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Method for extracting and separating light rare earth

A light rare earth and extraction technology, which is applied in the direction of improving process efficiency, can solve the problems of light rare earth extraction, separation, tank filling materials and large consumption of acid and alkali, so as to reduce equipment and tank filling investment, save tank filling materials, and reduce The effect of production costs

Active Publication Date: 2013-02-06
广东省富远稀土有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The present invention solves the problem of excessive consumption of tank filling material and acid-base consumption in the extraction and separation of light rare earth, and provides an advanced and reasonable process technology with less material for tank filling and lower production cost during extraction and separation of light rare earth, so that the production line can achieve continuous , stable, low-consumption assembly line operation requirements

Method used

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  • Method for extracting and separating light rare earth
  • Method for extracting and separating light rare earth
  • Method for extracting and separating light rare earth

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The composition of the light rare earth material is shown in the table below.

[0026] the element

La 2 o 3

CeO 2

PR 6 o 11

Nd 2 o 3

W RE / %

45.57

4.77

11.07

38.59

[0027] The above-mentioned light rare earth materials are separated into four single rare earth element products of La, Ce, Pr, and Nd, and the product quality index reaches the separation effect shown in the following table.

[0028] product name

Rare earth purity (%)

Non-rare earth impurities (%)

La

>99.99

CeO 2 、Pr 6 o 11 、Nd 2 o 3 All<0.002

Ce

>99.99

La 2 o 3 、Pr 6 o 11 、Nd 2 o 3 All<0.002

Pr

>99.9

La 2 o 3 , CeO 2 All 2 o 3 All<0.04

Nd

>99.9

La 2 o 3 , CeO 2 All6 o 11 <0.04

[0029] The organic phase is composed of extractant 2-ethylhexyl phosphate mono-2-ethylhexyl ester (referred to as P507) and diluent keros...

Embodiment 2

[0033] The composition of the light rare earth material is shown in the table below.

[0034] the element

La 2 o 3

CeO 2

PR 6 o 11

Nd 2 o 3

W RE / %

48.86

3.85

10.77

36.52

[0035] The above-mentioned light rare earth materials are separated into four single rare earth element products of La, Ce, Pr, and Nd, and the product quality index reaches the separation effect shown in the following table.

[0036] product name

Rare earth purity (%)

Non-rare earth impurities (%)

La

>99.99

CeO 2 、Pr 6 o 11 、Nd 2 o 3 All<0.002

Ce

>99.99

La 2 o 3 、Pr 6 o 11 、Nd 2 o 3 All<0.002

Pr

>99.9

La 2 o 3 , CeO 2 All 2 o 3 All<0.04

Nd

>99.9

La 2 o 3 , CeO 2 All6 o 11 <0.04

[0037] The organic phase is composed of extractant bis(2-ethylhexyl)phosphoric acid (referred to as P204) and diluent kerosene, the conce...

Embodiment 3

[0041] The composition of the light rare earth material is shown in the table below.

[0042] the element

La 2 o 3

CeO 2

PR 6 o 11

Nd 2 o 3

W RE / %

43.88

4.02

11.88

40.22

[0043] The above-mentioned light rare earth materials are separated into four single rare earth element products of La, Ce, Pr, and Nd, and the product quality index reaches the separation effect shown in the following table.

[0044] product name

Rare earth purity (%)

Non-rare earth impurities (%)

La

>99.99

CeO 2 、Pr 6 o 11 、Nd 2 o 3 All<0.002

Ce

>99.99

La 2 o 3 、Pr 6 o 11 、Nd 2 o 3 All<0.002

Pr

>99.9

La 2 o 3 , CeO 2 All 2 o 3 All<0.04

Nd

>99.9

La 2 o 3 , CeO 2 All6 o 11 <0.04

[0045] The organic phase is composed of extractant bis(2-ethylhexyl)phosphoric acid (referred to as P204) and diluent kerosene, the conce...

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PUM

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Abstract

The invention discloses a method for extracting and separating light rare earth and aims at providing an extracting and separating technology with low separation cost and less one-time investment for the light rare earth. The key points of the technical scheme provided by the invention are as follows: light rare earth materials containing La, Ce, Pr and Nd elements are separated into single elements of the La, the Ce, the Pr and the Nd; and due to the utilization of a fuzzy separation technology, a separation module combined linkage technology, a displacement extraction technology, an extraction amount and washing mount multiplexing technology, an organic feeding technology, a three-outlet technology, a washing and acid regurgitation operating technology, a rare earth washing technology, a diversion technology, an organic phase extraction tank continuous saponification technology and an extraction tank continuous rare earth saponification technology for optimization, more materials filled in the tank for extracting and separating the light rare earth are saved, the production cost is lower and less waste water is produced. The method disclosed by the invention is used for extracting and separating light rare earth elements and belongs to a rare earth separation technology.

Description

technical field [0001] The invention relates to a separation technology of rare earth elements, more specifically, it relates to a method for extraction and separation of light rare earth elements. Background technique [0002] Light rare earth has a large content, a wide range of applications, and a large amount. It is an important part of rare earth elements. Ionic rare earth ores in southern my country (except high yttrium ore) are generally dominated by light rare earths (La, Ce, Pr, Nd), accounting for about 60%. Mixed rare earth concentrates in northern my country and bastnaesite in Sichuan are also Light rare earths dominate, accounting for 96% to 98%. This characteristic of the North and South rare earth mines determines that the key to the separation of rare earths lies in the separation of light rare earths. The separation cost of light rare earths accounts for 30% to 60% of the entire separation cost. The light rare earth components of mixed rare earth concentrate...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B59/00C22B3/40
CPCY02P10/20
Inventor 杨金华凌诚韩旗英韩新福
Owner 广东省富远稀土有限公司
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