Extracting method for separating and purifying heavy rare earth

A heavy rare earth and extraction technology, applied in the direction of improving process efficiency, can solve the problems of high acid and alkali consumption, affecting the separation and high purification of heavy rare earth, and low impurity removal rate, so as to achieve reduced acid and alkali consumption, good interface phenomenon, Effect of Separation Improvement

Active Publication Date: 2017-10-24
INST OF APPLIED CHEM JIANGXI ACAD OF SCI
View PDF6 Cites 13 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the separation of heavy rare earths in the P507 extraction system still has the problems of high acidity in stripping, incomplete stripping, and large acid-base consumption, which affects the separation and high purification of heavy rare earths.
In addition, with the gradual improvement of national environmental protection requirements, the existing P507 extraction system has increasingly prominent problems such as large acid-base consumption and ammonia nitrogen pollution. From the perspective of source prevention, the development of new extraction agents with low acid-base consumption and high selectivity and The extraction system is crucial to the development of a new process for the efficient and clean separation of rare earths
[0004] In recent years, functional ionic liquids have been widely concerned in the field of rare earth separation as a research hotspot in green chemistry. The prior art discloses a variety of methods for separating rare earths with functional ionic liquids as extraction agents. Publication No. CN101723975 discloses "A A

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Extracting method for separating and purifying heavy rare earth
  • Extracting method for separating and purifying heavy rare earth
  • Extracting method for separating and purifying heavy rare earth

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Weigh 100g of diglycolic anhydride and dissolve it in 1000mL of tetrahydrofuran, add 189g of di-n-octylamine, and react at room temperature for 48 hours under the protection of argon, and dissolve the obtained solution in 400mL of chloroform after rotary evaporation, and wash with dilute hydrochloric acid solution After distillation and vacuum drying, dioctyl diglycol amic acid was obtained; 90g dioctyl diglycol amic acid, 37.2g aminopropyl imidazole, 61.2g dicyclohexylcarbodiimide, 40.2g 1-hydroxybenzene Dissolve triazole in 1000mL chloroform, react at room temperature under the protection of argon for 12h, filter the solution under reduced pressure, distill and dissolve it in 500mL ethyl acetate, wash with sodium carbonate solution to remove residual 1-hydroxybenzo Triazole, spin out ethyl acetate under vacuum condition, adopt silica gel column chromatography, use chloroform and methanol as mobile phase, obtain 2-[2-(aminopropyl imidazole-2 oxo)]-N,N -dioctylacetamide...

Embodiment 2

[0028] Weigh 100g of diglycolic anhydride and dissolve in 1000mL of tetrahydrofuran, add 189g of di(2-ethylhexyl)amine, and react at room temperature for 48h under the protection of argon, and dissolve the obtained solution in 400mL of chloroform after rotary evaporation, and use After washing with dilute hydrochloric acid solution, distill and vacuum-dry to obtain bis(2-ethylhexyl) diglycol amic acid; 90g bis(2-ethylhexyl) diglycol amic acid, 37.2g aminopropyl imidazole, 61.2 g of dicyclohexylcarbodiimide and 40.2g of 1-hydroxybenzotriazole were dissolved in 1000mL of chloroform, reacted at room temperature under the protection of argon for 12h, and the solution was filtered under reduced pressure, distilled and dissolved in 500mL of ethyl acetate In, wash with sodium carbonate solution to remove residual 1-hydroxybenzotriazole, spin out ethyl acetate under vacuum condition, adopt silica gel column chromatography, use trichloromethane and methanol as mobile phase, obtain 2-[2-...

Embodiment 3

[0030]Weigh 100g of diglycolic anhydride and dissolve it in 1000mL of tetrahydrofuran, add 189g of di-n-octylamine, and react at room temperature for 48 hours under the protection of argon, and dissolve the obtained solution in 400mL of chloroform after rotary evaporation, and wash with dilute hydrochloric acid solution After distillation and vacuum drying, dioctyl diglycol amic acid was obtained; 90g dioctyl diglycol amic acid, 37.2g aminopropyl imidazole, 61.2g dicyclohexylcarbodiimide, 40.2g 1-hydroxybenzene Dissolve triazole in 1000mL chloroform, react at room temperature under the protection of argon for 12h, filter the solution under reduced pressure, distill and dissolve it in 500mL ethyl acetate, wash with sodium carbonate solution to remove residual 1-hydroxybenzo Triazole, spin out ethyl acetate under vacuum condition, adopt silica gel column chromatography, use chloroform and methanol as mobile phase, obtain 2-[2-(aminopropyl imidazole-2 oxo)]-N,N - Dioctyl acetamid...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses an extracting method for separating and purifying heavy rare earth. The method uses an organic phase containing an extracting agent and a thinning agent for extracting rare earth sulfate solution; and the extracting agent is amide amine functional ion liquid. The method adopts water as strip liquor to reversely extract rare earth elements extracted in n-heptane to obtain reverse extracting liquid containing rare earth so as to realize extraction and separation of the rare earth elements. Solubility of the amide amine functional ion liquid structure in the thinning agent and affinity thereof to rare earth ions are improved due to ether oxygen bonds in the amide amine functional ion liquid structure, so that the separation capacity among the rare earth elements is prominently improved, in particular, heavy rare earth elements are preferentially extracted in the extracting process, and pretreatments of iron and aluminum removal are not needed; and in subsequent reverse extracting process, water is generally used for realizing reverse extraction of heavy rare earth to reduce acid and alkali consumption. The method is excellent in interface phenomenon in the extracting process, and can achieve the extraction and separation effects without saponifying the extracting agent and adding a salting-out agent.

Description

technical field [0001] The invention relates to an extraction method for separating and purifying heavy rare earths, belonging to the technical field of rare earth extraction. Background technique [0002] Rare earths have excellent optical, electrical and magnetic properties, and are widely used in the fields of national defense and military industry and high-tech new materials, and have the reputation of "industrial vitamins". Among them, the distribution of medium and heavy rare earths (samarium to lutetium and yttrium) in southern ion-adsorption rare earth mines is as high as 30% to 80%. Close, the product has high added value, and its irreplaceable important application in the fields of high-tech and national defense and military industry really restricts the development of related foreign fields, and it is a strategic resource with absolute competitive advantages. [0003] At present, the separation of single rare earth mainly adopts the extraction and separation meth...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C22B59/00C22B3/36
CPCC22B59/00C22B3/362Y02P10/20
Inventor 崔红敏冯雪娇李玲柳跃伟石劲松
Owner INST OF APPLIED CHEM JIANGXI ACAD OF SCI
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products