CN205973921U - High concentration waste water electricity chemical oxidation reactor - Google Patents
High concentration waste water electricity chemical oxidation reactor Download PDFInfo
- Publication number
- CN205973921U CN205973921U CN201620964153.2U CN201620964153U CN205973921U CN 205973921 U CN205973921 U CN 205973921U CN 201620964153 U CN201620964153 U CN 201620964153U CN 205973921 U CN205973921 U CN 205973921U
- Authority
- CN
- China
- Prior art keywords
- shell body
- runner
- battery lead
- lead plate
- waste water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a high concentration waste water electricity chemical oxidation reactor, include: a shell body, it installs the S type buffering runner of a cavity and a vertical extension to constitute the plate electrode that has a vertical extension in the shell body, S type buffering runner is located lower part one side of plate electrode installation cavity, and its runner export with plate electrode installation cavity intercommunication, its runner import lies in the bottom and the conduct of shell body the water inlet of shell body, the top of shell body be provided with one with the delivery port of plate electrode installation cavity intercommunication, and a plurality of anode plates and a plurality of negative plate, a plurality of anode plates and a plurality of negative plate vertical spacing setting respectively are in the plate electrode installation cavity of shell body is indoor and be crisscross relative parallel distribution. The utility model has the advantages of the treatment effeciency is high, the energy consumption low, physics chemical properties stabilization, surface are difficult for contaminated, long service life.
Description
Technical field
This utility model is related to sewage treatment equipment technical field, and more particularly, to a kind of high-concentration waste water electrochemical oxidation is anti-
Answer device.
Background technology
In recent years, growing continuously and fast of China's industrial economy increases the demand of water for industrial use, thus also creating big
Amount industrial wastewater, Industrial Wastewater Treatment and the reuse market demand increase substantially.Membrane Separation for Water Treatment is more conventional at present
A kind of method for treating water, its according to the difference of mixture physical property, mainly quality, volume size and geometric shape difference,
Solid-liquid separation is carried out according to the method sieved to mixture using seperation film.However, existing Membrane Separation for Water Treatment exists directly
Connect that operating cost is higher, depreciation maintenance cost high, influent quality had higher requirements, retention time of sewage length, COD clearance low
Problem.
For this reason, applicant carried out beneficial exploration and trial, have found result of the above problems, will be detailed below being situated between
The technical scheme continuing produces under this background.
Utility model content
Technical problem to be solved in the utility model：There is direct operating cost for existing Membrane Separation for Water Treatment
Higher, depreciation maintenance cost is high, influent quality is had higher requirements, retention time of sewage length, the low problem of COD clearance, and carries
For a kind of operating cost relatively low, depreciation maintenance cost is low, influent quality is not required, retention time of sewage is short, COD removes
The high high-concentration waste water electrochemical oxidation reactions device of rate.
The technical problem that this utility model is solved can employ the following technical solutions to realize：
A kind of high-concentration waste water electrochemical oxidation reactions device, including：
One shell body, constitutes in described shell body and has a vertically extending battery lead plate to install chamber and a vertically extending S
Type buffer runner, described S type buffer runner is located at the bottom side that chamber installed by described battery lead plate, and its runner exit with described
Chamber installed by battery lead plate, and its tunnel inlets is located at the bottom of described shell body the water inlet as described shell body, institute
The top stating shell body is provided with the outlet of one and described battery lead plate installation chamber；And
Vertical spacing is arranged on institute respectively for some positive plates and some minus plates, described some positive plates and some minus plates
State shell body battery lead plate install within the chamber and submit wrong opposing parallel distribution, described some positive plates pass through the first binding post with
The positive terminal of external power source connects, and described some positive plates are connected with the negative pole end of external power source by the second binding post.
The operation principle of high-concentration waste water electrochemical oxidation reactions device of the present utility model is as follows：
After electrifying electrodes, surface produces a large amount of OH (hydroxyl radical free radical, oxidizing species).Waste water flows through electrode table
Face, the Organic substance in waste water and ammonia nitrogen are oxidized to the innocuous substances such as carbon dioxide, water, nitrogen completely, in water partial salts and
Inorganic matters also remove simultaneously.Chemical reagent need not be added, do not produce secondary pollution.Reaction equation is as follows：
M+H2O→M(·OH)+H++e-
M (OH)+pollutant → M+CO2+H2O+ inorganic ionss
Note：M：Electrode
The electrochemical oxidation technology of high-concentration waste water electrochemical oxidation reactions device of the present utility model and existing embrane method water
The technique effect for the treatment of technology is compared, as shown in the table：
Due to employing technical scheme as above, the beneficial effects of the utility model are：
1st, advanced in performance, long service life, reliability are high, and system design is compact, supporting flexibly.
