CN205873974U - Novel board -like rotary electrode electricity flocculation electrolysis device - Google Patents
Novel board -like rotary electrode electricity flocculation electrolysis device Download PDFInfo
- Publication number
- CN205873974U CN205873974U CN201620698313.3U CN201620698313U CN205873974U CN 205873974 U CN205873974 U CN 205873974U CN 201620698313 U CN201620698313 U CN 201620698313U CN 205873974 U CN205873974 U CN 205873974U
- Authority
- CN
- China
- Prior art keywords
- chamber
- wall
- output shaft
- electricity flocculation
- flocculation
- 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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- 238000005189 flocculation Methods 0.000 title claims abstract description 61
- 230000016615 flocculation Effects 0.000 title claims abstract description 60
- 230000005611 electricity Effects 0.000 title claims abstract description 58
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 37
- 238000006243 chemical reaction Methods 0.000 claims abstract description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 230000000875 corresponding Effects 0.000 claims abstract description 10
- 238000007789 sealing Methods 0.000 claims description 6
- 230000001808 coupling Effects 0.000 abstract 1
- 238000010168 coupling process Methods 0.000 abstract 1
- 238000005859 coupling reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 16
- 239000010865 sewage Substances 0.000 description 11
- 239000002245 particle Substances 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000000356 contaminant Substances 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 4
- 231100000719 pollutant Toxicity 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 230000036647 reaction Effects 0.000 description 3
- 150000001768 cations Chemical class 0.000 description 2
- 230000003311 flocculating Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxyl anion Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- -1 iron ion Chemical class 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 1
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical compound [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminum Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005039 chemical industry Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000737 periodic Effects 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000003638 reducing agent Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Abstract
The utility model relates to a novel board -like rotary electrode electricity flocculation electrolysis device, include: the reaction box, be equipped with a baffle in the reaction box just the baffle separates the reaction box for cavity I and cavity II, I outer wall of cavity is equipped with the water inlet and II outer walls of cavity are equipped with the delivery port, be equipped with a driving motor just on II outer walls of cavity driving motor's output shaft runs through this outer wall, the rigid coupling has the electrolysis positive pole just on the inner wall that cavity II and this outer wall are just corresponding driving motor's output shaft runs through the electrolysis positive pole, is located to join in marriage through sealed bearing on the output shaft between electrolysis positive pole and the baffle to have met electrolytic cathode, driving motor's output shaft runs through baffle and its and exposes on the free end in the cavity I to join in marriage through sealed bearing and connect the electricity negative pole that flocculates, I inner wall of cavity is equipped with the electricity flocculation positive pole that corresponds with electricity flocculation negative pole.
Description
Technical field
This utility model belongs to the dirty water decontamination handles technical field, particularly relates to New-type plate rotation electrode electricity flocculation electricity
Solve device.
Background technology
In recent years, occurring that more employing electrochemical principle processes the technology of industrial wastewater both at home and abroad, electric flocculation technique is exactly
One therein.Electric flocculation technique range of application is relatively wide, such as, can be used for chemical industry, plating, percolate, machinery, metallurgy, meal
The fields such as drink and carwash.
Electric flocculation technique processes the process of sewage and generally includes with the next stage: first under the effect of electric field, solubility electricity
Pole is dissolved and is produced metal cation (aluminium ion or iron ion), and water power is from producing hydroxide ion, wherein metal cation and hydrogen
Oxygen radical ion can combine formation " tiny flocculation agent " hydroxide of ferrum or aluminum (its composition be)；Under the effect of tiny flocculation agent,
The contaminant particle suspended in water can loss of stability；Mutually collide between contaminant particle and tiny flocculation agent after taking off surely, knot
Synthesize macroscopic big flocculating body, thus available precipitation or pneumatically supported method remove the pollutant in liquid.
Electricity flocculation process be the ion remaval pollutant utilizing cell reaction to produce, therebetween without additionally use oxidant or
Reducing agent, the less pollution therefore produced environment, is a kind of eco-friendly water technology；And electricity flocculation plant also has
Have that equipment is simple, floor space is few, be easily maintained and easily realize the advantages such as Automated condtrol.But, existing electricity flocculation
In use, the removal efficiency of pollutant still has much room for improvement device, and the use therefore easily causing electricity flocculation plant is subject to
To limiting.
