CN206069605U - A kind of agitation and filtration declines electrolysis reactor - Google Patents
A kind of agitation and filtration declines electrolysis reactor Download PDFInfo
- Publication number
- CN206069605U CN206069605U CN201621080511.XU CN201621080511U CN206069605U CN 206069605 U CN206069605 U CN 206069605U CN 201621080511 U CN201621080511 U CN 201621080511U CN 206069605 U CN206069605 U CN 206069605U
- Authority
- CN
- China
- Prior art keywords
- screen plate
- stirring vane
- filtration
- agitation
- declines
- 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.)
- Active
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The electrolysis reactor the utility model discloses a kind of agitation and filtration declines, including：Reaction tube；Filter assemblies, which includes screen plate and demarcation strip, and screen plate one end is connected to reaction tube inwall, the other end and is connected to demarcation strip lower end；Mixing component, drive shaft which includes coaxially being built in reaction tube, the first stirring vane in drive shaft, the motor for driving drive shaft rotation, brush body；Water inlet pipe and outlet pipe；To filter inclined-plane, the first stirring vane has hypotenuse, and brush body is arranged along the length of the hypotenuse direction for screen plate side.This utility model adds iron powder and powdered carbon as filler in reaction zone, which can supplement iron powder at any time, it is to avoid the replacing of filler, and promotes filler to be fully contacted with sewage by mixing component, which raises micro-electrolysis reaction efficiency；Screen plate is simultaneously set avoids filler from being lost in and reduce filler cost, and brush body is set uninterruptedly the filtering surface of screen plate is scrubbed, it is to avoid the filtration hole plug of screen plate.
Description
Technical field
This utility model is related to light electrolysis sewage disposal technology, declines cell reaction more particularly, to a kind of agitation and filtration
Device.
Background technology
Fe-C micro electrolysis are, using Principles of Metal Erosion method, to form the good process processed to waste water by galvanic element, and
Claim internal electrolysis, Filtration with Iron Filings etc..Micro electrolysis tech is in the case of cold, using the light electrolysis being filled in waste water
Material itself produces 1.2V potential differences and carries out electrolysis process to waste water, to reach the purpose of degradable organic pollutant.
Existing Fe-C micro electrolysis principal set up ferrum charcoal mixed layer as filler, the mixed particle diameter of filler generally 1～
4cm, after a period of time use, filler easily forms hardened, causes reaction efficiency to reduce；And, with constantly reaction, ferrum
Reduce into branch, so as to cause using needing to carry out after certain hour replacement, and replacement difficulty is big, it is low to change efficiency
Under, it is unfavorable for the raising of sewage treating efficiency；Meanwhile, existing micro-electrolysis reactor COD clearances are low, it is impossible to meet increasingly
The demand of development.
Utility model content
The purpose of this utility model is to overcome above-mentioned technical deficiency, proposes that a kind of agitation and filtration declines electrolysis reactor,
In solving prior art, easy hardened, the big replacing filler difficulty of micro-electrolysis reactor, sewage treating efficiency and COD clearances are low
Technical problem.
To reach above-mentioned technical purpose, the technical solution of the utility model provides a kind of agitation and filtration and declines cell reaction
Device, including,
Reaction tube；
Filter assemblies, which includes screen plate and demarcation strip, and described screen plate one end is connected to the reaction tube inwall, another
End is connected to the demarcation strip lower end, and the reaction tube inner chamber body is separated to form reaction zone and filter by the screen plate and demarcation strip
Liquid zone；
Mixing component, which includes coaxially being built in the drive shaft of the reaction tube, in the drive shaft first stirs
Mix blade, the motor for driving the drive shaft rotation, brush body；And
The water inlet pipe for connecting with the reaction zone and filtrate area respectively and outlet pipe；
Wherein, the screen plate relative response area side for filter inclined-plane, first stirring vane with one with it is described
The hypotenuse that inclined-plane is engaged is filtered, the brush body is arranged along the length of the hypotenuse direction, and the brush body can be with described first
Stirring vane rotates and scrubs the filtration inclined-plane of the screen plate.
Preferably, first stirring vane at least two and it is arranged circumferentially along the drive shaft.
Preferably, the brush body is provided with the hypotenuse of the first stirring vane described at least one.
Preferably, first stirring vane shape in a rectangular trapezoid, and each described first stirring vane is straight up
Extend and form the second stirring vane.
