CN206328195U - A kind of integrated micro-electrolysis reaction device - Google Patents
A kind of integrated micro-electrolysis reaction device Download PDFInfo
- Publication number
- CN206328195U CN206328195U CN201621479346.5U CN201621479346U CN206328195U CN 206328195 U CN206328195 U CN 206328195U CN 201621479346 U CN201621479346 U CN 201621479346U CN 206328195 U CN206328195 U CN 206328195U
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- China
- Prior art keywords
- micro
- electrolysis
- electrolysis reaction
- area
- 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
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 63
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000000945 filler Substances 0.000 claims abstract description 18
- 239000000706 filtrate Substances 0.000 claims abstract description 16
- 230000000712 assembly Effects 0.000 claims abstract description 14
- 238000000429 assembly Methods 0.000 claims abstract description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 239000000428 dust Substances 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims description 3
- 239000012528 membrane Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 7
- 239000002351 wastewater Substances 0.000 description 15
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 description 4
- 238000005273 aeration Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a kind of integrated micro-electrolysis reaction device, including micro-electrolysis reactor and filter assemblies, micro-electrolysis reactor is divided into micro-electrolysis reaction area and filtrate area, micro-electrolysis reaction is provided with filler in area, the water pipe with water pump is provided with above micro-electrolysis reactor, it is additionally provided with the air hose being connected with water pipe on micro-electrolysis reactor, the junction of air hose and water pipe, which is provided with ejector, micro-electrolysis reactor, is also respectively provided with water inlet pipe and outlet pipe；The utility model substantially increases the utilization rate of reaction unit, has saved cost of investment and floor space, improves micro-electrolysis reaction efficiency.
Description
Technical field
The utility model belongs to technical field of waste water processing, and in particular to a kind of integrated micro-electrolysis reaction device, this reality
The early stage pretreatment unit of industrial wastewater, municipal wastewater is can be widely used for as a kind of processing unit of economical and efficient with new,
For improving the biodegradability of this two classes waste water, it can also be used to there is the decolorization of colourity waste water.
Background technology
Micro electrolysis tech as a kind of conventional wastewater processing technology unit due to its excellent performance such as：Decolourize, drop
The performances such as COD, the biodegradability for improving waste water are widely applied in the treatment of waste water, especially should in Wastewater Pretreatment unit
It is larger with being worth.
Currently, conventional microelectrolysis processing technology is that the iron carbon ball commonly used from the market is pre-processed as filler,
This filler is disadvantageous in that, is primarily due to iron carbon ball volume reason, big quantity space is occupied in reaction unit, can be made
Voidage significantly increases cost of investment less than 50%.Waste water is handled as filler with iron carbon ball, during the course of the reaction can
A large amount of sludge are produced, while there is most of iron simple substance to participate in reaction, a large amount of wastes of material are caused.Contrast currently
, either all there is oxygen after operation a period of time still with iron filings, carbon granules as reaction material with iron carbon ball in micro electrolysis tech
The problem of changing, get rusty.
The presence of these problems seriously constrains the popularization of micro electrolysis tech, while also bringing great environment and engineering
Application problem.
Utility model content
The purpose of this utility model is that, according to the deficiencies in the prior art, design one kind integrates aeration, agitating function
Micro-electrolysis reaction device, solve that micro-electrolysis reactor in the prior art is easily hardened, big, waste water treatment efficiency of changing filler difficulty
The low technical problem with COD clearances.
The utility model solves the technical scheme that its technical problem used：A kind of integrated micro-electrolysis reaction device,
Micro-electrolysis reactor including tubbiness and it is arranged on the filter assemblies that micro-electrolysis reactor top is in zigzag, described filtering group
The lower middle portion of micro-electrolysis reactor is cut into micro-electrolysis reaction area and filtrate area, described micro-electrolysis reaction area and is provided with by part
The water pipe that two ends respectively extend into micro-electrolysis reaction area and filtrate area is provided with above filler, described micro-electrolysis reactor, institute
It is provided with water pump, described micro-electrolysis reactor to be additionally provided with the water pipe stated and extends into micro-electrolysis reaction area and be connected with water pipe
Logical air hose, described air hose and the junction of water pipe are provided with ejector, on the side wall of described micro-electrolysis reactor
The water inlet pipe and the outlet pipe positioned at filtrate area top being respectively arranged with above micro-electrolysis reaction area.
Described filter assemblies are low-pressure membrane or filter cloth.
Described filler is the mixture of iron powder and carbon dust.
The beneficial effects of the utility model are：
The utility model adds iron powder and carbon dust in micro-electrolysis reaction area as filler, and iron powder can be supplemented at any time, it is to avoid
The replacing of filler, without the need for substantial amounts of carbon dust and carbon dust is disposably added, substantially increases the utilization rate of reaction unit, section
About cost of investment and floor space.The utility model and promote filler fully to be contacted with waste water by water pump and ejector, mend
Enter enough air, improve micro-electrolysis reaction efficiency；Simultaneously set filter assemblies avoid filler be lost in reduce filler into
This, while reducing the damage of water pump.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Each reference is：1-micro-electrolysis reaction area, 2-filter assemblies, 3-water pump, 4-ejector, 5-air hose,
6-water pipe, 7-water inlet pipe, 8-outlet pipe.
Embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings.
Shown in reference picture 1, the utility model discloses a kind of integrated micro-electrolysis reaction device, include the light electrolysis of tubbiness
Reactor and the filter assemblies 2 that micro-electrolysis reactor top is in zigzag are arranged on, described filter assemblies 2 are by micro-electrolysis reaction
The lower middle portion of device is cut into micro-electrolysis reaction area 1 and filtrate area, described micro-electrolysis reaction area 1 and is provided with filler, described
The water pipe 6 that two ends respectively extend into micro-electrolysis reaction area 1 and filtrate area, described water pipe 6 are provided with above micro-electrolysis reactor
On be provided with water pump 3, described micro-electrolysis reactor to be additionally provided with and extend into what micro-electrolysis reaction area 1 was connected with water pipe 6
Air hose 5, described air hose 5 and the junction of water pipe 6 are provided with ejector 4, on the side wall of described micro-electrolysis reactor
It is respectively arranged with the water inlet pipe 7 and the outlet pipe 8 positioned at filtrate area top positioned at the top of micro-electrolysis reaction area 1.
Described filter assemblies 2 are low-pressure membrane or filter cloth.
Described filler is the mixture of iron powder and carbon dust.
A kind of application method of integrated micro-electrolysis reaction device, comprises the following steps：
A, by iron powder and carbon dust according to 1:2 ratio is well mixed and is arranged on as filler in micro-electrolysis reaction area 1；
B, opening water inlet pipe 7, make to be full of waste water in micro-electrolysis reaction area 1, waste water enters filtrate after filtering through filter assemblies 2
Area；
C, one end drive water pump 3 after extending into the water inlet of water pipe 6 in filtrate area, in water pump 3, compressed air with ejector 4
Under effect, filler is set fully to contact, be aerated with waste water, the waste water after micro-electrolysis reaction enters filtrate area simultaneously after filter assemblies 2
Overflowed from outlet pipe 8.
Embodiment of the present utility model is, it would be desirable to the waste water of processing, enters micro-electrolysis reaction area by water inlet pipe 7
1, waste water enters filtrate area by filter assemblies 2, when water reaches certain depth, starts the Shui Jingshui of water pump 3, at this moment filtrate area
Pipe 6, water pump 3 enter ejector 4, and water can cause certain negative pressure during flowing, and compressed air enters incident flow by air hose 5
Device 4, and being mixed in ejector 4 with water, most the delivery port through ejector 4 sprays afterwards, the water of ejection with certain dynamics and
Angle, stirring is played a part of in micro-electrolysis reaction area 1, while containing certain air in the water sprayed, is played aeration and is made
With increasing reaction rate, thus circulate.React after a period of time, the depth of water in filtrate area highly reaches delivery port, reacted
Water is discharged by outlet pipe 8.
Above-described embodiment only illustrative principle of the present utility model and its effect, and the embodiment that part is used,
For the person of ordinary skill of the art, on the premise of the utility model creation design is not departed from, if can also make
Dry modification and improvement, these belong to protection domain of the present utility model.
Claims (3)
1. a kind of integrated micro-electrolysis reaction device, it is characterised in that：Micro-electrolysis reactor including tubbiness and it is arranged on micro- electricity
Solve the filter assemblies that reactor top is in zigzag（2）, described filter assemblies（2）The middle and lower part of micro-electrolysis reactor is split
Into micro-electrolysis reaction area（1）With filtrate area, described micro-electrolysis reaction area（1）Inside it is provided with filler, described micro-electrolysis reaction
Two ends, which are provided with, above device respectively extends into micro-electrolysis reaction area（1）With the water pipe in filtrate area（6）, described water pipe（6）On set
It is equipped with water pump（3）, it is additionally provided with described micro-electrolysis reactor and extends into micro-electrolysis reaction area（1）With water pipe（6）It is connected
Air hose（5）, described air hose（5）And water pipe（6）Junction be provided with ejector（4）, described micro-electrolysis reaction
It is respectively arranged with the side wall of device positioned at micro-electrolysis reaction area（1）The water inlet pipe of top（7）With the water outlet positioned at filtrate area top
Pipe（8）.
2. a kind of integrated micro-electrolysis reaction device according to claim 1, it is characterised in that described filter assemblies
（2）For low-pressure membrane or filter cloth.
3. a kind of integrated micro-electrolysis reaction device according to claim 2, it is characterised in that described filler is iron powder
With the mixture of carbon dust.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621479346.5U CN206328195U (en) | 2016-12-30 | 2016-12-30 | A kind of integrated micro-electrolysis reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621479346.5U CN206328195U (en) | 2016-12-30 | 2016-12-30 | A kind of integrated micro-electrolysis reaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206328195U true CN206328195U (en) | 2017-07-14 |
Family
ID=59294746
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621479346.5U Expired - Fee Related CN206328195U (en) | 2016-12-30 | 2016-12-30 | A kind of integrated micro-electrolysis reaction device |
Country Status (1)
| Country | Link |
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| CN (1) | CN206328195U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106698599A (en) * | 2016-12-30 | 2017-05-24 | 武汉兴天宇环境股份有限公司 | Integrated micro-electrolysis reaction device and use method |
-
2016
- 2016-12-30 CN CN201621479346.5U patent/CN206328195U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106698599A (en) * | 2016-12-30 | 2017-05-24 | 武汉兴天宇环境股份有限公司 | Integrated micro-electrolysis reaction device and use method |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170714 |