Technology for extracting zinc, lead and silver step by step by processing zinc-leached residues by full wet process
A technology of zinc leaching slag and full wet method, which is applied in the field of zinc leaching slag recovery, can solve the problems of secondary pollution, unfavorable recovery of other metals, high content of iron and silicon dioxide, and achieve mild and loose reaction conditions, low cost, and easy extraction high rate effect
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Embodiment 1
[0043] Add 750g of zinc leaching slag into the normal pressure reactor, in which the zinc content is 9.36wt.%, the lead content is 4.75wt.%, and the silver content is 239g / t. 2800g of 15wt.% sulfuric acid solution, heated to 90°C, reacted for 4 hours, the stirring rate was 400rpm, the obtained slurry was easy to separate, and the separated filter cake was weighed as 465g, containing 20wt of water .%, put it into a normal pressure reactor, add 1488g of 30wt.% sulfuric acid, heat up to 80°C, react for 3 hours, the stirring speed is 400rpm, the slurry obtained is easy to filter and separate, and the filter cake (lead-silver slag ) was washed 2 times; it weighed 297.6 g. A leaching filtrate 3095ml, add 30% H to it 2 o 269ml was oxidized for 0.5h, and 178.34g of quicklime was added to remove iron for 2.5h, and 615g of iron slag was obtained by filtration, 2727ml of filtrate, and 130.46g of sodium sulfide was added to the filtrate to obtain 42.99g of zinc sulfide concentrate. Put...
Embodiment 2
[0045] Add 500g of zinc leaching slag into the normal pressure reactor, in which the zinc content is 5.94wt.%, the lead content is 5.91wt.%, and the silver content is 196g / t. 2000g of 15wt.% sulfuric acid solution, heated to 90°C, reacted for 4 hours, the stirring rate was 400rpm, the obtained slurry was easy to separate, and the separated filter cake did not need to be washed and dried, and it was weighed as 367g, which contained 18wt of water .%, put it into a normal pressure reactor, add 1200g of 20wt.% sulfuric acid, heat up to 80°C, react for 3 hours, and the stirring speed is 400rpm. The obtained slurry is easy to filter and separate, and the separated filter cake (lead-silver residue ) was washed 2 times; it was weighed to 241 g. Add 30% H to the filtrate 2 o 2 38.17ml was oxidized for 0.5h, and 98.57g of quicklime was added to remove iron for 2.5h, and 135.84g of iron slag was obtained by filtration. After removing iron, the filtrate was 2002.1ml, and the filtrate w...
Embodiment 3
[0047] Add 500g of zinc leaching slag into the normal pressure reactor, in which the zinc content is 5.94wt.%, the lead content is 5.91wt.%, and the silver content is 196g / t. 1500g of 15wt.% sulfuric acid solution, heated to 90°C, reacted for 3 hours, the stirring rate was 400rpm, the obtained slurry was easy to separate, and the separated filter cake did not need to be washed and dried. It was weighed as 352g, which contained 19wt of water .%, put it into a normal pressure reactor, add 1200g of 15wt.% sulfuric acid, heat up to 80°C, react for 3 hours, the stirring speed is 400rpm, the slurry obtained is easy to filter and separate, and the filter cake (lead-silver slag ) washed 2 times; it weighed 232g. Add 30% H to the filtrate 2 o 2 38.17ml was oxidized for 0.5h, and 98.57g of quicklime was added to remove iron for 2.5h, and 133g of iron slag was obtained by filtration. After iron removal, 2010.13ml of filtrate was added, and 130.46g of sodium sulfide was added to the fi...
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