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Method using wet method to treat high-fluorine and high-chlorine copper smelting dust containing zinc

A wet processing, high fluorine technology, applied in the field of heavy metal metallurgy, can solve the problems of limited removal of fluorine and chlorine, difficult recovery, increased labor costs and production costs, etc., achieving significant economic and social benefits, eliminating high COD, The effect of cost-effective treatment

Active Publication Date: 2018-03-09
CHENZHOU FENGYUE ENVIRONMENTAL PROTECTION TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At the same time, when the concentration of fluoride and chloride ions in the electrolyte is too high, it will also increase labor costs and production costs. For example, too high fluoride ions will cause corrosion of the cathode plate, making it difficult to manually strip the plate, and will indirectly lead to increased loss of the cathode plate. Excessive chloride ion content will seriously corrode the anode plate, resulting in a sharp increase in production costs, so controlling the concentration of fluoride and chloride ions in the zinc electrolyte is also very important
Recently, due to the good situation of the zinc market, the supply of high-quality materials containing zinc is in short supply. Therefore, it is imminent to develop a new technology to deal with zinc materials with high impurities.
Copper soot is a good zinc secondary material, but often this soot often contains high levels of impurity metals such as fluorine and chlorine, which makes it difficult to recover valuable metals in this material
Therefore, on the basis of referring to the process of removing zinc oxide, fluorine and chlorine by wet alkali washing, the copper soot is pretreated by alkali washing process, but the effect of removing fluorine and chlorine is limited.

Method used

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  • Method using wet method to treat high-fluorine and high-chlorine copper smelting dust containing zinc
  • Method using wet method to treat high-fluorine and high-chlorine copper smelting dust containing zinc
  • Method using wet method to treat high-fluorine and high-chlorine copper smelting dust containing zinc

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Take copper soot (Cu: 2.65wt%, Zn: 23.62wt%, F: 2.26wt%, Cl: 8.55wt%) and pour 8t into 50m 3 In the reaction tank, add 40m of river water3 , heat the reaction tank with steam to 75°C and stir the reaction, take 200L hydrogen peroxide and slowly add it to the solution, the addition time is controlled to 1.5h, add caustic soda during the reaction process, control the pH of the reaction end point to 9, and the reaction time is 2h, After the reaction, liquid-solid separation is carried out, the liquid enters the sewage station for treatment, and the slag is poured into another reaction tank for alkali secondary washing.

[0033] Pass 40m into the reaction tank equipped with alkali-washing slag 3 River water, heat the reaction tank with steam to 75°C and stir the reaction, add the additive sodium carbonate during the reaction, control the pH of the reaction end point to 9, and the reaction time is 2h. A part is taken for laboratory analysis, and the slag after alkali second...

Embodiment 2

[0045] Take copper soot (Cu: 2.65%, Zn: 23.62%, F: 2.26%, Cl: 8.55%) and pour 8t into 50m 3 In the reaction tank, add alkali two washing liquid 40m in example 1 3 , heat the reaction tank with steam to 75°C and stir the reaction, take 200L hydrogen peroxide and slowly add it to the solution, the addition time is controlled to 1.5h, add caustic soda during the reaction process, control the pH of the reaction end point to 10, and the reaction time is 2h, After the reaction, liquid-solid separation is carried out, the liquid enters the sewage station for treatment, and the slag is poured into another reaction tank for alkali secondary washing.

[0046] Pass 40m into the reaction tank equipped with alkali-washing slag 3 River water, heat the reaction tank with steam to 75°C and stir the reaction, add the additive sodium carbonate during the reaction, control the pH of the reaction end point to 10, and the reaction time is 2h. A part is taken for laboratory analysis, and the slag...

Embodiment 3

[0058] Take copper soot (Cu: 3.21%, Zn: 29.96%, F: 1.96%, Cl: 5.23%) 8t and pour it into 50m 3 In the reaction tank, add 40m of river water 3 , heat the reaction tank with steam to 80°C and stir the reaction, take 250L hydrogen peroxide and slowly add it to the solution, the adding time is controlled to 1.5h, add caustic soda during the reaction, control the pH of the reaction end point to 8, and the reaction time is 2h, After the reaction, liquid-solid separation is carried out, the liquid enters the sewage station for treatment, and the slag is poured into another reaction tank for alkali secondary washing.

[0059] Pass 40m into the reaction tank equipped with alkali-washing slag 3 River water, heat the reaction tank with steam to 80°C and stir the reaction, add additive sodium carbonate during the reaction, control the pH of the reaction end point to 8, and the reaction time is 2h. A part is taken for laboratory analysis, and the slag after alkali secondary washing is ca...

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Abstract

The invention a method using a wet method to treat high-fluorine and high-chlorine copper smelting dust containing zinc. The method includes: the copper smelting dust is subjected to alkali washing twice to remove fluorine and chlorine impurity elements in the copper smelting dust, the alkali washing residues of the copper smelting dust are subjected to neutralizing to leach valuable metal such aszinc and copper in the copper smelting dust, the solution after the neutralizing is subjected to copper precipitation and chlorine removing, the solution after the chlorine removing is subjected to goethite-method jarosite precipitation twice to remove impurity ions such as iron, arsenic, antimony, fluorine and chlorine in the solution and lower the COD of the solution, the solution after the jarosite precipitation enters a thickening tank for subsequent purification, and the purified solution finally enters a zinc electrowinning system; neutralizing residues are subjected to medium-acid leaching once and high-acid leaching once and then enter a lead pyrometallurgy system. The method has the advantages that the valuable metal such as the zinc and the copper is recycled effectively, and the fluorine and chlorine removing effects are above 90%; efficient and low-cost effective treatment of the high-fluorine and high-chlorine copper smelting dust is achieved, and the influence of high COD caused by the high-fluorine and high-chlorine copper smelting dust on zinc electrowinning is eliminated at the same time.

Description

technical field [0001] The invention relates to a method for wet treatment of high-fluorine and chlorine-containing zinc-copper soot, which is a new process for wet leaching, separation, enrichment and recovery of valuable metals such as zinc and copper, and belongs to the field of heavy metal metallurgy. Background technique [0002] In the zinc hydrometallurgy process, excessive impurity elements such as cobalt, nickel, arsenic, and antimony in the electrolyte have a relatively large impact on the zinc electrowinning system, and often cause accidents such as electrowinning plates, so the concentration of impurity elements needs to be strictly controlled. At the same time, when the concentration of fluoride and chloride ions in the electrolyte is too high, it will also increase labor costs and production costs. For example, too high fluoride ions will cause corrosion of the cathode plate, making it difficult to manually strip the plate, and will indirectly lead to increased ...

Claims

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Application Information

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IPC IPC(8): C22B7/02C22B15/00C22B19/30
CPCC22B7/006C22B7/02C22B15/0065C22B15/0089C22B19/30Y02P10/20
Inventor 段良洪廖谨鹏刘伟高海明王敏杰廖召军
Owner CHENZHOU FENGYUE ENVIRONMENTAL PROTECTION TECH
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