Combined long-term stable operation ammonium chloride method zinc electrolysis process flow
A technology with a process flow and stable operation, applied in the electrolysis process, photography process, electrolysis components, etc., can solve the problems of incomplete system, unsuitable equipment, large consumption of zinc powder, etc.
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example 1
[0022] Example 1. Direct leaching of raw materials
[0023] The raw material is secondary zinc oxide, containing 41% zinc, 4% lead, and 4% fluorine and chlorine. The raw material is sent to the leaching tank after a screw feeder or pulping at a speed of 4.5 tons / hour, and is subjected to countercurrent washing and leaching. The leaching liquid-solid ratio is 8-12:1, the leaching liquid contains ammonium chloride 4.5-5.5mol / l, the temperature is 30-90 degrees, stirred, the leaching time is 2 hours, the leaching liquid contains more than 37g / l of zinc, 3.6g / l of lead, and others Copper 0.05g / l, cadmium 0.3g / l, iron trace;
example 2
[0024] Example 2, leaching after rough washing of ultra-impurity raw materials
[0025] Small ash: 61% zinc, 5% iron, 15.5% fluorine and chlorine, sent to coarse cycle washing and pressure filtration, 62.2% zinc, 5.4% iron, less than 6% fluorine and chlorine, sent to leaching;
example 3
[0026] Example 3. Combined purification of leaching solution
[0027] Leaching solution: zinc 37g / l, lead 5g / l, trace iron, other copper 0.05, cadmium 0.3, two-stage coarse purification of zinc scum, one-stage deep purification of zinc powder, one-stage mixed liquid supplementation of ammonia and then purified liquid, Zinc 38g / l, lead 0.008, copper 0.003, cadmium 0.006, other trace amounts.
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