Method for recycling valuable metal from copper smelting white smoke
A valuable metal, white smoke technology, applied in the direction of improving process efficiency, can solve problems such as insufficient utilization, environmental pollution, large amount of fossil fuel or power consumption
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Embodiment 1
[0032] Such as figure 1 Shown: (1) Main components of white soot ash and primary power wave cycle waste acid are shown in Tables 1 and 2;
[0033] Table 1 Main components of white soot
[0034]
[0035] Table 2 Main components of waste acid in primary power wave cycle
[0036]
[0037] (2) Take 40 tons of primary power wave circulating waste acid and pump it into the leaching tank, then add 5 tons of white smoke and dust, stir and leaching for 30 minutes at room temperature, filter, wash the filter cake with 1.5 tons of zinc-precipitating liquid and incorporate it into the filtrate , after analysis, copper, zinc, arsenic content are respectively in the filtrate: 2.7g / L, 21.5g / L, 13.3g / L; The filter cake weight of dry basis is 1120kg, and lead content is 43.6wt%, and lead recovery rate is greater than 95.5%, the dissolution rates of copper, zinc and arsenic are 92.6%, 97.5% and 95.5% respectively;
[0038] (3) Take 40m of pickling solution 3 According to 0.8 times the...
Embodiment 2
[0042] (1) The main components of white soot and ash and primary power wave cycle waste acid are shown in Tables 3 and 4;
[0043] Table 3 Main components of white soot
[0044]
[0045] Table 4 Main components of waste acid in primary power wave cycle
[0046]
[0047] (2) Take 40 tons of primary power wave circulating waste acid and pump it into the leaching tank, then add 5 tons of white smoke and dust, stir and leaching for 30 minutes at room temperature, filter, wash the filter cake with 1.5 tons of zinc-precipitating liquid and incorporate it into the filtrate , after analysis, copper, zinc, arsenic content are respectively in the filtrate: 2.9g / L, 23.3g / L, 13.2g / L; The dry basis filter cake quality is 1265kg, and lead content is 40.2wt%, and lead recovery rate is greater than 95.7%, the dissolution rates of copper, zinc and arsenic are 92.8%, 98.6% and 95.1% respectively;
[0048] (3) Take 40m3 of acid leaching solution, add 1.0 times the theoretical amount requ...
Embodiment 3
[0052] (1) The main components of white soot and ash and primary power wave cycle waste acid are shown in Tables 5 and 6;
[0053] Table 5 Main components of white soot
[0054]
[0055] Table 6 Main components of waste acid in primary power wave cycle
[0056]
[0057] (2) Take 40 tons of primary power wave circulating waste acid and pump it into the leaching tank, then add 4 tons of white smoke ash, stir and leaching for 30 minutes at room temperature, filter, wash the filter cake with 1.5 tons of zinc-precipitating liquid and incorporate it into the filtrate , after analysis, copper, zinc, arsenic content are respectively in the filtrate: 2.3g / L, 18.6g / L, 11.5g / L; The filter cake weight of dry basis is 811kg, and lead content is 48.2wt%, and lead recovery rate is greater than 95.5%, the dissolution rates of copper, zinc and arsenic are 92.6%, 97.5% and 95.5% respectively;
[0058] (3) Get 40m3 of pickling solution, add 182kg of solid sodium sulfide with an effective...
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