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Method for preparing 6N-grade neodymium chloride through fractional extraction separation process

A neodymium chloride and extraction technology, applied in the preparation/treatment of rare earth metal chlorides, rare earth metal compounds, rare earth metal halides, etc., to achieve the effects of high product purity, good separation effect, and high yield

Active Publication Date: 2022-07-05
NANCHANG HANGKONG UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] In view of the fact that there is no method for preparing 6N-grade neodymium chloride at present, the present invention establishes a 4N-grade neodymium chloride aqueous solution as the feed liquid and 2-ethylhexylphosphonic acid mono-2-ethylhexyl ester (P507 for short) as the extraction agent, through CePr / NdSm full load fractional distillation extraction separation system and Nd / Sm full load fractional distillation extraction separation system to prepare 6N grade neodymium chloride aqueous solution

Method used

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  • Method for preparing 6N-grade neodymium chloride through fractional extraction separation process

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Embodiment 1

[0020] The unsupported organic phase is a sulfonated kerosene solution of P507, wherein the concentration of P507 is 1.0 mol / L.

[0021] The rare earth element concentrations in the 4N-grade neodymium chloride aqueous solution of the feed solution are Ce 2.8 mg / L, Pr 5.6 mg / L, Nd 147 g / L, and Sm 4.5 mg / L, respectively.

[0022] CePr / NdSm full-load fractional distillation extraction and separation system: with saponification section The obtained loaded CePrNd organic phase is a rare earth saponified organic phase, and the rare earth saponified organic phase loaded CePrNd organic phase enters the CePr / NdSm full-load fractionation extraction system from the first stage; 4N-grade neodymium chloride aqueous solution is used as the feed liquid, and the feed liquid is 4N-grade chloride The neodymium aqueous solution enters the CePr / NdSm full-load fractional distillation extraction system from the 56th stage (feed stage); the balanced aqueous phase of the Nd / Sm full-load fractional d...

Embodiment 2

[0030] The unsupported organic phase is a sulfonated kerosene solution of P507, wherein the concentration of P507 is 1.0 mol / L.

[0031] The concentrations of rare earth elements in the 4N-grade neodymium chloride aqueous solution of the feed solution were Ce 1.4 mg / L, Pr 4.2 mg / L, Nd 145 g / L, and Sm 3.0 mg / L, respectively.

[0032] CePr / NdSm full-load fractional distillation extraction and separation system: with saponification section The obtained loaded CePrNd organic phase is a rare earth saponified organic phase, and the rare earth saponified organic phase loaded CePrNd organic phase enters the CePr / NdSm full-load fractionation extraction system from the first stage; 4N-grade neodymium chloride aqueous solution is used as the feed liquid, and the feed liquid is 4N-grade chloride The neodymium aqueous solution enters the CePr / NdSm full-load fractional distillation extraction system from the 59th stage (feed stage); the balanced aqueous phase of the Nd / Sm full-load fractio...

Embodiment 3

[0040] The unsupported organic phase is a sulfonated kerosene solution of P507, wherein the concentration of P507 is 1.0 mol / L.

[0041] The rare earth element concentrations in the 4N-grade neodymium chloride aqueous solution of the feed solution were Ce 0.70 mg / L, Pr 2.0 mg / L, Nd 143 g / L, and Sm 1.5 mg / L, respectively.

[0042] CePr / NdSm full-load fractional distillation extraction and separation system: with saponification section The obtained loaded CePrNd organic phase is a rare earth saponified organic phase, and the rare earth saponified organic phase loaded CePrNd organic phase enters the CePr / NdSm full-load fractionation extraction system from the first stage; 4N-grade neodymium chloride aqueous solution is used as the feed liquid, and the feed liquid is 4N-grade chloride The neodymium aqueous solution enters the CePr / NdSm full-load fractionation extraction system from the 62nd stage (feed stage); the balanced aqueous phase of the Nd / Sm full-load fractional distillat...

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Abstract

The invention discloses a method for preparing 6N-grade neodymium chloride through a fractional extraction separation process. The method comprises a saponification section, a CePr / NdSm full-load fractional extraction separation system, a saponification section, a purification section, an Nd / Sm full-load fractional extraction separation system and a reverse extraction section. Specifically, a 4N-grade neodymium chloride aqueous solution is used as a feed liquid, rare earth element impurities such as cerium, praseodymium and samarium in the feed liquid are separated and removed through a CePr / NdSm full-load fractional extraction separation system and an Nd / Sm full-load fractional extraction separation system, and a 6N-grade neodymium chloride aqueous solution is prepared. The purity of neodymium in the target product 6N-grade neodymium chloride aqueous solution is 99.99991%-99.99998%, and the yield of neodymium is 96%-98%. The method has the advantages of high product purity, high neodymium yield, good separation effect and the like.

Description

technical field [0001] The present invention is a method for preparing 6N-grade neodymium chloride through a fractional distillation, extraction and separation process. Specifically, a 4N-grade neodymium chloride aqueous solution is used as a feed liquid, and the 4N-grade neodymium chloride is removed through a CePr / NdSm full-load fractionation extraction and separation system and a Nd / Sm full-load fractionation extraction and separation system. The rare earth element impurities cerium, praseodymium and samarium in the aqueous solution of neodymium chloride are used to prepare an aqueous solution of 6N-grade neodymium chloride. The specific technical field of the present invention belongs to the preparation of 6N grade neodymium chloride. Background technique [0002] 6N grade neodymium compounds have important uses in the fields of laser materials, magnetic materials, special ceramics and other high-tech materials. At present, there is no public report on the preparation m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F17/271C01F17/17
CPCC01F17/271C01F17/17C01P2006/80Y02P10/20
Inventor 钟学明万权谢依婷
Owner NANCHANG HANGKONG UNIVERSITY