Preferably, the screen plate is tapered and is coaxially disposed with the reaction tube, and the demarcation strip is cylindrical in shape and under which
End is connected in the screen plate upper end.
Preferably, the screen plate and demarcation strip are tabular.
Preferably, the agitation and filtration declines electrolysis reactor also including an aeration component, and the aeration component includes setting
The Aeration fan that aeration tube in the reaction zone bottom is connected with the aeration tube.
Preferably, one and only one described first stirring vane is netted, and one and only one second stirring vane is
Netted, the first netted stirring vane and the second stirring vane are copper wire and work out.
Compared with prior art, this utility model adds iron powder and powdered carbon as filler in reaction zone, and which can supplement at any time
Iron powder, it is to avoid the replacing of filler, and promote filler to be fully contacted with sewage by mixing component, which raises micro-electrolysis reaction
Efficiency；Arranging screen plate simultaneously avoids filler loss from reducing filler cost, and arranges filtration of the brush body uninterruptedly to screen plate
Scrubbed in face, it is to avoid the filtration hole plug of screen plate.
Description of the drawings
Fig. 1 be agitation and filtration of the present utility model decline electrolysis reactor a kind of embodiment attachment structure illustrate
Figure；
Fig. 2 be agitation and filtration of the present utility model decline electrolysis reactor another embodiment attachment structure illustrate
Figure.
Specific embodiment
In order that the purpose of this utility model, technical scheme and advantage become more apparent, below in conjunction with accompanying drawing and enforcement
Example, is further elaborated to this utility model.It should be appreciated that specific embodiment described herein is only to explain
This utility model, is not used to limit this utility model.
Refer to Fig. 1, Fig. 2, embodiment of the present utility model declines electrolysis reactor there is provided a kind of agitation and filtration, bag
Include,
Reaction tube 1；
Filter assemblies 2, which includes screen plate 21 and demarcation strip 22, and 21 one end of the screen plate is connected to the reaction tube 1
Inwall, the other end are connected to 22 lower end of the demarcation strip, and 1 inner chamber body of the reaction tube is divided by the screen plate 21 and demarcation strip 22
Every formation reaction zone 101 and filtrate area 102；
Mixing component 3, which includes coaxially being built in the drive shaft 31 of the reaction tube 1, in the drive shaft 31
First stirring vane 32, the motor 33 for driving the drive shaft 31 rotation, and brush body 34；And
The water inlet pipe 4 for connecting with the reaction zone 101 and filtrate area 102 respectively and outlet pipe 5；
Wherein, 21 relative response area of the screen plate, 101 side is filtration inclined-plane 211, and first stirring vane 32 has
There is a hypotenuse 321 being engaged with the filtration inclined-plane 211, the brush body 34 is arranged along 321 length direction of the hypotenuse, and institute
State the filtration inclined-plane 211 that brush body 34 can rotate and scrub the screen plate 21 with first stirring vane 32.
During sewage disposal, sewage is entered in reaction tube 1 by water inlet pipe 4, and iron powder and charcoal are added in the sewage of reaction zone 101
Powder, and be stirred continuously by mixing component 3 to promote iron powder and powdered carbon and sewage to be fully contacted, and then promote micro-electrolysis reaction effect
Rate, can supplement iron powder as needed during the present embodiment micro-electrolysis reaction, it is to avoid ferrum reduce after filler replacing.Light electrolysis
Reacted sewage enters filtrate area 102 after the filtration of screen plate 21, and the sewage in filtrate area 102 can be discharged by outlet pipe 5
To subsequent processing, the screen plate 21 of the present embodiment can avoid filler from entering filtrate area 102 by reaction zone 101, and then avoid filler
Loss.Wherein, when screen plate 21 is filtered, the accumulation of filtration inclined-plane 211 filler of screen plate 21 is easily caused, and then blocks screen plate
21, therefore the present embodiment arranges the hypotenuse 321 that inclined-plane 211 mutually agrees with that filters with screen plate 21 on the first stirring vane 32, and
Brush body 34 is set on hypotenuse 321, filtration inclined-plane 211 of the brush body 34 to screen plate 21 is rotarily driven by the first stirring vane 32
Scrubbed, the filler brush accumulated on inclined-plane 211 will be filtered to sewage, so as to avoid screen plate 21 from blocking.Wherein, this enforcement
Filtering holes are provided with example screen plate 21 to pass through and intercept filler to pass through in order to sewage, demarcation strip 22 is non-porous structure, can be hindered
Only sewage enters filtrate area 102.And, the water inlet pipe 4 is connected with 101 bottom of the reaction zone, the outlet pipe 5 with it is described
Connect at the top of filtrate area 102, consequently facilitating the water inlet of 101 bottom of reaction zone, the 102 top water outlet of filtrate area.
