Method for extracting and recovering copper and selenium from copper anode sludge by microwave treatment
A copper anode slime and microwave treatment technology, which is applied in the field of hydrometallurgy, can solve the problems that the reaction temperature cannot be very high (the maximum temperature does not exceed 90 °C, the reaction intensity is weak, the reaction speed is slow, etc., and the surface hardening and unevenness are avoided. , the effect of increasing the leaching speed and reducing the leaching time
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Embodiment 1
[0033] (1) Add water to the copper anode slime for coarse slurry adjustment, sieve out sand impurities with a particle diameter greater than 5mm, drain the water, and add sulfuric acid with a concentration of 500g / L to the drained copper anode slime for slurry adjustment , control the weight concentration of copper anode slime in the copper anode slime slurry at 30%;
[0034] (2) Put the obtained copper anode slurry in a microwave oven, and add oxidant H to the copper anode slurry 2 o 2 , adjust microwave frequency to 1500MHz, microwave heating power to 120w, leaching reaction under normal pressure for 10min, copper in copper anode slime is replaced by CuSO 4 Form leaching, selenium as H 2 SeO 3 、SeSO 3 and other forms of leaching.
[0035] h 2 o 2 The dosage is 2.5molH 2 o 2 / L slurry.
[0036] After leaching, the leaching rate of copper was analyzed to be 93.5%, and the leaching rate of selenium was 75.5%.
Embodiment 2
[0038] (1) Add water to the copper anode slime for coarse slurry adjustment, sieve out sand impurities with a particle diameter greater than 5mm, drain the water, and add sulfuric acid with a concentration of 20g / L to the drained copper anode slime for slurry adjustment , control the weight concentration of copper anode slime in the copper anode slime slurry at 1%;
[0039] (2) Put the obtained copper anode slurry in a microwave oven, and add oxidant H to the copper anode slurry 2 o 2 , adjust microwave frequency to 2450MHz, microwave heating power to 460w, leaching reaction under normal pressure for 3min, copper in copper anode slime is dissolved in CuSO 4 Form leaching, selenium as H 2 SeO 3 、SeSO 3 and other forms of leaching.
[0040] h 2 o 2 The dosage is 5molH 2 o 2 / L slurry.
[0041] After leaching, the leaching rate of copper was analyzed to be 98.6%, and the leaching rate of selenium was 84.5%.
Embodiment 3
[0043] (1) Add water to the copper anode slime for coarse slurry adjustment, sieve out sand impurities with a particle diameter greater than 5mm, drain the water, and add sulfuric acid with a concentration of 200g / L to the drained copper anode slime for slurry adjustment , control the weight concentration of copper anode slime in the copper anode slime slurry at 15%;
[0044] (2) Put the obtained copper anode slurry in a microwave oven, and add oxidant H to the copper anode slurry 2 o 2 , adjust microwave frequency to 1500MHz, microwave heating power to 280w, leaching reaction under normal pressure for 5min, copper in copper anode slime is replaced by CuSO 4 Form leaching, selenium as H 2 SeO 3 、SeSO 3 and other forms of leaching.
[0045] h 2 o 2 The dosage is 0.05molH 2 o 2 / L slurry.
[0046] After leaching, the leaching rate of copper was analyzed to be 99.1%, and the leaching rate of selenium was 90.4%.
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