Method for increasing leaching rate of zinc and indium in secondary zinc oxide
A technology for secondary zinc oxide and leaching rate, which is applied in the field of improving the leaching rate of zinc and indium in secondary zinc oxide, can solve the problems of large acid mist, high energy consumption, low degree of automation, etc., so as to reduce the initial acid concentration of sulfuric acid and improve the reaction temperature, the effect of improving treatment efficiency
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Embodiment 1
[0041] (1) Neutral leaching: Mix secondary zinc oxide with zinc electrolytic waste solution containing sulfuric acid at a concentration of 15g / L for leaching reaction, wherein the temperature of the leaching reaction is 70°C, the leaching time is 2h, and the end point pH of the leaching reaction is The value is 5.0; the middle immersion liquid and the underflow are obtained through solid-liquid separation, and the obtained middle immersion liquid is sent to the zinc smelting system to recover zinc, and the obtained underflow enters the step (2) process;
[0042] (2) Low-acid leaching: Mix the underflow obtained in step (1) with the oxygen pressure acid leaching solution at a solid-to-liquid ratio of 1:4g / mL for leaching reaction, wherein the temperature of the leaching reaction is 80°C, and the leaching time is 4h , the final acid concentration of leaching is 20g / L. The low-acid leaching residue and low-acid leaching solution are obtained through solid-liquid separation, and t...
Embodiment 2
[0046] (1) Neutral leaching: Mix secondary zinc oxide with zinc electrolytic waste solution containing sulfuric acid at a concentration of 20g / L for leaching reaction. The temperature of the leaching reaction is 75°C and the leaching time is 2.5h. The end point of the leaching reaction The pH value is 5.1; the middle immersion liquid and the underflow are obtained through solid-liquid separation, and the obtained middle immersion liquid is sent to the zinc smelting system to recover zinc, and the obtained underflow enters the process of step (2);
[0047] (2) Low-acid leaching: Mix the underflow obtained in step (1) with the oxygen pressure acid leaching solution at a solid-to-liquid ratio of 1:6g / mL for leaching reaction, wherein the temperature of the leaching reaction is 85°C, and the leaching time is 4h , the final acid concentration of leaching is 25g / L. The low-acid leaching residue and low-acid leaching solution are obtained through solid-liquid separation, and the obta...
Embodiment 3
[0051] (1) Neutral leaching: Mix secondary zinc oxide with zinc electrolytic waste solution containing sulfuric acid at a concentration of 25g / L for leaching reaction, wherein the temperature of the leaching reaction is 80°C, the leaching time is 3h, and the end point pH of the leaching reaction is The value is 5.2; the middle immersion liquid and the underflow are obtained through solid-liquid separation, and the obtained middle immersion liquid is sent to the zinc smelting system to recover zinc, and the obtained underflow enters the step (2) process;
[0052] (2) Low-acid leaching: Mix the underflow obtained in step (1) with the oxygen pressure acid leaching solution at a solid-to-liquid ratio of 1:8g / mL for leaching reaction, wherein the temperature of the leaching reaction is 90°C, and the leaching time is 4h , the final acid concentration of leaching is 30g / L. The low-acid leaching residue and low-acid leaching solution are obtained through solid-liquid separation, and t...
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