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A method for separating and purifying selenium and tellurium from a mixture of selenium and tellurium

A mixture, selenium-tellurium technology, applied in the field of tellurium, separation and purification of selenium, can solve the problems of difficult separation of selenium-tellurium mixture, low extraction rate of selenium-tellurium and the like

Active Publication Date: 2018-01-05
YUNNAN COPPER CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In view of the above-mentioned deficiencies in the prior art, the object of the present invention is to provide a method for separating and purifying selenium and tellurium from a mixture of selenium and tellurium, aiming to solve the problems in the prior art that the extraction rate of selenium and tellurium is low, the mixture of selenium and tellurium is difficult to separate, etc.

Method used

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  • A method for separating and purifying selenium and tellurium from a mixture of selenium and tellurium

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Effect test

Embodiment 1

[0026] 120Kg wet weight of selenium-tellurium mixture, which contains 35% water, 28.304% selenium, and 22.94% tellurium. After slurrying, add 150L hydrochloric acid, and add oxidant for water-soluble chlorination (the amount of oxidant added is until the slurry There are no visible solids in the medium, the oxidizing agent can be sodium chlorate), and the liquid-solid ratio is 3:1. After two staged reductions of sulfur dioxide (the first reduction steam is heated to 90°C, the second reduction steam is heated to 90°C, both using liquid sulfur dioxide), the output of selenium is 21.5kg, tellurium is 17.8kg, and the purity of selenium and tellurium is respectively 99% , tellurium 95%, the yield of selenium is 96.41%, the yield of tellurium is 94.51%.

Embodiment 2

[0028] 120Kg wet weight of selenium-tellurium mixture, which contains 35% water, 28.304% selenium, and 22.94% tellurium. After slurrying, add 140L hydrochloric acid, and add oxidant for water-soluble chlorination (the amount of oxidant added is until the slurry There are no visible solids in the medium, the oxidizing agent can be sodium chlorate), and the liquid-solid ratio is 3:1. After two staged reductions of sulfur dioxide (the first reduction steam is heated to 80°C, and the second reduction steam is heated to 90°C, both using liquid sulfur dioxide), the output of selenium is 20.4kg, tellurium is 16.8kg, and the purity of selenium and tellurium is 97% respectively. , tellurium 94%, the yield of selenium is 94.31%, the yield of tellurium is 92.64%.

Embodiment 3

[0030] 120Kg wet weight of selenium-tellurium mixture, which contains 35% water, 28.304% selenium, and 22.94% tellurium. After slurrying, add 160L hydrochloric acid, and add oxidant to carry out water-soluble chlorination (the amount of oxidant added is until the slurry There are no visible solids in the medium, the oxidizing agent can be sodium chlorate), and the liquid-solid ratio is 3:1. After two staged reductions of sulfur dioxide (the first reduction steam is heated to 80°C, and the second reduction steam is heated to 80°C, both using liquid sulfur dioxide), the output of selenium is 20.9kg, tellurium is 16.5kg, and the purity of selenium and tellurium is respectively 99%. , tellurium 94%, the yield of selenium is 94.53%, the yield of tellurium is 94.31%.

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Abstract

The invention discloses a method of separating and purifying Se and Te from a Se / Te mixture, which includes the following steps: 1) Se / Te mixture leaching: firstly slurrying the Se / Te mixture and then adding hydrochloric acid and an oxidant into slurry to perform water-dissolving and chlorination leaching, and filtering a leached product, wherein filter residues are fed back to selenium reduction and a filtrate is used for later use; 2) primary reduction of the filtrate: heating the filtrate with vapor, adding SO2 to perform the primary reduction of the filtrate, and after a certain time, filtering the reduced filtrate to generate selenium powder and a primary reduced solution; and 3) secondary reduction of the primary reduced solution: heating the primary reduced solution with vapor, feeding SO2 to perform the secondary reduction, and after a certain time, filtering the primary reduced solution to obtain crude tellurium and a secondary reduced solution. The method is carried out in a manner of leaching the Se / Te mixture and reducing the leachate in sections, so that the grade of selenium reaches 95-99% and the grade of tellurium reaches 90-95% after reduction, thereby greatly increasing the purities of Se and Te after recycling.

Description

technical field [0001] The invention relates to the technical field of hydrometallurgy, in particular to a method for separating and purifying selenium and tellurium from a selenium-tellurium mixture. Background technique [0002] In the process of copper anode slime treatment, the selenium in the anode slime exists in the chlorinated liquid after chlorination, and the chlorinated liquid is reduced by sulfur dioxide in one stage to produce crude selenium, and the reduced liquid in the first stage is reduced to produce crude selenium in the second stage. A selenium-tellurium mixture containing about 20-30% selenium, 15-25% tellurium, and 20-30% copper is produced. The crude selenium produced by the first-stage reduction is refined by vacuum melting to produce selenium products, while for the second-stage reduction product For the selenium-tellurium mixture, there is no mature process for the separation and purification of selenium and tellurium, but the existing technology ha...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B19/02
Inventor 叶钟林张邦琪沙梅王鹏程夏挺郭开师李玉东郑金和
Owner YUNNAN COPPER CO LTD
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