Copper electrolyte adsorption, impurity removal and purification method

A technology for copper electrolyte and impurity adsorption, applied in copper electrolyte adsorption, decontamination purification, separation and recovery of bismuth, arsenic and antimony impurities in copper electrolyte, and can solve the problem of poor working environment, high energy consumption and inability to clean liquid. Completely replace the copper electrolyte purification process and other problems to achieve the effect of recycling

Active Publication Date: 2014-09-24
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] There are many defects in the traditional copper electrolyte purification process: high energy consumption, purification of 1m 3 The electrolyte consumes 100-120kwh of electricity and 0.8-1 ton of steam; the operating environment of the clean liquid is poor, producing a large amount of black copper sludge and black copper plates, and releasing harmful gas AsH 3 The direct recovery rate of copper electrolysis is low, and the black copper mud and black copper plate are returned to the fire method system to recover the copper, which causes the copper and impurities arsenic, antimony and bismuth to circulate in the smelting system.
However, these methods are only supplements to the traditional liquid purification process and cannot completely replace the traditional copper electrolyte purification process

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Take 5L of copper electrolytic refining electrolyte, add Sb according to the molar ratio of Sb(III) / As(V) 2:1 2 o 3 , and add hydrated Sb according to Sb(IV) / Sb(III) molar ratio 1:8 2 o 4, stirred at 85°C for 1.5h, cooled to 45°C and filtered. The filtrate is returned to the copper electrolyte circulation system; the filter residue is firstly stirred with water according to the solid-to-liquid ratio of 1:5g / ml, then added with NaOH to adjust the pH to 11.5, stirred at 85°C for 2 hours, and filtered to obtain the hydrated antimony oxide and arsenic-containing solution. Add sulfuric acid to the arsenic-containing solution to adjust the pH to 6.5, then add iron sulfate at 1.1 times the theoretical amount of ferric arsenate, stir at 55°C for 2 hours, and filter to obtain arsenic-enriched slag and arsenic-removed liquid. The arsenic-enriched slag is used for arsenic recovery; after arsenic removal, the liquid is cooled to crystallize sodium sulfate for later use. The tes...

Embodiment 2

[0028] Take 3L of copper electrolytic refining electrolyte, add Sb according to the molar ratio of (Sb(III)+Bi(III)) / As(V) 3.5:1 2 o 3 and Bi 2 o 3 A mixture of Sb in the mixture 2 o 3 with Bi 2 o 3 The molar ratio of Sb(V) / Sb(III) is 1:3, and the hydrated Sb is added according to the molar ratio of Sb(V) / Sb(III) 1:2 2 o 5 , stirred at 95°C for 1h, cooled to 50°C and filtered. The filtrate is returned to the copper electrolyte circulation system; the filter residue is first added with water and stirred at a solid-to-liquid ratio of 1:5g / ml, and then NaHCO is added 3 Adjust the pH to 9.5, stir at 75°C for 2 hours, and filter to obtain hydrated antimony and bismuth oxides and arsenic-containing solutions. Add magnesium sulfate to the arsenic-containing solution according to 1.2 times the theoretical amount of magnesium arsenate formed, stir at 75°C for 0.5h, and filter to obtain arsenic-enriched slag and arsenic-removed liquid. The arsenic-enriched slag is used for ars...

Embodiment 3

[0031] Take 3L of the solution after the electrowinning of copper electrolytic refining electrolyte to produce cathode copper, add the hydrated antimony oxide obtained in Example 1 according to the molar ratio of Sb(III) / As(V) of 1:1, stir at 65°C for 1h, filter . Return the filtrate to the copper electrolyte circulation system; add water to the filter residue according to the solid-to-liquid ratio of 1:6g / ml and stir, then add sodium carbonate to adjust the pH to 10.8, stir at 75°C for 3 hours, and filter to obtain hydrated antimony oxides and arsenic-containing solutions. Add barium carbonate to the arsenic-containing solution at twice the theoretical amount to form barium arsenate, stir at 85°C for 1 hour, and filter to obtain arsenic-enriched slag and arsenic-removed liquid. The test results before and after the copper electrolyte adsorption are as follows:

[0032]

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PUM

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Abstract

The invention discloses a copper electrolyte adsorption, impurity removal and purification method which is characterized by comprising the following steps: by taking oxides of antimony or / and bismuth and hydrates thereof as adsorbents, selectively adsorbing impurities As, Sb and Bi from copper electrolyte or from a solution in which cathode copper is produced through electrodeposition of the copper electrolyte or from a crystallizing mother solution obtained after copper sulfate is evaporated, concentrated and crystallized in the copper electrolyte. According to desorption of loaded adsorbents and regeneration of the analyzed solution, the adsorbents and analytical solution can be recycled, and the adsorbed impurities As, Sb and Bi can be recycled. The method has the advantages of simple process, simple and convenient operation, low production cost, good purification effect and the like, side effects on a main process are avoided, a traditional electrodeposition copper and impurity removal copper electrolyte purification process can be completely substituted, black copper sludge and black copper plate in the copper electrolyte purification process are completely eliminated, emission of harmful substances such as AsH3 is avoided, pollution is reduced, and the environment is protected.

Description

technical field [0001] The invention belongs to the field of hydrometallurgy, and in particular relates to a copper electrolyte adsorption, impurity removal and purification method, which is suitable for the separation and recovery of impurities arsenic, antimony and bismuth in the copper electrolyte. Background technique [0002] During the refining process of copper electrolysis, the impurities arsenic, antimony and bismuth are electrochemically dissolved together with the anode copper into the copper electrolyte. After the impurities arsenic, antimony and bismuth enter the copper electrolyte, As(III) and Sb(III) can be gradually dissolved in the air in the electrolyte (O 2 ) is oxidized to As(V) and Sb(V), but the oxidation rate of As(III) is much faster than that of Sb(III), so under normal circumstances, 90-95% of arsenic in copper electrolyte is It exists in the form of As(V), while more than 90% of antimony exists in the form of Sb(III). The valence state of bismuth...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C25C1/12C25C7/06
CPCY02P10/20
Inventor 王学文王明玉王兴明
Owner CENT SOUTH UNIV
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