A method of comprehensively recovering rhenium and copper from copper smelting waste acid
A technology for copper smelting and rhenium-rich slag, which is applied in the field of targeted rhenium sinking copper-rhenium-rich slag high-pressure leaching-leaching rhenium-rich solution to prepare potassium perrhenate by sinking rhenium, which can solve the complex process, low recovery rate, and processing time. Long-term problems, to achieve the effect of increasing the precipitation rate, reducing the dosage, and increasing the reaction rate
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Embodiment 1
[0032] In this embodiment, the copper smelting waste acid sulfuric acid concentration is 73.48g / L, the rhenium concentration is 17.94mg / L, the arsenic concentration is 7.58g / L, and the copper concentration is 58.38mg / L. The treatment process and effects are as follows:
[0033] (1) Targeted sinking of rhenium: the waste acid from copper smelting is filtered to remove lead and then pumped to the rhenium-copper precipitation tank. 3 Add 20L of 20% sodium thiosulfate and 20g of sodium sulfide to the waste acid, heat it with steam to 70°C, and stir for 5 minutes; the obtained rhenium-rich slag consists of 2.45% rhenium, 32.22% arsenic, and 8.30% copper; the precipitation rate of rhenium is 99.7%, The arsenic precipitation rate is only 2.78%, and the copper precipitation rate is 99.9%.
[0034] (2) Hot-pressed oxidation leaching of rhenium: The rhenium-rich slag obtained in step (1) was subjected to pressurized oxygen leaching, the leaching conditions were: liquid-solid ratio 6, le...
Embodiment 2
[0039] In this example, the sulfuric acid concentration of copper smelting waste acid is 73.48g / L, the rhenium concentration is 17.94mg / L, the arsenic concentration is 7.58g / L, and the copper concentration is 58.38mg / L. The treatment process and effect are as follows: (1) Targeted rhenium sinking : Pump the waste acid after filtering and removing lead to the rhenium-copper precipitation tank, and use a metering pump at a rate of 1m 3 Add 25L of 20% sodium thiosulfate and 10g of sodium sulfide to the waste acid, heat to 65°C with steam, and stir for 15 minutes. The composition of the obtained rhenium-rich slag is 2.49% rhenium, 25.14% arsenic and 8.42% copper. The precipitation rate of rhenium is 99.7%, that of arsenic is only 2.15%, and that of copper is 99.2%. (2) Hot-pressed oxidation leaching of rhenium: The rhenium-rich slag obtained in step (1) is subjected to pressurized oxygen leaching, the leaching conditions are: liquid-solid ratio 8:1, leaching temperature 130°C, ox...
Embodiment 3
[0043] In this example, the sulfuric acid concentration of copper smelting waste acid is 73.48g / L, the rhenium concentration is 17.94mg / L, the arsenic concentration is 7.58g / L, and the copper concentration is 58.38mg / L. The treatment process and effect are as follows: (1) Targeted rhenium sinking : Pump the waste acid after filtering and removing lead to the rhenium-copper precipitation tank, and use a metering pump at a rate of 1m 3 Add 10L of 20% sodium thiosulfate and 15g of sodium sulfide to the waste acid, heat to 50°C with steam, and stir for 15 minutes. The composition of the obtained rhenium-rich slag is 3.16% rhenium, 30.36% arsenic and 9.66% copper. The precipitation rate of rhenium was 91.5%, that of arsenic was only 1.76%, and that of copper was 88.4%. (2) Hot-pressed oxidation leaching of rhenium: The rhenium-rich slag obtained in step (1) is subjected to pressurized oxygen leaching, the leaching conditions are: liquid-solid ratio 4:1, leaching temperature 150°C,...
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