Method for recovering tellurium in copper anode slime through normal-pressure closed oxygenation
A technology of copper anode slime and copper recovery, applied in chemical instruments and methods, selenium/tellurium compounds, inorganic chemistry, etc., can solve the problems of harsh leaching conditions, excessive consumption of oxygen and alkali, and large pollution, and achieve industrialized recovery , Realize recycling and reduce production costs
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Embodiment 1
[0025] The composition of copper anode slime contains 0.4% Te, 3.5% Ag and 12.6% Cu by weight percentage.
[0026] (1) Add a mixed acid of dilute sulfuric acid and dilute nitric acid to the copper anode slime to adjust the slurry, control the weight volume ratio of the copper anode slime in the slurry to 20g / mL, the concentration of dilute sulfuric acid in the mixed acid is 0.5mol / L, and the concentration of dilute nitric acid 0.03mol / L;
[0027] (2) Put the adjusted slurry in a closed container, start stirring, pass in oxygen to remove the air in it, the leaching temperature is 110°C, the stirring speed is 400r / min, and the solid-liquid separation is carried out after leaching under normal pressure for 0.5h to obtain Tellurium-containing leachate.
[0028] The analysis results show that the leaching rate of tellurium is 98.7%. Under the same conditions, without adding nitric acid, the leaching rate of tellurium is 15.3%.
Embodiment 2
[0030] The composition of copper anode slime contains 1.2% Te, 3.1% Ag and 11.5% Cu by weight percentage.
[0031] (1) Add a mixed acid of dilute sulfuric acid and dilute nitric acid to the copper anode slime to adjust the slurry, control the weight volume ratio of the copper anode slime in the slurry to 15g / mL, the concentration of dilute sulfuric acid in the mixed acid is 2mol / L, and the concentration of dilute nitric acid is 0.1mol / L;
[0032] (2) Put the adjusted slurry in a closed container, start the stirring, pass in oxygen to remove the air in it, the leaching temperature is 100°C, the stirring speed is 500r / min, and the solid-liquid separation is carried out after leaching under normal pressure for 1.5h to obtain Tellurium-containing leachate.
[0033] The analysis results show that the leaching rate of tellurium is 97.6%. Under the same conditions, without adding nitric acid, the leaching rate of tellurium is 18.4%.
Embodiment 3
[0035] The composition of copper anode slime contains 0.6% Te, 5.4% Ag and 13.7% Cu by weight percentage.
[0036] (1) Add the mixed acid of dilute sulfuric acid and dilute nitric acid to the copper anode slime to adjust the slurry, control the weight volume ratio of copper anode slime in the slurry to 15g / mL, the concentration of dilute sulfuric acid in the mixed acid is 1.5mol / L, and the concentration of dilute nitric acid 0.06mol / L;
[0037] (2) Put the adjusted slurry in a closed container, start stirring, pass in oxygen to remove the air in it, the leaching temperature is 115°C, the stirring speed is 400r / min, and the solid-liquid separation is carried out after leaching under normal pressure for 1 hour to obtain the Tellurium leaching solution.
[0038] The analysis results show that the leaching rate of tellurium is 99.8%. Under the same conditions, without adding nitric acid, the leaching rate of tellurium is 16.8%.
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