Summary of the invention
This utility model provides one compared to existing technologies for solving technical problem present in known technology,
Can either be effectively prevented in course of reaction polar board surface produce bubble and raw sewage in impurity particle be attached to pole
Plate surface, improves treatment effeciency, simultaneously, additionally it is possible to simplify the New-type plate electric rotating of periodic replacement electricity flocculation positive plate program
Extremely electricity flocculation electrolysis unit.
This utility model is adopted the technical scheme that by solving technical problem present in known technology:
A kind of New-type plate rotation electrode electricity flocculation electrolysis unit, including: reaction chamber, it is provided with a dividing plate in described reaction chamber
And reaction chamber is divided into chamber I and chamber II by described dividing plate, described chamber I outer wall is provided with water inlet and chamber II outer wall is provided with
Outlet, the output shaft that described chamber II outer wall is provided with a driving motor and described driving motor runs through this outer wall, described chamber
The output shaft being connected with electrolytic anode and described driving motor on the inwall that room II is the most corresponding with this outer wall runs through electrolytic anode, position
Electrolysis cathode, the output shaft of described driving motor has been connected by sealing bearing on output shaft between electrolytic anode and dividing plate
Run through dividing plate and it is exposed on the free end in chamber I connect electricity flocculation negative electrode, described chamber I inwall by sealing bearing
It is provided with the electricity flocculation anode corresponding with electricity flocculation negative electrode.
For solving technical problem of the prior art, this utility model is provided with technique scheme.
Compared with prior art, improvements of the present utility model are as follows:
The first: improve the structure of reaction chamber, it may be assumed that be provided with a dividing plate and described dividing plate in described reaction chamber by reaction chamber
Being divided into chamber I and chamber II, described chamber I outer wall is provided with water inlet and chamber II outer wall is provided with outlet.
Designing based on this, operator can set electricity flocculation electrode and electrolysis electrode in chamber I and chamber II respectively, in order to
Sewage, after water inlet enters chamber I, first passes through electricity flocculation treatment process, in this process, under the effect of tiny flocculation agent, water
The contaminant particle of middle suspension can loss of stability；Mutually collide between contaminant particle and tiny flocculation agent after taking off surely, in conjunction with
Become macroscopic big flocculating body, thus available precipitation or pneumatically supported method remove the pollutant in liquid.Afterwards, in view of water inlet
Filling into pending sewage continuously, the sewage level that the electric flocculation technique through chamber I processes progressively increases, until energy
Enough enter by the way of overflow in chamber II.In view of being provided with electrolysis electrode in chamber II, through the electric flocculation technique of chamber I
The sewage processed will be processed further, then, discharge from outlet.
It two is: improve electricity flocculation negative electrode and the mounting means of electrolysis cathode, it may be assumed that described chamber II outer wall is provided with one
The output shaft driving motor and described driving motor runs through this outer wall, affixed on the inwall that described chamber II is the most corresponding with this outer wall
The output shaft having electrolytic anode and described driving motor runs through electrolytic anode, on the output shaft between electrolytic anode and dividing plate
By seal bearing connected electrolysis cathode, the output shaft of described driving motor run through dividing plate and its be exposed in chamber I from
Electricity flocculation negative electrode has been connected by sealing bearing by end.
When installing driving motor, can be installed on the outer wall of chamber II, then, drive the output shaft of motor to run through
This outer wall, is i.e. provided with the outer wall driving motor, is also connected with electrolysis on the inwall that chamber chamber II is the most corresponding with this outer wall
Anode, drives the main shaft of motor to run through electrolytic anode simultaneously.
Based on above-mentioned design, when operator drives motor, drive the output shaft of motor by band galvanic electricity flocculation negative electrode and electricity
Solving negative electrode to rotate, now, electricity flocculation negative electrode and electrolysis cathode in rotation can be respectively to water bodys in chamber I and chamber II simultaneously
Produce a certain degree of disturbance.During electricity flocculation and cell reaction, electricity flocculation negative electrode and the rotation of electrolysis cathode and two
The disturbance in person's rotary course, water body caused, it is possible to be effectively prevented electricity flocculation negative electrode and the bubble of electrolysis cathode surface generation
And the impurity particle in raw sewage is attached to the surface of two cathode plates, thus greatly improve the actual treatment effect of sewage
Rate.In addition, it is contemplated that electricity flocculation anode is as expendable part, changing with needing preiodic type, based on above-mentioned design, this preiodic type is more
Program of changing will be the easiest.
The design of dividing plate, is not only divided into two independent chambers by reaction chamber, in order to ensure electricity flocculation reaction and electrolysis
Carrying out successively of reaction, it can also enough support forces certain for the output shaft offer driving motor.
In technique scheme, this utility model can also use following technical measures: described reaction chamber upper end open and
Connect capping.
In technique scheme, this utility model can also use following technical measures: described water inlet is positioned at described chamber
Bottom the outer wall of room I, described outlet is positioned at bottom described chamber II outer wall.
In technique scheme, this utility model can also use following technical measures: the height of described dividing plate is described
The 2/3 of reaction chamber height.
This utility model has the advantage that with good effect:
Improvement based on technique scheme, this utility model by improving the structure of reaction chamber, whole by reaction chamber
Body formula structure is divided into chamber I and chamber II, so as to carry out electricity flocculation reaction and electrolysis respectively in chamber I and chamber II
Reaction；Also by improving electricity flocculation negative electrode and the mounting means of electrolysis cathode, it is achieved that drive the output shaft band galvanic electricity of motor
Flocculation negative electrode and electrolysis cathode rotate simultaneously, during electricity flocculation and cell reaction, and electricity flocculation negative electrode and the rotation of electrolysis cathode
The disturbance turned and in the two rotary course, water body is caused, it is possible to be effectively prevented electricity flocculation negative electrode and is produced from electrolysis cathode surface
Impurity particle in raw bubble and raw sewage is attached to the surface of two cathode plates, thus greatly improves the reality of sewage
Border treatment effeciency.Improvement based on above-mentioned optimal technical scheme, the technical solution of the utility model is able to the most perfect.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1, reaction chamber；2, dividing plate；3, chamber I；4, chamber II；5, water inlet；6, outlet；7, motor is driven；8、
Electrolytic anode；9, electrolysis cathode；10, electricity flocculation negative electrode；11, electricity flocculation anode.
Detailed description of the invention
Below in conjunction with the accompanying drawings detailed description of the invention of the present utility model is described further.At this it should be noted that
The explanation of these embodiments is adapted to assist in and understands this utility model, but be not intended that restriction of the present utility model.This
Outward, as long as the technical characteristic related in each embodiment of this utility model disclosed below does not constitutes conflict each other
Just can be mutually combined.
Embodiment one:
Refer to Fig. 1, a kind of New-type plate rotation electrode electricity flocculation electrolysis unit, including: reaction chamber 1, described reaction chamber 1
Inside being provided with a dividing plate 2 and described dividing plate 2 and reaction chamber 1 is divided into chamber I 3 and chamber II 4, described chamber I 3 outer wall is provided with into water
Mouth 5 and chamber II 4 outer wall are provided with outlet 6.Carry out in chamber I 3 be electricity flocculation reaction and carry out in chamber II 4 be electrolysis
Reaction, above-mentioned two course of reaction is carried out successively, when pending sewage is in water inlet constantly flows into chamber I 3, electricity flocculation sun
Gap liquid level between pole and electricity flocculation negative electrode constantly increases, and can overflow to the gap of electrolysis cathode and electrolytic anode.
The output shaft that described chamber II 4 outer wall is provided with a driving motor 7 and described driving motor 7 runs through this outer wall, institute
State and be connected with the output shaft of electrolytic anode 8 and described driving motor 7 on the inwall that chamber II 4 is the most corresponding with this outer wall and run through electrolysis
Anode 8.When installing driving motor, can be installed on the outer wall of chamber II, then, drive the output shaft of motor to run through this
Outer wall, is i.e. provided with the outer wall driving motor, is also connected with electrolysis sun on the inwall that chamber chamber II is the most corresponding with this outer wall
Pole, drives the main shaft of motor to run through electrolytic anode simultaneously.
On output shaft between electrolytic anode 8 and dividing plate 2 by seal bearing connected electrolysis cathode 9, described in drive
The output shaft of galvanic electricity machine 7 runs through dividing plate 2 and it is exposed on the free end in chamber I 3 connect electricity flocculation by sealing bearing
Negative electrode 10, described chamber I 3 inwall is provided with the electricity flocculation anode 11 corresponding with electricity flocculation negative electrode 10.This design gives electricity wadding
Solidifying anode and electricity flocculation negative electrode and electrolytic anode and the position relationship of electrolysis cathode, and drive the output shaft of motor successively with
Electrolytic anode, electrolysis cathode and the annexation of electricity flocculation negative electrode.
In the present embodiment, described reaction chamber 1 upper end open and connected capping.
In the present embodiment, described water inlet 5 is positioned at bottom described chamber I 3 outer wall, and described outlet 6 is positioned at described chamber
Bottom II 4 outer walls.
In the present embodiment, the height of described dividing plate 2 is the 2/3 of described reaction chamber 1 height.
These are only preferred implementation of the present utility model, it is noted that for the ordinary skill people of the art
For Yuan, on the premise of without departing from this utility model know-why, it is also possible to make some improvements and modifications, these improve and
Retouching also should be regarded as protection domain of the present utility model.
Claims (4)
1. a New-type plate rotation electrode electricity flocculation electrolysis unit, it is characterised in that: including: reaction chamber (1), described reaction chamber
(1) it is provided with a dividing plate (2) and described dividing plate (2) in and reaction chamber (1) is divided into chamber I (3) and chamber II (4), described chamber I
(3) outer wall is provided with water inlet (5) and chamber II (4) outer wall is provided with outlet (6), and described chamber II (4) outer wall is provided with one and drives
The output shaft of galvanic electricity machine (7) and described driving motor (7) runs through this outer wall, interior the most corresponding with this outer wall of described chamber II (4)
The output shaft being connected with electrolytic anode (8) and described driving motor (7) on wall runs through electrolytic anode (8), is positioned at electrolytic anode (8)
And connected electrolysis cathode (9), the output shaft of described driving motor (7) by sealing bearing on the output shaft between dividing plate (2)
Run through dividing plate (2) and it is exposed on the free end in chamber I (3) connect electricity flocculation negative electrode (10), institute by sealing bearing
State chamber I (3) inwall and be provided with electricity flocculation anode (11) corresponding with electricity flocculation negative electrode (10).
New-type plate rotation electrode electricity the most according to claim 1 flocculation electrolysis unit, it is characterised in that: described reaction chamber
(1) upper end open and connected capping.
New-type plate rotation electrode electricity the most according to claim 1 flocculation electrolysis unit, it is characterised in that: described water inlet
(5) being positioned at bottom described chamber I (3) outer wall, described outlet (6) is positioned at bottom described chamber II (4) outer wall.
4. according to the New-type plate rotation electrode electricity flocculation electrolysis unit described in any one of claims 1 to 3, it is characterised in that:
The height of described dividing plate (2) is the 2/3 of described reaction chamber (1) height.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620698313.3U CN205873974U (en) | 2016-07-05 | 2016-07-05 | Novel board -like rotary electrode electricity flocculation electrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620698313.3U CN205873974U (en) | 2016-07-05 | 2016-07-05 | Novel board -like rotary electrode electricity flocculation electrolysis device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205873974U true CN205873974U (en) | 2017-01-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620698313.3U Expired - Fee Related CN205873974U (en) | 2016-07-05 | 2016-07-05 | Novel board -like rotary electrode electricity flocculation electrolysis device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205873974U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354134A (en) * | 2018-10-24 | 2019-02-19 | 东莞市三人行环境科技有限公司 | A kind of method of electric flocculation removal anodic oxidation Determinating Chromaticity of Dyeing Effluent |
-
2016
- 2016-07-05 CN CN201620698313.3U patent/CN205873974U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354134A (en) * | 2018-10-24 | 2019-02-19 | 东莞市三人行环境科技有限公司 | A kind of method of electric flocculation removal anodic oxidation Determinating Chromaticity of Dyeing Effluent |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170111 Termination date: 20210705 |