Mine acid wastewater utilization and deep purification method
A technology for deep purification of mine acid wastewater, applied in chemical instruments and methods, zinc sulfate, multi-stage water treatment, etc., can solve problems such as being unsuitable for high-concentration acid wastewater treatment, poor metal ion tolerance, and low treatment efficiency. , to achieve the effect of simple facilities, reduced environmental risks, and efficient enrichment
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Embodiment 1
[0030] The sample was taken from the raffinate wastewater of a gold and copper mine smelting company, with an acidity of 0.33mol / L, a copper ion content of 85mg / L, a zinc ion content of 204mg / L, and a total iron ion content of 8.6g / L. Follow the steps below:
[0031] 1) Use a neutralizer to adjust the pH value of the acidic mine wastewater to 2.2, and then separate the solid and liquid to obtain gypsum;
[0032] 2) Use a neutralizer to adjust the pH value of the acidic mine wastewater to 3.2, remove iron ions, and recover iron slag;
[0033] 3) adding a vulcanizing agent to the solution after iron removal to obtain copper-zinc slag;
[0034] 4) Copper-zinc slag is separated to obtain copper-rich slag and zinc sulfate solution after acid leaching, and reclaims vulcanizing agent;
[0035] 5) Advanced treatment of the final effluent.
[0036] The neutralizing agent of steps 1) and 2) is calcium carbonate.
[0037] In step 3), the molar ratio of vulcanizing agent sodium sulfid...
Embodiment 2
[0042] The sample was taken from the raffinate wastewater B / D of a gold and copper mine smelting company, with an acidity of 0.41mol / L, a copper ion content of 584mg / L, a zinc ion content of 216mg / L, and a total iron ion content of 8.3g / L. Follow the steps below:
[0043] 1) Use a neutralizer to adjust the pH value of the mine acid wastewater to 2.4, and then separate the solid and liquid to obtain gypsum;
[0044] 2) Use a neutralizer to adjust the pH value of the mine acid wastewater to 3.0, remove iron ions, and recover iron slag;
[0045] 3) adding a vulcanizing agent to the solution after iron removal to obtain copper-zinc slag;
[0046] 4) Copper-zinc slag is separated to obtain copper-rich slag and zinc sulfate solution after acid leaching, and reclaims vulcanizing agent;
[0047] 5) Advanced treatment of the final effluent.
[0048] The neutralizing agent in step 1) and 2) is calcium carbonate, sodium carbonate, magnesium carbonate, calcium oxide, magnesium oxide. ...
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