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Method for separating arsenic and selenium from copper anode slime alkaline leach liquor

A copper anode slime and leaching solution technology, applied in the field of separation of arsenic and selenium, can solve the problems of sulfur dioxide pollution, long process, and large acid consumption, and achieve good separation effect, short process flow and simple operation

Active Publication Date: 2015-09-16
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the separation methods of arsenic in alkaline solution mainly include crystallization precipitation method and acidification precipitation method. Among them, the crystallization precipitation method uses the solubility difference of arsenate at different temperatures to separate arsenic, and can only deal with high-concentration arsenic-containing solutions. The precipitation method is to acidify the solution and then oxidize it, and then add reagents such as iron salts to form insoluble arsenate. The process is long and the reaction process requires a lot of acid
The separation method of selenium in alkaline solution is mainly the reduction method, that is, using sulfur dioxide, sodium sulfite and other reducing agents to reduce selenium to elemental selenium in a strong acid system and recover it. The main problem is that the acid consumption and waste water are large, and there is low concentration of sulfur dioxide pollution.
At the same time, the above-mentioned separation methods for arsenic and selenium are generally only aimed at a single alkaline solution containing arsenic or selenium, without considering the separation and enrichment of arsenic and selenium and the recovery of alkali

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  • Method for separating arsenic and selenium from copper anode slime alkaline leach liquor

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Effect test

Embodiment 1

[0030] A method for separating arsenic and selenium from copper anode slime alkaline leaching solution of the present invention, its technological process is as follows figure 1 shown, including the following steps:

[0031] 1) Oxidation: take 1L of alkaline leaching solution (As: 2g / L, Se: 2g / L, OH - : 0.5mol / L), ozone was introduced at a stirring speed of 200r / min and the temperature was kept at 25°C until the potential of the copper anode slime alkaline leaching solution tended to be stable, and the oxidized copper anode slime alkaline leaching solution was obtained.

[0032] 2) Precipitation of arsenic: Add calcium hydroxide (the molar ratio of calcium hydroxide to arsenic in the alkaline leaching solution is 3) to the oxidized copper anode slime alkaline leaching solution, stir at a stirring speed of 200r / min for 1h, and filter Finally, calcium arsenate precipitate and arsenic solution are obtained. After testing, the arsenic concentration in the liquid after arsenic pr...

Embodiment 2

[0035] A method for separating arsenic and selenium from copper anode slime alkaline leaching solution of the present invention, its technological process is as follows figure 1 shown, including the following steps:

[0036] 1) Oxidation: Take 1L of alkaline leaching solution (As: 10g / L, Se: 15g / L, OH - : 1mol / L), ozone was introduced at a stirring speed of 300r / min and the temperature was kept at 40°C until the potential of the copper anode slime alkaline leaching solution tended to be stable, and the oxidized copper anode slime alkaline leaching solution was obtained.

[0037] 2) Precipitation of arsenic: Add calcium hydroxide (the molar ratio of calcium hydroxide to arsenic element in the alkaline leaching solution is 6) to the oxidized copper anode slime alkaline leaching solution, stir at a stirring speed of 300r / min for 3 hours, and filter Finally, calcium arsenate precipitate and arsenic solution are obtained. After testing, the arsenic concentration in the solution a...

Embodiment 3

[0040] A method for separating arsenic and selenium from copper anode slime alkaline leaching solution of the present invention, its technological process is as follows figure 1 shown, including the following steps:

[0041]1) Oxidation: Take 1L of alkaline leaching solution (As: 25g / L, Se: 20g / L, OH - : 3mol / L), ozone was introduced at a stirring speed of 500r / min and the temperature was maintained at 60°C until the potential of the copper anode slime alkaline leaching solution became stable, and the oxidized copper anode slime alkaline leaching solution was obtained.

[0042] 2) Precipitation of arsenic: Add calcium hydroxide (the molar ratio of calcium hydroxide to arsenic in the alkaline leaching solution is 9) to the oxidized copper anode slime alkaline leaching solution, and stir at a stirring speed of 500r / min for 6h, filter Finally, calcium arsenate precipitate and arsenic solution are obtained. After testing, the concentration of arsenic in the solution after arseni...

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Abstract

The invention discloses a method for separating arsenic and selenium from copper anode slime alkaline leach liquor. The method comprises the following steps: 1) oxidation, namely adding an oxidizing agent or introducing oxidizing gas into the copper anode slime alkaline leach liquor, so that oxidized copper anode slime alkaline leach liquor is obtained; 2) arsenic precipitation, namely adding a calcium salt into the oxidized copper anode slime alkaline leach liquor, stirring the obtained mixture so as to produce a precipitate, and carrying out filtration and separation on the precipitate so as to obtain a calcium arsenate precipitate and arsenic post-precipitation liquid; and 3) selenium precipitation, namely adding a barium salt into the arsenic post-precipitation liquid obtained in the step 2), stirring the obtained mixture so as to produce a precipitate, carrying out filtration and separation on the precipitate so as to obtain a barium selenate precipitate and selenium post-precipitation liquid, and carrying out evaporative crystallization on the selenium post-precipitation liquid so as to recycle alkali, or directly returning to a leaching process. The method disclosed by the invention is short in technological process, less in equipment and simple in operation, and can be used for realizing the separation and enrichment of arsenic and selenium, the precipitation rate of arsenic is higher than 96%, and the precipitation rate of selenium is higher than 99%; by virtue of carrying out evaporative crystallization on a solution for recycling or directly returning the solution to a leaching process, the recovery of alkali is realized.

Description

technical field [0001] The invention relates to a method for separating arsenic and selenium, in particular to a method for separating arsenic and selenium from copper anode slime alkaline leaching solution. Background technique [0002] Copper anode slime is a type of intermediate product produced in the copper electrolytic refining process that contains valence elements such as copper, lead, antimony, selenium, tellurium and noble metals, as well as harmful element arsenic. After the copper anode slime is treated by alkaline metallurgical processes such as soda roasting leaching, alkaline smelting leaching, and pressurized alkaline leaching, arsenic and selenium are separated from heavy and precious metals and enriched in the alkaline leaching solution. [0003] At present, the separation methods of arsenic in alkaline solution mainly include crystallization precipitation method and acidification precipitation method. Among them, the crystallization precipitation method us...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B30/04C01B19/02
CPCY02P10/20
Inventor 李栋郭学益田庆华
Owner CENT SOUTH UNIV
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