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Integral electroplating waste water treatment equipment and process

A technology for electroplating wastewater and treatment equipment, which is applied in the fields of metallurgical wastewater treatment, water/sewage multi-stage treatment, neutralization water/sewage treatment, etc. , to achieve the effect of low operating cost, strong adaptability and convenient operation

Inactive Publication Date: 2012-02-01
VISBE XIAMEN ENVIRONMENT TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, at present, most electroplating factories have multiple electroplating varieties at the same time, and there is no separation and separation of electroplating wastewater, resulting in the mixed discharge of various electroplating wastewater, which brings certain difficulties to the treatment of wastewater
And for the same electroplating factory, the daily variation of water quality is also large, and the amount of dosing is not easy to control. If the amount of dosing is insufficient, the treatment will not meet the standard, and if the amount of dosing is too much, the treatment cost will increase.

Method used

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  • Integral electroplating waste water treatment equipment and process
  • Integral electroplating waste water treatment equipment and process
  • Integral electroplating waste water treatment equipment and process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] 1) Use hydrochloric acid to adjust the pH in the decontamination tank to 3.0, and add bleaching powder under stirring conditions, and react for 30 minutes. The added bleaching powder is calculated as 0.7kg / ton of electroplating wastewater;

[0030] 2) The waste water after the bleaching powder breaks the network flows into the ferrous sulfide packed bed for reaction;

[0031] 3) The effluent from the ferrous sulfide packed bed enters the coagulation tank, and alkali is added to the coagulation tank to adjust the pH to 8.0, and 200 g / ton of electroplating wastewater PAC coagulant is added, and the reaction is stirred for 7 minutes;

[0032] 4) Add 200ml / ton of electroplating wastewater into the flocculation tank, with a mass fraction of 0.5% PAM flocculant. Stir slowly for 2 minutes and enter the sedimentation tank. After flocculation and sedimentation, the produced water enters the clear water tank. The experimental results are shown in Table 1.

[0033] Table 1: Exper...

Embodiment 2

[0037] 1) Use hydrochloric acid to adjust the pH in the network-breaking tank to 2.5, and add bleaching powder under stirring conditions, and react for 20 minutes. The added bleaching powder is calculated as 1.0 kg / ton of electroplating wastewater;

[0038] 2) The waste water after the bleaching powder breaks the network flows into the ferrous sulfide packed bed for reaction;

[0039] 3) The effluent from the ferrous sulfide packed bed enters the coagulation tank, and alkali is added to the coagulation tank to adjust the pH to 8.5, and 50 g / ton of electroplating wastewater PAC coagulant is added, and the reaction is stirred for 10 minutes;

[0040] 4) Add 500ml / ton of electroplating wastewater into the flocculation tank, with a mass fraction of 0.75% PAM flocculant. Stir slowly for 1 min; enter the sedimentation tank, after flocculation and sedimentation, the produced water enters the clear water tank, and the experimental results are shown in Table 2.

[0041] Table 2: Exper...

Embodiment 3

[0045] 1) Use hydrochloric acid to adjust the pH in the pool to 3.5, and add bleaching powder under stirring conditions, and react for 30 minutes. The added bleaching powder is calculated as 0.7kg / ton of electroplating wastewater.

[0046] 2) The waste water after the bleaching powder breaks the network flows into the ferrous sulfide packed bed to react.

[0047] 3) The effluent from the ferrous sulfide packed bed enters the coagulation tank, and alkali is added to the coagulation tank to adjust the pH to 7.5, and 500 g / ton of electroplating wastewater PAC coagulant is added, and the reaction is stirred for 5 minutes;

[0048] 4) Add 100ml / ton of electroplating wastewater into the flocculation tank, with a mass fraction of 1.0% PAM flocculant. Stir slowly for 2 minutes and enter the sedimentation tank. After flocculation and sedimentation, the produced water enters the clear water tank. The experimental results are shown in Table 3.

[0049] Table 3: Experimental Results

[...

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Abstract

The invention discloses integral electroplating waste water treatment equipment, which comprises an integral electroplating waste water pool, a decomplexing pool, a coagulating pool, a flocculating pool, a precipitating pool and a clean water pool in sequential connection and is characterized in that a ferrous sulfide filling material bed is also arranged between the decomplexing pool and the coagulating pool, a water inlet of the ferrous sulfide filling material bed is positioned under the ferrous sulfide filling material bed, and a water outlet of the ferrous sulfide filling material bed is positioned above the ferrous sulfide filling material bed. The invention also discloses an integral electroplating waste water treatment process, which is characterized in that ferrous sulfide is used as slow release filling materials, in addition, the decomplexed electroplating waste water is in sufficient contact with the ferrous sulfide for reaction, hexavalent chromium is reduced to trivalent chromium, and in addition, the trivalent chromium forms stable sulfide precipitates with heavy metals beyond the hexavalent chromium. The integral electroplating waste water treatment equipment and the process are used for the integral electroplating waste water treatment and have the advantages that the operation is convenient, the control is easy, the operation cost is low, the raw materials are easy to obtain, the continuous reagent feeding is not needed, stronger adaptability is realized on the waste water ingredients, the concentration and the water quality, and the like.

Description

technical field [0001] The invention relates to the field of electroplating wastewater treatment, in particular to a comprehensive electroplating wastewater treatment equipment and process. Background technique [0002] In the electroplating industry, commonly used plating types include galvanized, copper-plated, chrome-plated, galvanized, cadmium-plated, etc. The sources of waste water are quite extensive, generally: (1) plating parts cleaning waste water, (2) electroplating waste water, (3) other waste water: including washing the floor of the workshop, scrubbing the floor and ventilation equipment condensate and due to the leakage or operation of the plating tank Various bath liquids and drainage caused by improper management; (4) equipment condensate: equipment condensate is generally not polluted by heavy metals except for cooling during use. Among them, the cleaning wastewater of plating parts is the main source of electroplating wastewater, accounting for more than 8...

Claims

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Application Information

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IPC IPC(8): C02F9/04C02F1/66C02F1/52C02F103/16
Inventor 宋晓铭任以伟王俊川
Owner VISBE XIAMEN ENVIRONMENT TECH CO LTD
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