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Lead zinc ore dressing wastewater treatment device and treatment method

A technology of beneficiation wastewater and treatment device, applied in biological treatment device, water/sewage treatment, water treatment parameter control, etc., can solve the problems of poor treatment effect and high cost of lead-zinc beneficiation wastewater

Active Publication Date: 2018-06-29
湖南中金岭南康盟环保科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The invention provides a lead-zinc beneficiation wastewater treatment device and treatment method to solve the technical problems of high cost and poor treatment effect of lead-zinc beneficiation wastewater

Method used

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  • Lead zinc ore dressing wastewater treatment device and treatment method
  • Lead zinc ore dressing wastewater treatment device and treatment method
  • Lead zinc ore dressing wastewater treatment device and treatment method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0073] Introduce the lead-zinc ore dressing wastewater into the pretreatment reaction tank, stir at 100r / min, and expose CO 2 , the aeration rate is 0.3g / L wastewater, the aperture of the aerator is 1 μm, the aeration time is 1min, and the pH is adjusted to 9.5; after standing for 3h, the clear liquid enters the aerobic biological reaction tank 200.

[0074] Aerobic biological treatment reactor sludge load is 0.5kg COD Cr / (kg MLSS·d), air aeration adopts 8 groups Microporous aerator, service area 0.16m 2 / piece, its oxygen utilization rate is 20%; the aerobic biological reaction tank 200 stays for 10-12h, the biochemical index of the reactor is the same as that of the acclimation period, half of the water after biological treatment enters the ion exchange device for desalination after secondary precipitation .

[0075] The ion exchange device is filled with anion exchange resin, the resin volume is 80L, and the residence time is 30min. The biochemical effluent is rinsed ...

Embodiment 2

[0077] The pretreatment and biological treatment steps are the same as in Example 1. 90% of the biologically treated wastewater enters the ion exchange device for desalination, and the effluent from the ion exchange column is mixed with the remaining 10% biochemically treated effluent and used as mineral processing water.

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Abstract

The invention discloses a lead zinc ore dressing wastewater treatment device and a lead zinc ore dressing wastewater treatment method. The lead zinc ore dressing wastewater treatment device comprisesa pretreatment tank for adjusting the pH value of lead zinc ore dressing wastewater so as to remove heavy metal ions through sedimentation and an aerobic bioreaction tank for reducing the COD value ofeffluent water of the pretreatment tank, wherein the aerobic bioreaction tank comprises an aeration zone and a precipitation zone which are communicated with each other; the aeration zone is communicated with the pretreatment tank, and is provided with aerobic biological sludge suspending in the lead zinc ore dressing wastewater through an aerating mechanism; the aerobic bioreaction tank furthercomprises a sulfate removing mechanism communicated with the precipitation zone and used for reducing the sulfate concentration of effluent water of the pretreatment zone. The lead zinc ore dressing wastewater treatment device is creatively provided with the sulfate removing mechanism on the basis of removal of the heavy metal ions from the lead zinc ore dressing wastewater and reduction in the COD value of the lead zinc ore dressing wastewater, so that the water quality of the effluent water meets requirements on water for ore processing.

Description

technical field [0001] The invention relates to the field of mineral processing wastewater reuse, in particular to a lead-zinc mineral processing wastewater treatment device. In addition, the present invention also relates to a treatment method comprising the above-mentioned lead-zinc mineral processing wastewater. Background technique [0002] The flotation process of non-ferrous metal ores is accompanied by a large amount of beneficiation wastewater, with an annual discharge of 1.2-1.5 billion tons, accounting for about 30% of the non-ferrous metal industrial wastewater. This wastewater contains a large amount of heavy metal ions and organic pollutants such as xanthate, phenylene terpene, ethyl disulfide nitrogen, and sodium humate. The composition is complex, the toxicity is strong, and the concentration is high, which seriously affects the environment of the mining area. Therefore, the treatment and reuse of mineral processing wastewater is of great significance to solv...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14
CPCC02F1/441C02F1/58C02F1/62C02F3/1215C02F9/00C02F2001/422C02F2203/006C02F2209/06C02F2209/08C02F2209/19
Inventor 周康根余承红狄国勋伍敬峰文剑杨有才吴班高峰陈伟军
Owner 湖南中金岭南康盟环保科技有限公司