2nd, treatment effeciency is high, and novel electrode catalytic performance is high, can produce the hydroxyl radical free radical (OH) of a large amount of strong oxidizing properties,
Almost all of organic pollution can be processed, to COD removal efficiency up to 80%～99%.It is less demanding to influent quality,
Have wide range of applications in Industrial Waste Water Treatments field.
3rd, filtering material superior performance, recyclable noble metal, have that specific surface area is big, adsorption capacity is big, adsorption rate is fast,
The features such as usage cycles are long.
4th, operating cost is low, and novel electrode current utilization rate is high, loss is low, performance is strong, and system energy utilization rate is up to
More than 99%.Medicament need not be added in processing procedure, save medicament expense and use.Battery lead plate can be continuously using 5～8 years, filter material
The material replacement cycle is 0.5～1 year.
5th, stable, equipment acid and alkali-resistance corrode, electrode plate there is good physics and chemical stability it is not easy to
Fouling, anti impulsion load, stable effluent quality.
6th, easy and simple to handle, high degree of automation.System integrally can achieve intelligentized control method, according to change of water quality, adjusts fortune
Line parameter is it is ensured that standard water discharge.And can achieve remote monitoring, without staff on duty.
Brief description
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Or in description of the prior art the accompanying drawing of required use be briefly described it should be apparent that, drawings in the following description are only
It is some embodiments of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work
Under, other accompanying drawings can also be obtained according to these accompanying drawings.
Fig. 1 is three dimensional structure diagram of the present utility model.
Fig. 2 is longitudinal sectional view of the present utility model.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that this utility model is realized are easy to understand, under
Face combines and is specifically illustrating, and this utility model is expanded on further.
Referring to Fig. 1 and Fig. 2, what in figure was given is a kind of high-concentration waste water electrochemical oxidation reactions device, including shell body 100
And two pieces of positive plates 210 and two pieces of minus plates 220.
Constitute in shell body 100 and have a vertically extending battery lead plate that chamber 110 and a vertically extending S type buffer stream are installed
Road 120, S type buffer runner 120 is located at the bottom side that chamber 110 installed by battery lead plate, and its runner exit 121 and battery lead plate peace
Room 110 of behaveing affectedly connects, and its tunnel inlets 122 is located at the bottom of shell body 100 water inlet 130 as shell body 100, shell
The top of body 100 is provided with an outlet 140, and this outlet 140 is installed chamber 110 with battery lead plate and connected.
Vertical spacing is arranged on the battery lead plate installation cavity of shell body 100 respectively for two pieces of positive plates 210 and two pieces of minus plates 220
Room 110 is interior and submits wrong opposing parallel distribution, and two pieces of positive plates 210 are connected with the positive terminal of external power source by binding post 310,
Two pieces of minus plates 220 are connected with the negative pole end of external power source by binding post 320.Certainly, positive plate 210 and minus plate 220
Quantity is not limited to the quantity in the present embodiment, and it should install the size of chamber 110 according to battery lead plate and electrochemical oxidation requires
Determine etc. factor.
Waste water enters in S type buffer runner 120 from the water inlet 130 of shell body 100, then via S type buffer runner 120
Runner exit 121 enter battery lead plate install chamber 110 in, then waste water flows through two pieces of positive plates 210 and two pieces from bottom to top
The runner being formed between minus plate 220, finally flows out from the outlet 140 of shell body 100.S type buffer runner 120 makes to enter
Waste water in shell body 100 is necessarily buffered so that through battery lead plate install chamber 110 in pole plate when current more
Uniformly it is ensured that the pollutant in waste water are preferably degraded.
Of the present utility model ultimate principle and principal character and of the present utility model advantage have been shown and described above.One's own profession
The technical staff of industry it should be appreciated that this utility model is not restricted to the described embodiments, described in above-described embodiment and description
Principle of the present utility model is simply described, on the premise of without departing from this utility model spirit and scope, this utility model is also
Have various changes and modifications, these changes and improvements both fall within the range of claimed this utility model.This utility model
Claimed scope is by appending claims and its equivalent thereof.
