A method for comprehensive utilization of arsenic-containing smoke and dust and precipitation conversion method to synthesize arsenic-fixed minerals
A technology of precipitation transformation and arsenic fume, which is applied in the field of metallurgy, can solve the problems of low recovery rate of valuable metals, limited market for arsenic products, untreated sodium arsenate, etc. The effect of low content
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Embodiment 1
[0044] Taking arsenic-containing soot from a lead-zinc smelter in China as an example, the main components of the raw material are Pb 1.57%, As 48.56%, Sn 0.51%, Sb 21.24%, Zn 0.73%, Te 0.35%, Se 0.25%, and the following steps are used for processing :
[0045] (1) Oxygen pressure water immersion: Weigh a certain quality of high arsenic and antimony fumes into the reactor, the control conditions are liquid-solid volume mass ratio 10:1, stirring speed 300r / min, leaching temperature 160°C, oxygen partial pressure 2Mpa, The leaching time is 2 hours. After the leaching is completed, remove the slurry and filter and separate to obtain the leaching solution and leaching residue;
[0046] After testing: the leaching rate of arsenic is 64.53%, the concentration of each element in the leach solution is 709.60ppm Pb, 31.02ppm Se, 1.26g / L Sb, 123.28ppm Te, and 29.88g / L As.
[0047] (2) Fix arsenic in the leach solution: adjust the pH value of the leach solution to 1.5, add calcium oxide...
Embodiment 2
[0055] Taking arsenic-containing soot from a lead-zinc smelter in China as an example, the main components of the raw material are Pb 6.88%, As 36.51%, Sn 1.11%, Sb 29.77%, Zn 0.54%, Te 0.24%, Se 0.05%, and the following steps are used for processing :
[0056] (1) Oxygen pressure water immersion: Weigh a certain quality of high arsenic and antimony fumes into the reactor, the control conditions are liquid-solid volume mass ratio 20:1, stirring speed 300r / min, leaching temperature 160°C, oxygen partial pressure 0.5Mpa , the leaching time is 2h, after the leaching is finished, remove the slurry and filter and separate to obtain the leachate and leach residue;
[0057] After testing: the arsenic leaching rate is 51.29%, and the concentration of each element in the leach solution is 515.20ppm Pb, 31.56ppm Se, 0.88g / L Sb, 122.26ppm Te, and 9.36g / L As.
[0058] (2) Fixing arsenic in the leach solution: adjust the pH value of the leach solution to 2, add calcium oxide to the leach ...
Embodiment 3
[0066] Taking arsenic-containing soot from a lead-zinc smelter in China as an example, the main components of the raw material are Pb 5.46%, As 30.29%, Sn0.98%, Sb 29.58%, Zn 0.68%, Te 0.26%, Se 0.07%, and the following steps are used for processing :
[0067] (1) Oxygen pressure water immersion: Weigh a certain quality of high arsenic and antimony fume in the reaction kettle, the control conditions are liquid-solid volume mass ratio 10:1, stirring speed 300r / min, leaching temperature 200℃, oxygen partial pressure 2.5Mpa , the leaching time is 4h, after the leaching is finished, remove the slurry, filter and separate, and obtain the leaching solution and leaching residue;
[0068] After testing: the arsenic leaching rate is 64.52%, and the concentration of each element in the leach solution is Pb 956.35ppm, Se 18.91ppm, Sb 0.93g / L, Te 144.92ppm, As 19.54g / L.
[0069] (2) Arsenic fixation in the leach solution: adjust the pH value of the leach solution to 3, add calcium oxide ...
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