Waste water treating device and method based on electrochemical principle

A wastewater treatment and electrochemical technology, applied in the field of environmental engineering, can solve the problems of increasing energy consumption, reducing treatment efficiency, and large electrode consumption, and achieve the effects of preventing electrode passivation, prolonging equipment life, and reducing equipment energy consumption

Active Publication Date: 2017-02-22
SINOSTEEL ANSHAN RES INST OF THERMO ENERGY CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This technology has disadvantages such as slow reaction speed, easy blockage of the reactor, and large dosage of iron filings and acid-base; (2) electrocatalytic oxidation, which uses an anode with high potential and catalytic activity to directly oxidize pollutants in wastewater. The technical electrode consumption is large, the electrode is expensive, and the cost is high; (3) electrodialysis is to add a selective permeable membrane in the electric field to separate pollutants. Its disadvantage is that it is easy to produce concentration extremes during operation and cause equipment Scaling reduces treatment efficiency and increases energy consumption; (4) electrocoagulation, under the condition of power on, the metal anode generates cations and forms a flocculant, which flocculates and removes pollutants, and at the same time, oxidation-reduction decomposition pollution and gas Separation of pollutants by flotation
Electrocoagulation is widely used in the field of wastewate

Method used

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  • Waste water treating device and method based on electrochemical principle
  • Waste water treating device and method based on electrochemical principle
  • Waste water treating device and method based on electrochemical principle

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0038] Example 1:

[0039] To treat coking wastewater, the coking wastewater used is the effluent of the secondary sedimentation tank after biochemical treatment. The distance between the plates is 8mm, the anode and cathode are made of aluminum electrodes, the input voltage of the pulse power supply is 220V, the input frequency is 50Hz, the power supply duty ratio is 60%, the output frequency is 3000Hz, and the output current is 1A / m 2 , the processing time is 10min. The flocs are removed by static separation, and the effluent complies with the coking chemical pollutant discharge standard (GB16171-2012). The water quality indicators before and after treatment are shown in Table 1.

[0040] Table 1: Changes in water quality indicators after coking wastewater treatment

[0041]

Example Embodiment

[0042] Example 2:

[0043] Treatment of wastewater containing a variety of heavy metals. The distance between the plates is 10mm, the anode and cathode are aluminum electrodes, the input voltage of the pulse power supply is 220V, the input frequency is 50Hz, the power supply duty ratio is 70%, the output frequency is 500Hz, and the output current is 6A / m 2 , the processing time is 45min. The concentrations of heavy metals in the water before and after treatment are shown in Table 2.

[0044] Table 2: Concentration change of heavy metal wastewater after treatment

[0045]

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Abstract

A waste water treating device and method based on an electrochemical principle comprises a reaction tank, an electrode A, an electrode B, an electrode fixing strip, an electrode supporting column, a stirring paddle and rotating shafts, wherein the reaction tank is cylindrical; flanges and flange covers are arranged at the upper end and the lower end of the reaction tank; each rotating shaft is mounted in the center of the corresponding flange cover through a bearing; the electrode supporting column is fixed on the flange cover of the lower part of the reaction tank; the electrode A and the electrode B are alternately stacked at the upper end of the electrode supporting column; the stirring paddle is placed between the electrode A and the electrode B; the diameters of center holes of the electrode A and the electrode B are greater than the diameter of each rotating shaft; the center hole of the stirring paddle is matched with the outer diameter of the rotating shaft; one side of the electrode fixing strip is fixed on the inner wall of the reaction tank; and the other side of the electrode fixing strip is clamped in grooves in the periphery of the electrode A and the periphery of the electrode B. The distance between pole plates is adjusted adaptively and is not changed, a bidirectional pulse power supply is used, passivation of the electrodes is prevented, the stirring paddle accelerates migration of ions and air bubbles on the pole plates, and matters attached to the pole plates are removed.

Description

technical field [0001] The invention relates to the field of environmental engineering, in particular to a wastewater treatment device and method based on electrochemical principles. Background technique [0002] Due to its versatility, high flexibility, no pollution or less pollution, and easy control, electrochemical technology is gradually applied to various chemical wastewater and water purification in electroplating, chemical, pharmaceutical, printing and dyeing, and papermaking. At present, there are mainly the following electrochemical technologies and equipment: (1) Micro-electrolysis, mainly iron filings and activated carbon form countless primary batteries under acidic conditions, and use micro-electrolysis to remove pollutants in wastewater. This technology has disadvantages such as slow reaction speed, easy blockage of the reactor, and large dosage of iron filings and acid-base; (2) electrocatalytic oxidation, which uses an anode with high potential and catalytic...

Claims

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Application Information

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IPC IPC(8): C02F1/463
CPCC02F1/46104C02F1/46109C02F1/463C02F2001/46123C02F2201/46105C02F2201/46175
Inventor 安路阳张立涛张功多孟庆锐刘志博刘硕陈亮
Owner SINOSTEEL ANSHAN RES INST OF THERMO ENERGY CO LTD
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