Claims (1)
1. a kind of high-concentration waste water electrochemical oxidation reactions device is it is characterised in that include：
One shell body, constitutes in described shell body and has a vertically extending battery lead plate installation chamber and a vertically extending S type to delay
Swash of wave road, described S type buffer runner is located at the bottom side that chamber installed by described battery lead plate, and its runner exit and described electrode
Chamber installed by plate, and its tunnel inlets is located at the bottom of described shell body the water inlet as described shell body, described outer
The top of housing is provided with the outlet of one and described battery lead plate installation chamber；And
Vertical spacing is arranged on outside described respectively for some positive plates and some minus plates, described some positive plates and some minus plates
The battery lead plate of housing is installed within the chamber and is submitted wrong opposing parallel distribution, and described some positive plates pass through the first binding post and outside
The positive terminal of power supply connects, and described some positive plates are connected with the negative pole end of external power source by the second binding post.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620964153.2U CN205973921U (en) | 2016-08-26 | 2016-08-26 | High concentration waste water electricity chemical oxidation reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620964153.2U CN205973921U (en) | 2016-08-26 | 2016-08-26 | High concentration waste water electricity chemical oxidation reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205973921U true CN205973921U (en) | 2017-02-22 |
Family
ID=58038450
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620964153.2U Expired - Fee Related CN205973921U (en) | 2016-08-26 | 2016-08-26 | High concentration waste water electricity chemical oxidation reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205973921U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111847595A (en) * | 2019-04-30 | 2020-10-30 | 西藏神州瑞霖环保科技股份有限公司 | Nano electrochemical reaction device |
| CN112374584A (en) * | 2020-11-25 | 2021-02-19 | 深圳市超其环境科技有限公司 | Industrial wastewater treatment device and treatment method thereof |
-
2016
- 2016-08-26 CN CN201620964153.2U patent/CN205973921U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111847595A (en) * | 2019-04-30 | 2020-10-30 | 西藏神州瑞霖环保科技股份有限公司 | Nano electrochemical reaction device |
| CN112374584A (en) * | 2020-11-25 | 2021-02-19 | 深圳市超其环境科技有限公司 | Industrial wastewater treatment device and treatment method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103058335B (en) | Electrochemical reactor of graphene-Ti electrode for treating printing and dyeing wastewater | |
| CN204675927U (en) | A kind of device of electrochemical oxidation method treatment of dyeing and printing | |
| CN205973921U (en) | High concentration waste water electricity chemical oxidation reactor | |
| CN106673276A (en) | Apparatus for treating high-salinity wastewater jointly by photoelectric catalytic oxidation and electric adsorption | |
| CN100334006C (en) | Three-phase activated carbon fluidized bed electrochemical treatment installation and method for organic wastewater | |
| CN103482730B (en) | A kind of Electrocatalytic wastewater treatment system | |
| CN211283840U (en) | Plasma aeration sewage treatment device | |
| CN111320243A (en) | Membrane-free electrodeionization method and device with current perpendicular to water flow direction | |
| CN208700646U (en) | A kind of photocatalysis three-dimensional electrolysis fluidized-bed reactor | |
| CN203625090U (en) | Electrocatalytic wastewater treatment system | |
| CN1275685C (en) | Electrochemical regenerator and regenerating method for activated carbon | |
| CN106145460A (en) | A kind of electrochemical oxidation method processes the device of dyeing waste water | |
| CN202912755U (en) | Device for treating organic wastewater via electric field ozone compound catalysis and oxidation | |
| CN105762394B (en) | A kind of filter-type cathode microbial desalination cell and its application | |
| CN212222679U (en) | Wastewater recycling treatment system based on flow electrode | |
| CN209721886U (en) | A kind of electricity production 20-87W/m2Energy conservation catalysis water treatment facilities | |
| CN203741100U (en) | Multidimensional sewage treatment device | |
| CN203256011U (en) | Electrolytic oxidation-chemical oxidation compounded sewage treatment apparatus | |
| CN2726715Y (en) | Electrochemical regenerating device of active carbon | |
| CN2729049Y (en) | Three-phase active carbon fluid-bed electrochemical treatment device of organic waste water | |
| CN206828156U (en) | The photoelectrocatalysis processing system of high-salt wastewater | |
| CN216687757U (en) | Electrooxidation system of conductive ceramic electrode | |
| CN219297334U (en) | Energy-saving sewage treatment device | |
| CN209442707U (en) | A kind of advanced oxidation reaction device electro-catalysis pole heap | |
| CN217377627U (en) | Efficient landfill leachate preprocessing device and landfill leachate processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170222 Termination date: 20180826 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |