Method for producing electrolytic lead powder through alkali immersion rotational flow electrolysis of wet electrolytic zinc acid dipping residues
A technology for electrolysis of zinc acid leaching residue and cyclone electrolysis, applied in the field of smelting, can solve the problems of low recovery rate, poor operating conditions, and high energy consumption of zinc leaching residue, and achieve high leaching rate, low labor intensity and high market value. Effect
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[0033] Example 1: See Table 1 for the chemical composition of acid leaching slag produced in a typical wet electrolytic zinc production.
[0034] Table 1 Chemical composition of acid leaching residue produced in wet electrolytic zinc production / %
[0035] Zn Cu Pb sn Fe Ni As Sb 4.7 0.23 30.5 14.1 0.23 0.06 1.96 0.77
[0036] ① Leaching
[0037] According to the liquid-solid mass ratio of the sodium hydroxide aqueous solution leaching agent and the acid leaching residue produced in the wet electrolytic zinc production of 5:1, the free alkali in the leaching agent is 150~250 g / L, and the reaction is carried out at a temperature of 100 °C for 4 h. The free alkali at the end of the leaching reaction is 150 g / L, and after liquid-solid separation, a clarified leachate and tin-containing leach residue are obtained;
[0038] ② purification
[0039] In the clarified leaching solution described in ①, add lead powder of 6 times the amount of ...
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