Micro-electrolysis flocculation method for treating acid waste water containing heavy metals in mine
A technology for acid wastewater and heavy metals, applied in mining wastewater treatment, chemical instruments and methods, water/sewage multi-stage treatment, etc.
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Embodiment 1
[0029] A mine wastewater has a copper ion concentration of 81.5mg / L and trace amounts of other heavy metals, and a pH of 4.5. Pass the waste water through pre-precipitation and pass it into the iron-carbon fixed bed with built-in cast iron chips and activated carbon ratio of 1:1 to treat the waste water. After 30 minutes of treatment, the treatment process will not be aerated; The pH of the effluent is 7.1, which can meet the reuse or discharge standard, and the metal recovery rate reaches 99.6%.
Embodiment 2
[0031] The mining wastewater of a mine has a concentration of 92.2mg / L of lead ions, 25.5mg / L of zinc ions and trace amounts of other heavy metals, pH 3.0. After pre-sedimentation and pre-aeration, the wastewater is passed into the iron-carbon aeration bed. The aeration bed is built with 2.5:1 iron-carbon, and the iron is a combination of sponge iron and steel at a ratio of 1:1. The combination of coal ash, the ratio is 1:1, the aeration rate is 1m 3 Gas / m 3 Water.min, stay for 2h; adjust pH to 7.2 after effluent, after solid-liquid separation, effluent lead ion concentration 0.55mg / L, zinc ion concentration 1.33mg / L, pH 7.8, effluent can meet reuse or discharge standard, metal The recovery rate is 99.9%.
[0032] The iron scraps selected by the present invention can be cast iron scraps, and can also be any one of sponge iron, steel, and iron-based alloy scraps containing iron weight percentage ≥ 70%, or their multiple combinations; the activated carbon used can also be It ...
Embodiment 3
[0034] A certain mine wastewater has ion concentrations of lead 63.5mg / L, cobalt 13.5mg / L, nickel 16.3mg / L, and trace amounts of other heavy metals, pH 1.0. Adjust the pH of the waste water to 2.0, and pass it into the iron-carbon fluidized bed after pre-sedimentation and pre-aeration treatment. The fluidized bed is built with 4:1 iron-carbon, a combination of cast iron scraps for iron, sponge iron and steel, and the ratio is 2:1:1, the carbon is a combination of coke, coal and calcium carbide slag, the ratio is 3:1:1, stay for 3 hours, aerate after effluent, the aeration rate is 2m 3 Gas / m 3 Water.min; adjust pH to 8.0 after effluent, and add inorganic flocculant polyaluminium chloride (PAC) 10mg / L, solid-liquid separation, effluent lead ion concentration 0.53mg / L, cobalt ion concentration 0.15mg / L, nickel ion concentration The concentration is 0.21mg / L, the pH is 8.5, the effluent can meet the reuse or discharge standard, and the metal recovery rate can reach 99.9%.
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