Wherein, as micro-electrolysis reaction needs certain air, although the stirring of mixing component 3 can improve the molten of sewage
Oxygen amount, but in order to further improve micro-electrolysis reaction efficiency, the electrolysis reactor that declines of agitation and filtration described in the present embodiment is also wrapped
Include an aeration component 6, the aeration component 6 includes aeration tube 61 located at 101 bottom of the reaction zone, and the aeration tube 61
The Aeration fan 62 of connection, in course of reaction, controllable Aeration fan 62 carries out intermittent aeration, and which may advantageously facilitate light electrolysis
Reaction efficiency.
The quantity of the first stirring vane of the present embodiment 32 can be arranged as required to, in order to increase stirring efficiency, described first
Stirring vane 32 at least two and it is arranged circumferentially along the drive shaft 31, when specifically arranging, is generally two or three
It is preferred, the present embodiment is preferably arranged to two, two the first stirring vanes 32 are symmetricly set in 31 both sides of drive shaft.The present embodiment
When brush body 34 is arranged, brush body 34 can be respectively provided with each first stirring vane 32, but brush body 34 is arranged excessively, is easily caused
Filter plate 21 weares and teares, therefore when specifically arranging, and the present embodiment only arranges brush on the hypotenuse 321 of first stirring vane 32 wherein
Body 34.In order to further avoid screen plate 21 from wearing and tearing, brush body 34 can be set to banister brush, and brush body 34 can be set with hypotenuse 321
It is set to and is detachably connected, in order to changes.
Coordinate for the ease of the filtration inclined-plane 211 with screen plate 21, the present embodiment is preferably by first stirring vane 32
Shape in a rectangular trapezoid is set, and the right-angle side of the first stirring vane 32 is axially fixed on the outer peripheral face of drive shaft 31, hypotenuse
321 are coordinated with the filtration inclined-plane 211 of screen plate 21.And in order to increase mixing effect, the present embodiment each described first stirring
Blade 32 extends straight up and forms the second stirring vane 35, and concrete first stirring vane, 32 upper end is shorter edge, lower end is
Longer sides, therefore shorter edge extends to form the second stirring vane 35 straight up, the second stirring vane 35 may be configured as rectangle, and then
The sewage of 101 upper end of reaction zone is stirred.
Sewage water filtration efficiency and stirring efficiency, mistake when wherein, in order to improve screen plate 21 and the cooperation of the first stirring vane 32
The angle of filtration 211 relative level of inclined-plane of filter plate 21 is 45～75 °, is preferably arranged to 60 °, corresponding hypotenuse 321 and water
The setting identical with the angle of 21 relative level of screen plate of the angle of plane, which is also preferably set to 60 °.
The shape of the present embodiment screen plate 21 and demarcation strip 22 can be arranged as required to, as shown in figure 1, screen plate 21 and point
Dividing plate 22 may be configured as tabular, and the lower surface of screen plate 21 is the filtration inclined-plane 211 being engaged with the first stirring vane 32,
The outer rim of screen plate 21 is connected to 22 lower end of 1 inwall of reaction tube and demarcation strip, and two sides of demarcation strip 22 are connected in reaction tube 1
Wall, in being plane due to the filtration inclined-plane 211 of screen plate 21, therefore brush body 34 can only scrub filtration inclined-plane 211 in cleaning
Middle part；Also can be as shown in Fig. 2 the screen plate 21 to be tapered and be coaxially disposed with the reaction tube 1, the demarcation strip 22 is in cylinder
Shape and its lower end are connected in 21 upper end of the screen plate, and now the inner surface of screen plate 21 as filters inclined-plane 211, brush body
34 can move along inclined-plane 211 is filtered when rotating, and which can carry out continuous way to filtration inclined-plane 211 and scrub.Wherein, also can be by screen plate
21 and demarcation strip 22 be disposed as arc, which is the deformation of above-mentioned embodiment, and therefore not to repeat here.
