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
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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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