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A kind of extraction method of high-purity ammonium rhenate

An extraction method, ammonium rhenate technology, which is applied in the field of extraction of high-purity ammonium rhenate, can solve the problems of limited effect of rhenium extraction/purification process, difficulty in efficiently preparing high-purity ammonium rhenate, low efficiency, etc., and is easy to promote And industrial use, simple and easy operation, low equipment demand effect

Active Publication Date: 2021-12-17
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] In order to solve the problem that the existing rhenium extraction / purification process has limited effects, low efficiency or low purity, and is difficult to efficiently prepare high-purity ammonium rhenate, the invention provides a method for extracting high-purity ammonium rhenate

Method used

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  • A kind of extraction method of high-purity ammonium rhenate
  • A kind of extraction method of high-purity ammonium rhenate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] Preparation of anion exchange resin:

[0041] a1) be that the lactose powder that the average particle diameter is 1mm is placed in methyl acrylate and carries out impregnation adsorption 10min, filter out the lactose powder after its impregnation adsorption is saturated;

[0042] a2) Add divinylbenzene to benzene methane to prepare a 16.5wt% reaction solution, add cumene hydrogen peroxide to the reaction solution, the concentration of cumene hydrogen peroxide in the reaction solution is 0.10wt%, and every 100mL 5.5 g of lactose powder adsorbed with methyl acrylate was added to the reaction solution, and placed under stirring conditions to react, and filtered to obtain polymer pellets with a cross-linking degree of 5.5%;

[0043] a3) polymer pellets are placed in water for dipping and dissolving the lactose skeleton and add ferric chloride and chloroethyl ether to carry out chloromethylation reaction, to obtain the chlorinated pellets that the chlorine content is 17wt%;...

Embodiment 2

[0046] Preparation of anion exchange resin:

[0047] a1) the lactose powder that the mean particle diameter is 3mm is placed in methyl acrylate to carry out immersion adsorption 3min, to filter out the lactose powder after its immersion absorption saturation;

[0048] a2) adding divinylbenzene to benzene methane to prepare a 18wt% reaction solution, adding cumene hydrogen peroxide to the reaction solution, the concentration of cumene hydrogen peroxide in the reaction solution is 0.10wt%, and every 100mL reacts 6g of lactose powder adsorbed with methyl acrylate was added to the liquid, and placed under ultrasonic vibration to react, and filtered to obtain polymer pellets with a cross-linking degree of 5.0%;

[0049] a3) adding ferric chloride and chloroethyl ether to carry out chloromethylation reaction after placing polymer pellets in water and dipping and dissolving lactose skeleton, obtaining the chlorinated pellets that the chlorine content is 18wt%;

[0050] a4) Dip the c...

Embodiment 3

[0052] Preparation of anion exchange resin:

[0053] a1) be that the lactose powder that the average particle diameter is 1.5mm is placed in methyl acrylate and carry out immersion adsorption 5min, filter out the lactose powder after its immersion absorption saturation;

[0054] a2) adding divinylbenzene to benzene methane to prepare a 10wt% reaction solution, adding cumene hydrogen peroxide to the reaction solution, the concentration of cumene hydrogen peroxide in the reaction solution is 0.05wt%, and every 100mL reacts 3 g of lactose powder adsorbed with methyl acrylate was added to the liquid, and placed under stirring conditions to react, and filtered to obtain polymer pellets with a cross-linking degree of 4.5%;

[0055] a3) polymer pellets are placed in water and dipped to dissolve the lactose skeleton and then add ferric chloride and chloroethyl ether to carry out chloromethylation reaction, to obtain the chlorinated pellets that the chlorine content is 15wt%;

[0056]...

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Abstract

The invention relates to the technical field of chemical hydrometallurgy and rare precious metal recycling, in particular to a method for extracting high-purity ammonium rhenate. The method comprises the following steps: 1) redissolving the crude ammonium rhenate: dissolving the crude ammonium rhenate in dilute sulfuric acid, and preparing a rhenium solution after filtering; 2) ion exchange: performing ion exchange on the rhenium solution with an anion exchange resin, Obtain the crude extract after desorption; 3) Impurity removal and crystallization: use cation exchange resin to carry out further ion exchange on the crude extract, remove cationic impurities and crystallize to obtain high-purity ammonium rhenate crystals. The method of the invention has high extraction efficiency and simple and easy operation; the extracted ammonium rhenate has high purity and can effectively remove metal ion impurities; the demand for equipment is low, and it is easy to popularize and use industrially.

Description

technical field [0001] The invention relates to the technical field of chemical hydrometallurgy and rare and precious metal recycling, in particular to a method for extracting high-purity ammonium rhenate. Background technique [0002] Rhenium is an important strategic rare metal with special properties such as high melting point, creep resistance, high strength, corrosion resistance and wear resistance. It is widely used in aerospace, national defense, electronic industry, chemical industry and other national economic fields. The abundance of rhenium in nature is extremely low, and there are very few independent minerals, mostly associated with porphyry copper ores and molybdenite. Due to the scarcity of its resources and the particularity of its distribution, the separation and extraction of rhenium is difficult, so the production of rhenium has been low and expensive for a long time. Rhenium is often associated with copper-molybdenum ore and enters the smelting process w...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B61/00C22B3/42C22B3/22
CPCC22B61/00C22B3/42C22B3/22Y02P10/20
Inventor 郑国渠张惠斌曹华珍
Owner ZHEJIANG UNIV OF TECH