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Non-rare earth impurity and rare earth element extraction and separation method

A rare earth element and separation method technology, which is applied in the field of extraction and separation of non-rare earth impurities and rare earth elements, can solve the problems that the organic phase and the water phase cannot be separated, the advantages of extraction and separation are not large, and the extraction process is emulsified, so as to achieve comprehensive utilization, The effect of avoiding consumption and eliminating ammonia nitrogen wastewater

Active Publication Date: 2017-09-05
GUANGXI NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, when the P507-N235 system is used for the extraction and separation of rare earth elements, the existence of non-rare earth impurities will interfere with the extraction process. The iron in the rare earth feed solution can be extracted by both P507 and N235, while the back extraction of iron However, it is very difficult; the aluminum in the rare earth feed solution is easy to hydrolyze, and the existence of hydrolyzed products will lead to the occurrence of emulsification during the extraction process, making it impossible to separate the organic phase and the aqueous phase
In addition, for the extraction and separation of rare earth element yttrium, traditional methods mostly use saponification naphthenic acid system. The saponification process of naphthenic acid also consumes ammonia water, so the process of extraction and separation of yttrium will also produce ammonia nitrogen waste water; while P507-N235 can avoid ammonia nitrogen The production of wastewater, but the separation ability of yttrium is far lower than that of the saponified naphthenic acid system, so the P507-N235 system has little advantage in the extraction and separation of yttrium

Method used

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  • Non-rare earth impurity and rare earth element extraction and separation method
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  • Non-rare earth impurity and rare earth element extraction and separation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Mix 30% N235 and 70% kerosene evenly and send them into the acidification tank, mix with 1mol / L hydrochloric acid solution for 10 minutes, after the two phases are separated, separate the upper organic phase, send it into the extraction tank, and mix it with iron, aluminum, The rare earth chloride leaching solution of calcium and magnesium (the concentration of rare earth is 1.5mol / L, the concentration of iron is 1.35g / L, the concentration of aluminum is 3g / L, the concentration of calcium is 4g / L, and the concentration of magnesium is 1.1g / L) according to the phase The ratio (organic phase: water phase) was 1:1 and mixed for 15 minutes. After the two phases were separated, the iron concentration in the feed liquid at the water phase outlet of the extraction tank was measured to drop to 0.07g / L, and the organic phase flowing out from the organic phase outlet of the extraction tank The phase is sent to the stripping tank, and water is added to the organic phase according t...

Embodiment 2

[0039] The filtrate separated from the second stirred tank of Example 1 is sent to the fourth stage of the extraction section in the fractionation extraction process one, and the first stage of the extraction section is added to be composed of naphthenic acid 10%, N235 10%, 2-octanol 40 %, the organic phase of 35% kerosene, add 0.04mol / L hydrochloric acid solution in the 3rd stage of washing section, organic phase: material liquid: the flow ratio of washing liquid is 4:1:1, in the 3rd stage of stripping section Add 1.1mol / L hydrochloric acid solution, wherein the flow ratio of the organic phase to the aqueous phase is 1:2. The organic phase flowing out from the outlet of the stripping section returns to the first stage of the extraction section for recycling after being washed with water in two stages. It has been determined that the main component of the stripping solution flowing out of the water phase outlet of the stripping section is aluminum chloride, and the content of ...

Embodiment 3

[0041] The raffinate obtained in Example 2 is sent to the fifth stage of the extraction section in the fractionation extraction separation process two, and the composition is P50750%, N235 20%, and the organic phase of kerosene 30% is added to the first stage of the extraction section, and after washing The 5th grade of section adds 1.1mol / L hydrochloric acid solution, organic phase: material liquid: the flow ratio of washing liquid is 5:1:0.5, adds 3mol / L hydrochloric acid solution in the 3rd grade of stripping section, wherein organic phase and The flow ratio of the aqueous phase was 1:3. It has been determined that the raffinate mainly composed of La, Ce, Pr, Nd, Ca, Mg, Sm, Eu, Gd, Tb, Dy is obtained at the outlet of the water phase in the extraction section, among which Y, Ho, Er, Tm, Yb, The total concentration of Lu is lower than 310ppm, and the stripping solution mainly composed of Y, Ho, Er, Tm, Yb, and Lu is obtained at the outlet of the aqueous phase of the strippin...

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Abstract

The invention discloses a non-rare earth impurity and rare earth element extraction and separation method. The method comprises the steps that at first, N235 is adopted for extracting and separating iron in rare earth feed liquid, then a sediment iron removing method is used for eliminating the iron in the rare earth feed liquid completely further, and then unsaponifiable naphthenic acid is adopted for extracting and separating aluminum in the feed liquid; the rare earth feed liquid obtained after the iron and aluminum are separated is extracted and grouped by adopting an extraction agent P507-N235, heavy rare earth elements are separated from light and medium rare earth elements, for feed liquid containing the heavy rare earth elements, unsaponifiable naphthenic acid is adopted for separating yttrium and other heavy rare earth elements, for feed liquid containing the light rare earth elements, the extraction agent P507-N235 is adopted for extracting, grouping and separating calcium, magnesium and the light rare earth elements, and the extraction agent P507-N235 continues to be used for separating other rare earth elements one by one. According to the method, non-rare earth impurities such as iron, aluminum, calcium, magnesium and the rare earth elements are separated completely, acid is utilized comprehensively, the adopted extraction agent does not need to be saponified and can be used directly and circularly, an acid reagent and an alkaline reagent do not need to be added in the extraction process, and the separation cost is very low.

Description

technical field [0001] The invention relates to a method for extracting and separating rare earth elements, in particular to a method for extracting and separating non-rare earth impurities and rare earth elements. Background technique [0002] Rare earth elements have unique electronic structures and optical, electrical, and magnetic properties. The development and utilization of rare earth resources is of great significance for promoting the development of my country's economy. Rare earth ore is the main rare earth resource. During the smelting process of rare earth ore, the separation of rare earth elements from the leachate of rare earth ore is an important step. The commonly used separation method of rare earth elements is solvent extraction. The rare earth industry in my country mostly uses acidic phosphorus-type extractant P507 or P204 as the main extractant to separate rare earth elements. [0003] The traditional separation method using P507 or P204 as the main ex...

Claims

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Application Information

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IPC IPC(8): C22B59/00C22B3/28C22B3/40
CPCC22B59/00C22B3/282C22B3/402C22B3/409Y02P10/20
Inventor 刘葵王岩韦梦梅汤晓梦张萍
Owner GUANGXI NORMAL UNIV
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