Black copper sludge recycling and harmless processing method
A treatment method and technology of black copper mud, applied in the improvement of process efficiency, instruments, optics, etc., can solve the problems of small market demand for copper arsenate, poor labor environment, and high production cost, and achieve arsenic open circuit and harmless. Treatment, low risk of environmental pollution, reduced scale and cost effectiveness
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Embodiment 1
[0046] The main element content of the black copper mud sample: Cu 55.6%, As 33.7%, Bi 1.0%, Sb 1.3%, Pb 1.6%.
[0047] (1) Pressurized oxidation leaching, according to the liquid-to-solid ratio of 10, mix the black copper mud with 80g / L sulfuric acid solution into the autoclave, control the reaction temperature at 120°C, oxygen partial pressure 0.5MPa, reaction time 2h; reaction After the completion of solid-liquid separation, the leaching liquid and leaching residue are obtained, and the leaching residue is returned to the smelting system;
[0048] (2) Extraction-electrowinning, the leachate contains Cu 6.7g / L, As 15g / L, and the pH value is 1.9. The leachate diluted with backwater is extracted with the organic phase synthesized by 10% ZJ988+90% kerosene. O / A=2, time 5min, wash the loaded organic phase with 3g / L sulfuric acid solution to obtain the washed loaded organic phase and raffinate, the washed loaded organic phase is subjected to back extraction-electrodeposition to obtain...
Embodiment 2
[0054] The main element content of the black copper mud sample: Cu 55.6%, As 33.7%, Bi 1.0%, Sb 1.3%, Pb 1.6%.
[0055] (1) Hot acid oxidation leaching, according to the liquid-solid ratio of 20, mix the black copper mud with 50g / L sulfuric acid solution, control the reaction temperature of 80℃, and fill in air during the reaction and press 1.5t / t Black copper mud Add 30% concentration of H 2 O 2 , The reaction time is 6h; solid-liquid separation is performed after the reaction is completed to obtain the leachate and the leach slag, and the leach slag is returned to the smelting system;
[0056] (2) Extraction-electrowinning, the leachate contains Cu 9.3g / L, As 10.6g / L, pH value 1.7, dilute the leachate with backwater, and the leachate diluted with backwater is combined with 25% LIX984+75% kerosene. Phase extraction, control phase ratio O / A=4, time 10min for extraction, and then wash the loaded organic phase with 5g / L sulfuric acid solution to obtain the loaded organic phase and ra...
Embodiment 3
[0062] The main element content of the black copper mud sample: Cu 36.2%, As 34.2%, Bi 1.5%, Sb 1.5%, Pb 2.0%.
[0063] (1) Pressurized oxidation leaching, according to the liquid-solid ratio of 6, mix the black copper mud with 140g / L sulfuric acid solution and put it into the autoclave, control the reaction temperature of 150℃, oxygen partial pressure of 0.3MPa, and reaction time of 3h; After completion, solid-liquid separation is carried out, the leaching residue is returned to the smelting system, and the leaching liquid is diluted and enters the extraction system;
[0064] (2) Extraction-electrowinning, first dilute the leachate (Cu 3.8g / L, As 23g / L, pH value 2.1) with backwater, add 15% ZJ988 + 85% kerosene organic phase for extraction, compared to O / A=1.2, extraction is performed for 5 min, and then the loaded organic phase is washed with 5g / L sulfuric acid solution, and the washed loaded organic phase is subjected to back extraction-electrodeposition to obtain the electrode...
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