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A method for separating and extracting selenium and tellurium from a high selenium and low tellurium solution

A solution and high-selenium technology, applied in the field of separation and extraction of selenium from tellurium, high-selenium and low-tellurium solutions, can solve the problems of low recovery rates of selenium and tellurium

Active Publication Date: 2015-09-16
YUNNAN COPPER CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In view of the above deficiencies in the prior art, the object of the present invention is to provide a method for separating and extracting selenium and tellurium from a high-selenium and low-tellurium solution, aiming to solve the problem of low selenium and tellurium recovery in the prior art selenium-tellurium extraction method

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  • A method for separating and extracting selenium and tellurium from a high selenium and low tellurium solution

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Embodiment 1

[0029] When a copper smelter is processing a batch of copper anode slime, a batch of 10m in volume is obtained after copper removal and chlorination 3 The high-selenium and low-tellurium solution contains 28g / L selenium, 1.9g / L tellurium, 8g / L copper, 15g / L chloride ion concentration, and trace amounts of gold and silver. The process of separating and extracting selenium and tellurium with the high-selenium and low-tellurium solution in the present invention is adopted, and the two-stage reduction process is adopted for process control. In the first stage of reduction, the initial solution is reduced by using the reducing agent liquid sulfur dioxide. When the sulfuric acid concentration is 260g / L, the reaction is 2.5h. After the plate and frame pressure filtration, crude selenium and filtrate are produced (the reduced liquid ). The first-stage reduction liquid contains 0.3g / L of selenium and 1.75g / L of tellurium. The selenium content in crude selenium is 82% and the content of ...

Embodiment 2

[0031] When a copper smelter is processing a batch of copper anode slime, a batch of 12m in volume is obtained after copper removal and chlorination. 3 The high selenium and low tellurium solution contains 26.5g / L selenium, 1.78g / L tellurium, 7g / L copper, 10g / L chloride ion concentration, and trace amounts of gold and silver. The process of separating and extracting selenium and tellurium with the high-selenium and low-tellurium solution in the present invention is adopted, and the two-stage reduction process is adopted for process control. In the first stage of reduction, the initial solution is reduced by using a reducing agent, liquid sulfur dioxide. When the sulfuric acid concentration is 250g / L, the reaction is carried out for 2h, and after the plate and frame pressure filtration, crude selenium and filtrate are produced (one stage of reduced liquid) . The first-stage reduction liquid contains 0.3g / L of selenium and 1.65g / L of tellurium. The selenium content in crude selen...

Embodiment 3

[0033] When a copper smelter is processing a batch of copper anode slime, a batch of 13m in volume is obtained after copper removal and chlorination 3 The high-selenium and low-tellurium solution contains 27.6g / L of selenium, 1.82g / L of tellurium, 7.6g / L of copper, 20g / L of chloride ion, and trace amounts of gold and silver. The process of separating and extracting selenium and tellurium with the high-selenium and low-tellurium solution in the present invention is adopted, and the two-stage reduction process is adopted for process control. In the first stage of reduction, the initial solution is reduced by using the reducing agent liquid sulfur dioxide. When the sulfuric acid concentration is 280g / L, the reaction is carried out for 3 hours, and the plate and frame press filter produces crude selenium and filtrate (a stage of reduced liquid) . The first-stage reduction liquid contains 0.3g / L selenium and 1.73g / L tellurium. The crude selenium contains 80% selenium and 1.3% tellur...

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Abstract

The invention discloses a selenium and tellurium separation and extraction method for a high-selenium low-tellurium solution. According to the method, the high-selenium low-tellurium solution is subjected to reduction in two steps, wherein first-stage reduction is carried out in a first step, sulfur dioxide is added into an initial solution with the chloride ion concentration of 10-20 g / L so as to carry out reduction on selenium in the solution, the sulfuric acid concentration of the solution is controlled in the range of 250-280 g / L, and filtration and separation are carried out after the reduction is carried out for a period of time so as to produce crude selenium and a first-stage reduced solution; and second-stage reduction is carried out in a second step, the chloride ion concentration of the first-stage reduced solution is increased to 60-80 g / L, sulfur dioxide is adopted as a reducing agent, the sulfuric acid concentration of the first-stage reduced solution is controlled to be 280-320 g / L, and filtration and separation are carried out after the reduction is carried out for a period of time so as to produce a selenium-tellurium mixture and a second-stage reduced solution.

Description

Technical field [0001] The invention relates to the technical field of selenium and tellurium extraction, in particular to a method for separating and extracting selenium and tellurium from a high-selenium and low-tellurium solution. Background technique [0002] The selenium and tellurium in the copper concentrate are enriched in the copper refining electrolytic anode slime during the copper smelting process. In the combined treatment process of copper anode slime beneficiation and smelting, after the copper anode slime is chlorinated, some rare metals such as selenium, tellurium, etc. It is separated from precious metals and concentrated in the chlorinated solution, which contains 15-25g / L selenium and 1-3g / L tellurium. The chlorination solution uses sulfur dioxide to reduce the solution to produce crude selenium (75%-85% selenium). The reduced solution contains 0.5-1g / L selenium and about 1-2g / L tellurium. At present, there is no mature process to effectively recover the resi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B19/02
Inventor 徐养良沙梅王鹏程蒋惠祥姚伟东孙绪杰代峰献胡一平
Owner YUNNAN COPPER CO LTD
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