Method for efficiently separating copper arsenic in arsenic matte
An arsenic matte, high-efficiency technology, applied in the field of efficient separation of copper and arsenic from arsenic matte, can solve the problems of high operating cost, low metal recovery rate, long process flow, etc., and achieve high recovery rate of valuable metals, good copper and arsenic The effect of separation and short process flow
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Embodiment 1
[0049] Arsenic matte (Cu 49.22wt%, As 15.83wt%, Fe 1.75wt%, S 0.6wt%, Pb 15.69wt%, Sb 6.05wt%, Ag 3071g / t) was crushed, ground and passed through a 100-mesh sieve. Take 150g arsenic matte powder with sulfuric acid solution and Cu 2+ Ions are added to the reaction kettle, the concentration of sulfuric acid solution is 150g / L, the temperature is set at 130°C, the liquid-solid ratio is 6:1 (mL / g), the oxygen partial pressure is 0.8MPa, Cu 2+ The amount of ions added is 2g / L, and the reaction time is 4h. After the leaching reaction is completed, liquid-solid separation is carried out to obtain a copper sulfate leaching solution. Non-ferrous metals such as lead and silver are stored in the leaching slag, and the leaching slag is returned to the fire method system to recover lead and silver and other metals. Precipitate copper and arsenic with caustic soda on the copper sulfate leaching solution, adjust pH to 4.5, leaching copper and arsenic slag with alkali, 20g / L sodium hydroxide...
Embodiment 2
[0052] Arsenic matte (Cu 45.22wt%, As 10.91wt%, Fe 5.24wt%, S 3.41wt%, Pb 15.66wt%, Sb 4.77wt%, Ag 2854g / t) was crushed, pulverized, and passed through a 100-mesh sieve. Take 150g arsenic matte powder with sulfuric acid solution and Cu 2+ Ions were added to the reaction kettle, the concentration of sulfuric acid solution was 100g / L, the temperature was set at 150°C, the liquid-solid ratio was 8:1 (mL / g), the oxygen partial pressure was 0.8MPa, Cu 2+ The amount of ions added is 5g / L, and the reaction time is 4h. After the leaching reaction is completed, liquid-solid separation is carried out to obtain a copper sulfate leaching solution. Non-ferrous metals such as lead and silver are stored in the leaching slag, and the leaching slag is returned to the fire method system to recover lead and silver and other metals. Precipitate copper and arsenic with caustic soda on the leaching liquid, adjust pH to 4.5, leaching copper and arsenic slag with alkali, 30g / L sodium hydroxide solut...
Embodiment 3
[0055] Arsenic matte (Cu 42.52wt%, As 13.76wt%, Fe 5.09wt%, S 4.14wt%, Pb 10.44wt%, Sb 5.87wt%, Ag 4154g / t) was crushed, pulverized, and passed through a 100-mesh sieve. Take 150g arsenic matte powder with sulfuric acid solution and Cu 2+ Ions are added to the reactor, the concentration of sulfuric acid solution is 80g / L, the temperature is set at 180°C, the liquid-solid ratio is 10:1 (mL / g), the oxygen partial pressure is 1.2MPa, Cu 2+ The amount of ions added is 8g / L, and the reaction time is 4h. After the leaching reaction is finished, liquid-solid separation is carried out to obtain a copper sulfate leaching solution. Non-ferrous metals such as lead and silver exist in the leaching slag, and the leaching slag is returned to the fire system to recover metals such as lead and silver. 4.5~5.0, alkaline leaching of copper arsenic slag, 40g / L sodium hydroxide solution, liquid-solid ratio 5:1 (mL / g), stirring in 80°C water bath for 2h, liquid-solid separation, solution containi...
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