Copper mine raffinate treatment method
A treatment method and raffinate technology, which is applied in the field of copper mine raffinate treatment, can solve the problems of underutilization of valuable resources, lack of comprehensive recycling methods, secondary pollution, etc., and achieve maximum improvement Maximize utilization, be conducive to sustainable and healthy development, and reduce the effect of stockpiling
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Embodiment 1
[0022] A gold-copper mine in Longyan, Fujian Province adopts bio-pile leaching copper process. After the copper product is extracted and recovered, the raffinate pH is 2.5, the copper content is 1.2g / L, the arsenic is 0.8g / L, the lead is 0.17g / L, and the ferric iron is 2.8 g / L, ferrous iron 9.7g / L.
[0023] (1) Add 3.2 g of fresh reduced iron powder (active iron powder) to 1000 mL of the above raffinate to recover copper. The particle size of the added fresh reduced iron powder is 0.1-1.0 mm. The specific recovery process is two-stage closed-circuit countercurrent reduction process, fresh reduced iron powder is added from the outlet of the second stage, and the underflow copper-containing iron powder slag after the reaction is returned to the first stage for further replacement reaction. The reaction residence time of the whole process is controlled at 0.5-1.0h. After the reaction is completed The obtained underflow slag adopts the magnetic separation process to separate the c...
Embodiment 2
[0028] After extraction and recovery of copper products from a large copper mine in Jiangxi, the raffinate has a pH of 2.0-2.5, copper content of 1.6g / L, arsenic of 1.2g / L, cadmium of 0.1g / L, arsenic of 1.85g / L, ferric iron of 5.8 g / L, ferrous iron 16.3g / L.
[0029] Take 1000ml of the above-mentioned raffinate, add 5.2g of fresh reduced iron powder with a particle size of 0.1-1.0mm in two stages, filter after controlling the residence time of the whole reaction at 0.5-1.0h, and recycle the iron in the filter residue; Then add 0.25 g of sodium hydrosulfide to the waste liquid after copper recovery, control the pH of the reaction to 2.5 to 3.0, and filter after 0.5 h of reaction; add 10 to 15 g / L of sodium hydroxide to the above-mentioned treated liquid to control the pH to 7 ~8, 50~100m3 / L under the condition of aeration, the temperature is 40~50℃, and the reaction time is 1.0~1.5h. After the reaction is over, increase the aeration intensity to 100-200m3 / L, the temperature is ...
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