Macroporous ion exchange resin with function of highly selectively adsorbing rhenium metal ions and preparation method of macroporous ion exchange resin

An ion exchange resin and selective adsorption technology, which is applied in the direction of cation exchange materials, chemical instruments and methods, and other chemical processes, can solve the problems of complex process, low rhenium yield, and easy emulsification, so as to improve ion exchange rate, Effect of increasing the amount of amino grafts and enhancing the adsorption capacity of rhenium

Inactive Publication Date: 2020-12-04
ANHUI WANDONG CHEM
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are certain problems in the enrichment and recovery of rhenium by the extraction method. For example, rhenium and molybdenum have co-extraction properties, and the extraction and separation effect is not ideal. The emulsification phenomenon is also prone to occur during the extraction process, resulting in the loss of the extraction agent and the decrease in the yield. In addition, common organic extraction agents have Certain toxicity brings difficulties to wastewater treatment
The chemical method requires many reagents, complicated process, and the yield of rhenium is relatively low. There is also the problem of a large amount of waste water and waste residue in the production process.
[0004] Compared with the extraction separation method and chemical method, the ion exchange method has low toxicity, simple operation and good selectivity, but the current rhenium ion exchange resin has the disadvantages of low ion exchange capacity and poor adsorption selectivity.

Method used

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  • Macroporous ion exchange resin with function of highly selectively adsorbing rhenium metal ions and preparation method of macroporous ion exchange resin

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Experimental program
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Effect test

Embodiment 1

[0023] A preparation method of a macroporous ion exchange resin with highly selective adsorption of rhenium metal ions, comprising the following steps:

[0024] S1. Polymerization: Monomer methyl acrylate and cross-linking agent divinylbenzene are used to prepare white balls by suspension polymerization, in which ternary porogen diethylbenzene-isobutanol-toluene is added;

[0025] S2. Amino functionalization and cross-linking: After the white ball is fully swollen, add triethylenetetramine to reflux in a water bath at 70°C, add glutaraldehyde dropwise, continue to reflux in a water bath, and react for 3 hours;

[0026] S4. Methylation: mix the aminated sphere with formic acid, formaldehyde, and water, the mass ratio of the aminated sphere to formic acid, formaldehyde, and water is 18:200:3:40, and react at 50°C for 60 minutes to obtain the intermediate product resin A;

[0027] S4. Inorganic modification: the intermediate product resin A is soaked in NaOH solution, washed with...

Embodiment 2

[0029] A preparation method of a macroporous ion exchange resin with highly selective adsorption of rhenium metal ions, comprising the following steps:

[0030] S1. Polymerization: Preparation of seed white balls by precipitation polymerization: add divinylbenzene, methyl acrylate, initiator azobisisobutyronitrile, ternary porogen diethylbenzene-isobutanol-toluene and The solvent is acetonitrile, ultrasonically dispersed, nitrogen deoxygenated, heated to 70°C, reacted for 4 hours, suction filtered, washed, and dried;

[0031] S2. Amino functionalization and cross-linking: After the white ball is fully swollen, add triethylenetetramine to reflux in a water bath at 70°C, add glutaraldehyde dropwise, continue to reflux in a water bath, and react for 3 hours;

[0032] S4. Methylation: mix the aminated sphere with formic acid, formaldehyde, and water, the mass ratio of the aminated sphere to formic acid, formaldehyde, and water is 18:200:3:40, and react at 50°C for 60 minutes to ob...

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Abstract

The invention relates to a preparation method of a macroporous ion exchange resin capable of highly selectively adsorbing rhenium metal ions. According to the invention, gradient pore-forming is carried out by adopting a multi-element pore-forming agent, so that the pore channel structure is improved, the ion exchange resistance is reduced, and the ion exchange rate is increased. Glutaraldehyde isused as an amino modified cross-linking agent, so that the amino grafting amount is increased, the active center is increased, rapid diffusion and ion exchange of rhenium are facilitated, and the exchange capacity is further improved. Fe and Ce are adopted to carry out inorganic modification on the ion exchange resin together, so that the rhenium adsorption capacity is enhanced, and the selectivity is improved. When other ions are contained, the macroporous ion exchange resin prepared by the method has high rhenium selectivity, and the result shows that the macroporous ion exchange resin hashigh rhenium selectivity.

Description

technical field [0001] The invention belongs to the field of ion exchange resins, in particular to a macroporous ion exchange resin with highly selective adsorption of rhenium metal ions. Background technique [0002] Rhenium is a rare refractory metal, which not only has good plasticity, mechanical properties and creep resistance, but also has good wear resistance and corrosion resistance. Rhenium and its alloys are widely used in aerospace, electronics, petrochemical and other fields. The global reserves of rhenium are very small, and the price is relatively expensive. Therefore, the separation and collection of rhenium is very critical. [0003] Common methods for rhenium separation and enrichment are extraction separation, ion exchange, redox, precipitation separation, activated carbon adsorption and so on. There are certain problems in the enrichment and recovery of rhenium by the extraction method. For example, rhenium and molybdenum have co-extraction properties, a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08J9/40C08J9/28C08F220/14C08F8/02C08F8/00C08F8/32C08F212/36B01J39/20B01J20/26B01J20/30
CPCB01J20/267B01J39/20C08F8/02C08F212/36C08F220/14C08J9/286C08J9/40C08J2325/02C08J2325/08C08F8/00C08F8/32
Inventor 姚能平刘建荣胡德凯王晗樊致娟
Owner ANHUI WANDONG CHEM
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