Clean and efficient method for recycling arsenic, copper, lead, antimony and silver from copper-containing smelting slag
A technology for copper smelting slag and copper smelting, which is used in the field of silver, clean and efficient recovery of arsenic, copper, antimony and lead, can solve the problem of high energy consumption and cost of three wastes discharge and treatment, complicated process flow of iron salt method, and easy introduction of other impurities, etc. It can eliminate the arsenic pollution problem, realize the utilization of resources, and achieve the effect of fast reaction process.
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Embodiment 1
[0034] 1. Crushing the copper-containing smelting slag, then finely grinding the crushed copper-containing smelting slag to a fineness of -0.074 mm and accounting for more than 90%, passing through a 200-mesh sieve to obtain copper-containing slag powder.
[0035] 2. Put the copper-containing slag powder and the alkaline solution of sodium hydroxide with a concentration of 30g / L into the autoclave at a liquid-to-solid ratio of 5:1, and inject oxygen with a pressure of 0.8MP into the autoclave. , Stirring speed is 400rpm, pH is 7 under the conditions of pressurized oxidation alkali leaching reaction for 1.5h, after the reaction is completed, the slurry is filtered out of the kettle to obtain leaching residue containing copper, lead, antimony and silver and arsenic-containing leaching solution.
[0036] 3. Pass the arsenic-containing leaching solution with arsenic ion concentration of 35g / L through the tank with a pressure of 3.0V and a current density of 150A / m 2Alkaline system...
Embodiment 2
[0040] 1. Crushing the copper-containing smelting slag, then finely grinding the crushed copper-containing smelting slag to a fineness of -0.074mm and accounting for more than 90%, passing through a 200-mesh sieve to obtain copper-containing slag powder.
[0041] 2. Put copper-containing slag powder and sodium hydroxide alkaline solution with a concentration of 50g / L into the autoclave at a liquid-to-solid ratio of 4:1, and inject oxygen with a pressure of 0.6MP into the autoclave. , Stirring speed is 400rpm, pH is 8 under the conditions of pressurized oxidation alkali leaching reaction for 1.8h, after the reaction is completed, the slurry is filtered out of the kettle to obtain leaching residue containing copper, lead, antimony and silver and arsenic-containing leaching solution.
[0042] 3. Pass the arsenic-containing leaching solution with arsenic ion concentration of 32g / L through the tank with a pressure of 2.8V and a current density of 200A / m 2 Alkaline system swirling e...
Embodiment 3
[0046] 1. Crushing the copper-containing smelting slag, then finely grinding the crushed copper-containing smelting slag to a fineness of -0.074 mm and accounting for more than 90%, passing through a 200-mesh sieve to obtain copper-containing slag powder.
[0047] 2. Put the copper-containing slag powder and the sodium hydroxide alkaline solution with a concentration of 150g / L into the autoclave at a liquid-solid ratio of 6:1. , Stirring speed is 300rpm, PH is 10 under the conditions of pressurized oxidation alkali leaching reaction for 1.0h, after the reaction is completed, the slurry is filtered out of the kettle to obtain leaching residue containing copper, lead, antimony and silver and arsenic-containing leaching solution.
[0048] 3. Pass the arsenic-containing leaching solution with arsenic ion concentration of 35g / L through the tank with a pressure of 3.1V and a current density of 220A / m 2 Alkaline system swirling electrowinning, so that metal arsenic ions are deposited...
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