Embodiment 2

[0041]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 a rare earth chloride solution containing samarium, europium, and gadolinium 215g / l and an acidity of 1.2mol / L (consumption concentrated Hydrochloric acid 111ml, about 122 grams), the concentration of rare earth in the washing section is 255g / l, the organic phase of loaded rare earth contains rare earth 18g / l, back extraction with 6mol / L hydrochloric acid, obtain containing REO 225g / l,...

Embodiment 3

[0046] 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 5.5mol / L hydrochloric acid to back-extract the organic phase loaded with rare earth, and the first-stage water phase of the back-extraction (retraction liquid REO 230g / l, 1.2mol / L, Nd 2 o 3 / REO 2 / REO2 o 3 / REO45%) ).

[0047] 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 ...

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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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Patent Type & Authority Patents(China)
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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