In order to further improve micro-electrolysis reaction efficiency, the present embodiment one and only one described first stirring vane 32 is
It is netted, one and only one second stirring vane 35 be it is netted, the first netted stirring vane 32 and the second stirring vane 35 it is equal
Work out for copper wire.As first stirring vane 32 and the second stirring vane 35 of the present embodiment are disposed as two, therefore will
One of them first stirring vane 32 and second stirring vane 35 are set to copper mesh, another first stirring vane 32
Tabular is set to then with the second stirring vane 35, first stirring vane 32 and the second stirring vane 35 of tabular act primarily as stirring and make
With, and the first stirring vane 32 of copper mesh and the second stirring vane 35 be while stirring, sewage can pass through copper mesh
Mesh is simultaneously fully contacted with copper wire, and copper mesh is can to play catalytic action to micro-electrolysis reaction during waste water, its
Micro-electrolysis reaction efficiency more than 20% can be improved.Wherein, in order to avoid copper mesh deforms with drive shaft whipping process, this reality
Apply example and the framework for mutually being agreed with the first stirring vane 32 and the second stirring vane 35 respectively is set, copper mesh is embedded in framework.
Wherein, in order to ensure the harmony of first stirring vane 32 and the second stirring vane 35 of copper wire web frame, this reality
Apply the both sides that first stirring vane 32 and the second stirring vane 35 of copper wire web frame are respectively arranged at drive shaft.It is corresponding,
Brush body 34 is preferably arranged on the hypotenuse 321 of the first stirring vane 32 of tabular.
In order to improve the adequacy of micro-electrolysis reaction, in the present embodiment filler, 270～300 μm of the particle diameter of iron powder, powdered carbon are
160～180 μm, wherein iron powder particle diameter is preferably 280 μm, and powdered carbon is preferably 170 μm.
Compared with prior art, this utility model adds iron powder and powdered carbon as filler in reaction zone 101, and which can be mended at any time
Fill iron powder, it is to avoid the replacing of filler, and promote filler to be fully contacted with sewage by mixing component 3, which raises light electrolysis
Reaction efficiency；Arranging screen plate 21 simultaneously avoids filler loss from reducing filler cost, and it is uninterrupted to filtering to arrange brush body 34
The filtering surface of plate 21 is scrubbed, it is to avoid the filtration hole plug of screen plate 21.
The above specific embodiment of the present utility model, does not constitute the restriction to this utility model protection domain.
Any various other corresponding change made according to technology design of the present utility model and deformation, should be included in practical
In new scope of the claims.
Claims (8)
1. a kind of agitation and filtration declines electrolysis reactor, it is characterised in that include,
Reaction tube；
Filter assemblies, which includes screen plate and demarcation strip, and described screen plate one end is connected to the reaction tube inwall, the other end and connects
The demarcation strip lower end is connected to, the reaction tube inner chamber body is separated to form reaction zone and filtrate by the screen plate and demarcation strip
Area；
Mixing component, which includes coaxially being built in the drive shaft of the reaction tube, the first paddle in the drive shaft
Piece, the motor and brush body that drive the drive shaft rotation；And
The water inlet pipe for connecting with the reaction zone and filtrate area respectively and outlet pipe；
Wherein, the screen plate relative response area side is filtration inclined-plane, and first stirring vane has one with the filtration
The hypotenuse that inclined-plane is engaged, the brush body are arranged along the length of the hypotenuse direction, and the brush body can be with the described first stirring
Blade rotates and scrubs the filtration inclined-plane of the screen plate.
2. agitation and filtration according to claim 1 declines electrolysis reactor, it is characterised in that first stirring vane is extremely
It is two and to be arranged circumferentially along the drive shaft less.
3. agitation and filtration according to claim 2 declines electrolysis reactor, it is characterised in that described at least one, first stirs
Mix.
4. the agitation and filtration according to Claims 2 or 3 declines electrolysis reactor, it is characterised in that first paddle
Piece shape in a rectangular trapezoid, and each described first stirring vane extends the second stirring vane of formation straight up.
5. agitation and filtration according to claim 4 declines electrolysis reactor, it is characterised in that the screen plate is tapered simultaneously
It is coaxially disposed with the reaction tube, the demarcation strip is cylindrical in shape and its lower end is connected in the screen plate upper end.
