A method for multi-cycle selective leaching of copper, zinc and nickel in copper smelting wastewater sludge
A technology for wastewater sludge and copper smelting, which is applied in the direction of improving process efficiency, can solve the problems of small concentration difference, low valence metal concentration, and inability to directly enter conventional electrolysis, etc., and achieves the effect of simple method and good promotion prospects.
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Embodiment 1
[0022] The copper smelting sludge sample 1 was selectively leached by the method of the present invention, and the types and contents of metals in the sample 1 are shown in Table 1. process such as figure 1 As shown, the specific steps are as follows:
[0023] (1) Take 20g of copper smelting wastewater sludge sample 1 and place it in a leaching container, add 160mL of sulfuric acid with a concentration of 0.06g / mL, stir and mix with the sludge through an agitator, monitor the pH value of the leachate during the leaching process, and make The temperature is maintained at 5.4, and the leaching operation lasts for 2 hours; after the leaching is completed, the solid-liquid separation is carried out, and the leaching solution containing zinc and nickel is collected;
[0024] (2) Put the leaching residue from step (1) in the leaching container, take 160mL of sulfuric acid with a concentration of 0.12g / mL and stir and mix the leaching residue, monitor the pH of the leaching solution...
Embodiment 2
[0033] The copper smelting sludge sample 2 was selectively leached by the method of the present invention, and the types and contents of metals in the sample 2 are shown in Table 2.
[0034] process such as figure 1 As shown, the specific steps are as follows:
[0035] (1) Take 40g of copper smelting wastewater sludge sample 2 and place it in the leaching container, add 240mL of sulfuric acid with a concentration of 0.05g / mL, stir and mix with the sludge through an agitator, monitor the pH value of the leachate during the leaching process, and make The temperature is maintained at 5.6, and the leaching operation lasts for 2 hours; after the leaching is completed, the solid and liquid are separated, and the leaching solution containing zinc and nickel is collected;
[0036](2) Put the leaching residue of step (1) in the leaching container, take 240mL of sulfuric acid with a concentration of 0.14g / mL and stir and mix the leaching residue, monitor the pH of the leaching solution...
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