发明名称 |
EFFICIENT COMBINED ADVANCED TREATMENT METHOD OF ELECTROPLATING WASTE WATER |
摘要 |
An efficient combined advanced treatment method of electroplating wastewater is disclosed, which belongs to the technical field of electroplating wastewater treatment. The method includes: after pretreatments including cyanide breaking, dechromisation and coagulating sedimentation, introducing the electroplating wastewater to a contact oxidation tank for biochemical treatment, and settling the effluent from the contact oxidation tank down in an inclined pipe of a secondary sedimentation tank to realize the separation of the sludge from water; charging the effluent to a coagulating sedimentation tank, and undergoing coagulating sedimentation with the aid of a flocculant and a coagulant aid added; feeding the effluent, as an influent, to a resin adsorption tank for adsorption with a magnetic resin; and after passing through a filter, flowing the effluent after adsorption to a fixed bed resin adsorption unit, so as to realize the discharge up to standard and recycle of the effluent. |
申请公布号 |
US2015291449(A1) |
申请公布日期 |
2015.10.15 |
申请号 |
US201314412218 |
申请日期 |
2013.03.27 |
申请人 |
Nanjing University ;Nanjing University Yancheng Environmental Protection Tech. & Engineering Research Institute |
发明人 |
LI Aimin;FU Lichun;LIU Fuqiang;ZHOU Qing;DAI Jianjun;LU Zhaoyang;LI Yan;SHUANG Chendong;WANG Jinnan;ZHAO Weiwei |
分类号 |
C02F1/461 |
主分类号 |
C02F1/461 |
代理机构 |
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代理人 |
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主权项 |
1. An efficient combined advanced treatment method of electroplating wastewater, comprising:
(1) bio-contact oxidation: after subjecting the electroplating wastewater to pretreatments including cyanide breaking, dechromisation and coagulating sedimentation, introducing the effluent, as an influent, to a contact oxidation tank for biochemical treatment, and settling the effluent from the contact oxidation tank down in an inclined pipe of a secondary sedimentation tank to realize the separation of sludge from water, wherein after pretreatments, the quality indexes of the effluent are: the concentrations of the heavy metals Cu2+ and Ni2+: below 2.0 mg/L, the concentration of cyanide: below 2.0 mg/L, and COD: 80 to 200 mg/L; (2) coagulating sedimentation: charging the effluent from the step (1) to a coagulating sedimentation tank, and undergoing coagulating sedimentation with the aid of a flocculant and a coagulant aid added, to further remove the suspended solids, and the heavy metals Cu2+ and Ni2+ in the effluent after biochemical treatment; (3) magnetic resin adsorption: feeding the effluent from the step (2), as an influent, to a resin adsorption tank for adsorption with a magnetic resin; and (4) fixed bed resin adsorption: after passing through a filter, flowing the effluent from the step (3) to a fixed bed resin adsorption unit, to realize discharge up to standard or recycle of the effluent. |
地址 |
Nanjing, Jiangsu CN |