6. agitation and filtration according to claim 4 declines electrolysis reactor, it is characterised in that the screen plate and demarcation strip
It is tabular.
7. the agitation and filtration according to claim 5 or 6 declines electrolysis reactor, it is characterised in that the agitation and filtration formula
Micro-electrolysis reactor also includes an aeration component, and the aeration component includes aeration tube and the institute located at the reaction zone bottom
State the Aeration fan of aeration tube connection.
8. agitation and filtration according to claim 4 declines electrolysis reactor, it is characterised in that one and only one described
One stirring vane is netted, and one and only one second stirring vane is netted, and the first netted stirring vane and second is stirred
Blade is copper wire and works out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621080511.XU CN206069605U (en) | 2016-09-23 | 2016-09-23 | A kind of agitation and filtration declines electrolysis reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621080511.XU CN206069605U (en) | 2016-09-23 | 2016-09-23 | A kind of agitation and filtration declines electrolysis reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206069605U true CN206069605U (en) | 2017-04-05 |
Family
ID=58440806
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621080511.XU Active CN206069605U (en) | 2016-09-23 | 2016-09-23 | A kind of agitation and filtration declines electrolysis reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206069605U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106167321A (en) * | 2016-09-23 | 2016-11-30 | 武汉兴天宇环境股份有限公司 | A kind of agitation and filtration declines electrolysis reactor and reaction method thereof |
| CN111499057A (en) * | 2020-04-30 | 2020-08-07 | 杭州小鲤工业设计有限公司 | Energy-saving sewage treatment and cyclic treatment system |
-
2016
- 2016-09-23 CN CN201621080511.XU patent/CN206069605U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106167321A (en) * | 2016-09-23 | 2016-11-30 | 武汉兴天宇环境股份有限公司 | A kind of agitation and filtration declines electrolysis reactor and reaction method thereof |
| CN106167321B (en) * | 2016-09-23 | 2023-02-17 | 武汉兴天宇环境股份有限公司 | Stirring filtering type micro-electrolysis reactor and reaction method thereof |
| CN111499057A (en) * | 2020-04-30 | 2020-08-07 | 杭州小鲤工业设计有限公司 | Energy-saving sewage treatment and cyclic treatment system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106277457A (en) | A kind of horizontal integrated sewage disposal device | |
| CN109589860A (en) | A kind of highlands sewage treatment chemicals dosing plant | |
| CN205797116U (en) | A kind of sewage disposal flocculation tank with disturbance function | |
| CN206069605U (en) | A kind of agitation and filtration declines electrolysis reactor | |
| CN209697705U (en) | A kind of micro-nano bubble reinforcing dystopy elution equipment | |
| CN211936520U (en) | Stirrer device for dissolving organic polymer cation emulsion | |
| CN103520978A (en) | A vacuum filtering apparatus and an operating method thereof | |
| CN106167321A (en) | A kind of agitation and filtration declines electrolysis reactor and reaction method thereof | |
| CN207722442U (en) | A kind of nonferrous metals ore effluent treatment plant | |
| CN203845883U (en) | Textile wastewater coagulation inclined pipe combined settling pond | |
| CN106219861A (en) | A kind of belt Magneto separate sewage disposal system | |
| CN205258197U (en) | Energy -saving effluent treatment plant | |
| CN206069472U (en) | A kind of hybrid micro-electrolysis reactor of air | |
| CN210419393U (en) | Flocculating agent charge device for sewage treatment | |
| CN209493361U (en) | A kind of Sewage flocculation plant | |
| CN208603894U (en) | A kind of infant industry sewage treatment chemicals dosing plant | |
| CN208049541U (en) | A kind of crushing-ore system granulating pit residue filter equipment | |
| CN210764717U (en) | Industrial waste water desulfurization treatment device | |
| CN215946853U (en) | Novel high-efficient swash plate sedimentation treatment pond | |
| CN205933460U (en) | Integration sewage treatment sedimentation tank | |
| CN207904039U (en) | A kind of Laboratory Waste Water Treatment reaction unit | |
| CN207671826U (en) | A kind of system for regenerating and recycling of the fluorine-containing nitrogen-containing wastewater of electronics industry | |
| CN208008637U (en) | A kind of river black and odorous water tubular membrane MBR processing equipments | |
| CN208980459U (en) | A kind of industrial sewage recycling device | |
| CN106277453A (en) | A kind of sewage-treatment plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |