CN209322529U - A kind of organic sewage and waste water treatment device of rotary-type electrode of cylinder - Google Patents
A kind of organic sewage and waste water treatment device of rotary-type electrode of cylinder Download PDFInfo
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- CN209322529U CN209322529U CN201822031135.0U CN201822031135U CN209322529U CN 209322529 U CN209322529 U CN 209322529U CN 201822031135 U CN201822031135 U CN 201822031135U CN 209322529 U CN209322529 U CN 209322529U
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Abstract
The utility model relates to a kind of organic sewage and waste water treatment devices of the rotary-type electrode of cylinder, including shell, inlet and outlet, the shell is cylinder type and forms reactive tank, rotation system is equipped in reactive tank, connect electric system and pad system, the pad system includes the cartridge type positive plate being arranged in the inner walls, from the rotation polar plate group for connecing electric bushing and radiating outwardly extending several groups pole plate load-bearing axle and being arranged in the pole plate load-bearing axle, the rotation polar plate group in every group of pole plate load-bearing axle along cylinder spaced radial by being arranged and forming with the several layers arc surface positive plate of the insulation stirring shaft coaxial line and arc surface negative plate, and, the arc surface positive plate being arranged in every group of pole plate load-bearing axle is identical with the number of plies of arc surface negative plate, it is sequentially identical, interlamellar spacing is equal and end be disposed as it is opposite with cartridge type positive plate Arc surface negative plate.This reactor and method are not necessarily to additional mixing plant, and aerator reduces power consumption, and processing cost reduces.
Description
Technical field
The utility model relates to stain disease processing technology fields, more particularly to organic dirty useless using electrochemical method processing
The device and method of water.
Background technique
Two kinds of situations can occur during handling waste water for most of advanced oxidation, and one is venomous injurants in waste water
Matter has not been able to thorough mineralising, another kind be in order to reach certain treatment effect, need using a large amount of oxidant or other urge
Agent.No matter which kind of situation occurs during handling waste water, rising violently for wastewater treatment expense can be all caused, processing technique is difficult
It is promoted.Therefore, the development trend for purifying poisonous and harmful substance in organic industrial sewage is, place strong using catalysed oxidn
Reason effect is good, process flow is short technology, thus using electrochemical oxidation technology processing organic industrial sewage research increasingly by
To attention.
Electrochemical oxidation technology, in use due to only needing to provide clean electronics, is not necessarily to as water treatment technology
Add chemical agent, the setting of easy to operate, technique flexibly, the features such as degree of modularity is high and trail processing is easy and by phase
The concern in pass field, it is considered to be the technology of a kind of " environmental-friendly " has been employed successfully in ammonia nitrogen, dyestuff, coking, food at present
The processing of the sewage such as product and landfill leachate.
Electrode is the main place for carrying out charge transfer in electrochemical water treatment technology between electrode and solution, is to determine electrification
Where the core for learning water treatment system performance, electrode material directly affects the electric charge transfer rate between Cathode/Solution Interface.Electricity
Electrode material is both depended on the Index Theories such as Water Treatment process kinetic parameter, electrode life, process energy consumption
Physicochemical property.
Mainly there are graphite, activated carbon fibre (ACF) and boron-doped diamond (BDD) three currently used as the carbon material of anode material
Kind.Graphite mechanical strength therein is lower, easy to wear and oxidation；The overpotential for oxygen evolution of ACF electrode is low, and oxidability is limited, right
It is lower in persistent organic pollutants catalytic efficiency；BDD electrode is studied still immature at present, is also difficult to carry out commercial scale so far
It is and expensive with the production of size electrodes.Precious metal simple substance electrode such as Pd, Pt etc. are current most widely used electrodes, but
This kind of electrode is expensive, on a large scale for sewage treatment it is unrealistic, be often carried on other matrixes in practice with reduce at
This；In addition, this kind of electrode in degradation of organic substances it occur frequently that passivation phenomenon, while being easily oxidized to oxidation film and leading to electrification
Inactivation.
In addition, existing electrocatalysis oxidation reaction device still has many deficiencies, and such as: water inlet water distribution apparatus-form is single,
Waste water is easy to form the short stream of hydraulics or dead angle in reaction unit, influences treatment effect；It can release in use a large amount of
Heat, with the extension of working time, the temperature in device can be increased constantly, seriously affect the working efficiency of device and using the longevity
Life, etc..
It can be seen that existing plate material and reaction unit all have corresponding problem and shortage, it would be highly desirable to further change
It is kind.
Utility model content
The purpose of this utility model is in order to solve the above problem at least one, and the utility model provides a kind of cylinder rotation
The organic sewage and waste water treatment device of type electrode constructs single, inefficiency to change traditional electrocatalytic oxidation electrode reaction device,
Poor processing effect and the high status of energy consumption.
To solve the above problems, the utility model adopts the following technical solutions:
A kind of organic sewage and waste water treatment device of rotary-type electrode of cylinder, including shell, inlet and outlet, the shell
For cylinder type and reactive tank is formed, rotation system is equipped in reactive tank, connects electric system and pad system, the rotation system includes
The insulation stirring shaft of the heart within the barrel is set and the insulation connecting with insulation stirring shaft bottom agitation bearing, the insulation are stirred
The height of moving axis and the height of the cylinder are of substantially equal；The electric system that connects includes being enclosed in the insulation stirring shaft to connect electricity
It casing and connects the electrode that electric bushing is electrically connected with described and connects fulgurite, the pad system includes being arranged in the inner walls
Cartridge type positive plate, radiate outwardly extending several groups pole plate load-bearing axle and set in the pole plate load-bearing axle from connecing electric bushing
The rotation polar plate group set, every group of pole plate load-bearing axle include 1-5 root pole plate load-bearing axle, described every equal length of pole plate load-bearing axle and
To cartridge type positive plate have a distance H, the rotation polar plate group by every group of pole plate load-bearing axle along cylinder spaced radial setting and
It is formed with the several layers arc surface positive plate and arc surface negative plate of the insulation stirring shaft coaxial line, also, every group of pole plate is held
The arc surface positive plate being arranged on solid axle is identical with the number of plies of arc surface negative plate, sequence is identical, interlamellar spacing is equal and end is equal
It is set as the arc surface negative plate opposite with cartridge type positive plate.
Further, interlamellar spacing is between the arc surface positive plate and arc surface negative plate in all pole plate load-bearing axles
Distance H.
Further, the arc surface positive plate in every group of pole plate load-bearing axle and arc surface negative plate and adjacent sets pole plate load-bearing axle
On correspondence level on arc surface positive plate and arc surface negative plate between be all provided with and have the gap.
Further, the arc surface radial centre lines of the arc surface positive plate in each group pole plate load-bearing axle and arc surface negative plate
Between angle it is equal.
Further, the rotation polar plate group includes 2 circular arc positive plates, 3 circular arc negative plates, 5 groups of pole plates
Load-bearing axle and every group include 3 pole plate load-bearing axles for being from top to bottom aligned setting, the circular arc positive plate and circular arc negative plate with
Grafting or welding manner are connected with the pole plate load-bearing axle, and respectively connect fulgurite with electrode and be electrically connected, every group of pole plate load-bearing axle
Fulgurite is connect including at least one group of electrode, and the electrode connects fulgurite and at least one pole plate load-bearing axle parallel side-by-side is arranged, it is described
Electrode connects fulgurite, pole plate load-bearing axle and is connect electric bushing with described with grafting or welding manner and be connected, described to connect electric bushing and institute
Insulation stirring shaft is stated to socket-connect.
Further, the shell is externally provided with positive plate and connects electric handle, and external power supply is powered to cartridge type positive plate；Pass through the electricity
Pole, which connects, to be connect electric bushing external power supply and gives rotation polar plate group power supply, and the positive board group and the cathode board group described in fulgurite
It is in parallel respectively to be powered.
Further, the positive plate is titanium-based zinc doping lead dioxide electrode plate, and the negative plate is the modified titanium of oxalic acid
Pole plate.
Further, the water inlet is arranged in the outside of the lower part of the housing, the water inlet direction of the water inlet by down toward
On, and the inverse rotation direction in the rotation polar plate group；The edge of the case top is equipped with weir-type water outlet, in the weir-type
The outer side-lower of water outlet is equipped with water outlet diversion trench, and the water outlet is located at the outside of the water outlet diversion trench.
Further, the bottom of the shell is equipped with dreg removing system, and the dreg removing system includes slag-drip opening and shut-off valve；It is described
Foam removal device is equipped with above case top, which includes being parallel to the rotation removing scraper plate of the housing top surface and being used for
The connector that scraper plate is connected with the insulation rolling bearing is removed into the rotation.
Due to the use of above technical scheme, the utility model has following advantage compared with prior art:
Waste water is handled using the organic sewage and waste water treatment device of the rotary-type electrode of the cylinder of the utility model, electrode rotary can
To enhance water disturbance, efficiently solves wastewater treatment not exclusively and cause positive electricity pole surface and be easy depositing contaminants and organic carbon distribution
Deficiency, conversion zone is big, and water treatment effect improves, and enhances especially for the treatment effect of high concentrated organic wastewater.This is anti-
Answer device without additional mixing plant, aerator simplifies operating process, reduces power consumption, and processing cost reduces.
Detailed description of the invention
By reading the following detailed description of the preferred embodiment, various other advantages and benefits are common for this field
Technical staff will become clear.The drawings are only for the purpose of illustrating a preferred embodiment, and is not considered as practical to this
Novel limitation.And throughout the drawings, the same reference numbers will be used to refer to the same parts.In the accompanying drawings:
Fig. 1 is the structure top view according to the organic sewage and waste water treatment device of the rotary-type electrode of cylinder of the utility model；
Fig. 2 is the main view according to the organic sewage and waste water treatment device of the rotary-type electrode of cylinder of the utility model；
Fig. 3 is the vertical section schematic diagram according to the organic sewage and waste water treatment device of the rotary-type electrode of cylinder of the utility model；
Fig. 4 is the flow diagram according to the method for the organic stain disease of processing of the utility model.
Wherein: 1, shell；2, water inlet；3, water outlet；30, weir-type water purification outlet；31, it is discharged diversion trench；4, rotation system
Unite and connect electric system；40, insulate stirring shaft；41, electric bushing is connect；42, electrode connects fulgurite；43, pole plate load-bearing axle；5, pole plate system
System；50, positive plate connects electric handle, 51, positive plate group system；52, negative plate group system；6, slag-drip opening；60, shut-off valve；It is 7-1, pre-
Processing equipment；The organic sewage and waste water treatment device of the rotary-type electrode of 7-2, cylinder；7-3, drainage equipment；7-4, power equipment.
Specific embodiment
The illustrative embodiments of the disclosure are more fully described below with reference to accompanying drawings.Although showing this public affairs in attached drawing
The illustrative embodiments opened, it being understood, however, that may be realized in various forms the disclosure without the reality that should be illustrated here
The mode of applying is limited.It is to be able to thoroughly understand the disclosure on the contrary, providing these embodiments, and can be by this public affairs
The range opened is fully disclosed to those skilled in the art.
Embodiment according to the present utility model provides at a kind of organic stain disease of rotary-type electrode of cylinder with reference to Fig. 1-3
Manage device, including shell 1, water inlet 2 and water outlet 3, which is characterized in that the shell is cylinder type and forms reactive tank, instead
It answers and is equipped with rotation system in slot and connects electric system 4 and pad system 5, the rotation system includes the insulation that the heart within the barrel is arranged
Stirring shaft 40 and the insulation connecting with 40 bottom of insulation stirring shaft stir bearing, the height of the insulation stirring shaft 40 and institute
The height for stating cylinder is of substantially equal；It is described connect electric system include be enclosed in it is described insulation stirring shaft 40 connect electric bushing 41 and with
The electrode for connecing the electrical connection of electric bushing 41 connects fulgurite 42, and the pad system 5 includes the cylinder being arranged in the inner walls
Formula positive plate, from the rotation for connecing electric bushing and radiating outwardly extending 5 groups of pole plate load-bearing axles and being arranged in the pole plate load-bearing axle
Turn polar plate group, every group of pole plate load-bearing axle includes that the pole plate of 3 equidistant alignment settings holds load-bearing axle 43, and the pole plate load-bearing axle 43 is every
Root equal length and to cartridge type positive plate have a distance H, the rotation polar plate group by every group of pole plate load-bearing axle along cylinder diameter
It is formed to interval setting and with 5 layers of arc surface positive plate of insulation 40 coaxial line of stirring shaft and arc surface negative plate, also,
The arc surface positive plate being arranged in every group of pole plate load-bearing axle is identical with the number of plies of arc surface negative plate, identical, the interlamellar spacing phase of sequence
Deng and end be disposed as the arc surface negative plate opposite with cartridge type positive plate；In present embodiment, the rotation polar plate group packet
2 circular arc positive plates, 3 circular arc negative plates are included, the cartridge type positive plate and 2 circular arc positive plates are constituted just
Polar plate group system 51, the 3 circular arc negative plates constitute negative plate group system 52.Arc surface anode in every group of pole plate load-bearing axle
Plate and arc surface negative plate and the arc surface positive plate and arc surface negative plate on the corresponding level in adjacent sets pole plate load-bearing axle
Between be all provided with and have the gap.Interlamellar spacing is between arc surface positive plate and arc surface negative plate in all pole plate load-bearing axles
Distance H.Arc surface positive plate in each group pole plate load-bearing axle and the folder between the arc surface radial centre lines of arc surface negative plate
Angle is equal, is 72 degree in the embodiment as shown in Figure 1.The circular arc positive plate and circular arc negative plate are with grafting or welding side
Formula is connected with the pole plate load-bearing axle, and respectively connects fulgurite 42 with electrode and be electrically connected, in the embodiment, every pole plate load-bearing
Axis 42 includes that an electrode connects fulgurite 43, and the two parallel side-by-side is arranged, the electrode connect fulgurite 43, pole plate load-bearing axle 42 with
Grafting or welding manner connect electric bushing 41 with described in and are connected, and the electric bushing 41 that connects socket-connects with the insulation stirring shaft 40.
The shell is externally provided with positive plate and connects electric handle 50, and external power supply is powered to cartridge type positive plate；To connect electric bushing 40 external by described
Power supply is powered to the rotation polar plate group, and the positive board group energization in parallel with negative plate group difference.The positive plate
For titanium-based zinc doping lead dioxide electrode plate, the negative plate is the modified titanium pole plate of oxalic acid.
The water inlet 2 is arranged in the outside of the lower part of the housing, the water inlet direction of the water inlet 2 from the bottom to top, and
The inverse rotation direction in the rotation polar plate group；The edge of the case top is equipped with weir-type water outlet 30, goes out in the weir-type
The outer side-lower at the mouth of a river 30 is equipped with water outlet diversion trench 31, and the water outlet 3 is located at the outside of the water outlet diversion trench 31.
Further, the bottom of the shell is equipped with dreg removing system, and the dreg removing system includes slag-drip opening 6 and shut-off valve 60；
Be equipped with foam removal device (not shown) above the case top, the device include be parallel to the housing top surface rotation it is clear
Except scraper plate and for the connector that scraper plate is connected with the insulation rolling bearing to be removed in the rotation.
In the present embodiment, the plant bulk specification enumerated is as follows: the size of the cartridge type positive plate can for it is high by 400~
800mm, upper and lower 1 400~600mm of diameter of phi of circular cylindrical shell, and one is respectively welded in the lower edges of the cartridge type positive plate
The anode of a 80*30mm connects electric handle 50, and the anode connects electric handle 50 and is pierced by from the shell 1.Rotate the anode of polar plate group
The opposition setting parallel with negative plate group system 52 of board group system 51, positive/negative plate keep coaxial with one heart, are highly consistent；It is described
The spacing H of positive/negative plate and the cartridge type positive plate is consistent, and can be 10~50mm.The electrode connects fulgurite 42 and pole plate
Load-bearing axle 43 runs through positive and negative anodes board group, 50~100mm of diameter of phi with grafting or welding manner.
The preparation side for the titanium pole plate that wherein the positive plate titanium-based zinc doping lead dioxide electrode and negative plate oxalic acid are modified
Method is as follows with process:
Zr adulterates PbO2The preparation of electrode includes three parts: surface treatment, (two) electro-deposition of (one) Ti base electrode
The preparation of liquid, (three) Zr adulterate PbO2The preparation of coating.(1) surface treatment of Ti base electrode: with the coarse sand of 200~400 mesh
Then Ti base stage plate is polishing to by paper smoothly selects the fine sand paper polishing of 800 mesh or more to remove polar board surface oxide layer；It will polishing
The NaOH solution (m/m, 5%) that good Ti base stage plate is put into boiling impregnates 0.5~1h, contains oxalic acid (m/ in boiling after cleaning
M, 1%) 1~2h is impregnated in solution, is placed into the solution containing oxalic acid (m/m, 0.1%) and is impregnated spare, prevents Ti base stage
Plate secondary oxidation.Obtained pole plate is the modified titanium pole plate of oxalic acid.(2) preparation method of electrodeposit liquid: with deionized water
For solution, 100~200gL is added-1Plumbi nitras, 0.1~1.0gL-1Sodium fluoride, 0.1~4.0gL-1Zirconium nitrate selects nitric acid tune
Solution ph is saved to 2.0~2.5, is kept stirring under 60 DEG C of water baths until solution is sufficiently mixed.(3) Zr adulterates PbO2
Electrode preparation: using the Ti base stage plate handled well as anode, Ti base stage plate is as cathode, and 30~75 DEG C of depositing temperature, current density
For 10~30mA cm-2, sedimentation time is 0.5~2h, and pole plate spacing is 3~5cm, and remaining a constant speed during the deposition process, it is heavy to stir
Hydrops, mixing speed < 100rpm, and pay attention to clear up cathode surface generate lead simple substance to prevent tank voltage to be mutated, sedimentation time
After use deionized water cleaning electrode, can be prepared by after natural drying Zr doping PbO2Electrode.
The outside of 1 lower part of shell is arranged in the water inlet 2, and the water inlet direction of the water inlet 2 is from the bottom to top,
And the inverse rotation direction in the rotation polar plate group.The interior diameter of the water inlet 2 is 200~300mm, and the water inlet 2
Quantity be 1~2.The width of the water outlet diversion trench 31 is 150~200mm, the interior diameter of the water outlet 3 is 200~
300mm, the quantity of the water outlet 3 are 1~2.
The slag-drip opening 6 is to the waste residue that generates in wastewater treatment.It is equipped with shut-off valve 60 at the slag-drip opening 6, uses
To control the Push And Release of the slag-drip opening 6.The slag-drip opening 6 can take interval deslagging mode in reaction unit operational process,
And the treatment effeciency of the sample detection reactor, further to control.
In the present embodiment, the positive plate connects electric handle 50 and connects 42 external power supply power device of fulgurite, the power supply with electrode
Power device uses low-voltage dc power supply, and 0~50V of voltage is adjustable, and 0~3A of electric current is adjustable.The insulation rotation axis 40 with connect electricity
41 external power supply power device of casing, the mains power device use low pressure height stream DC power supply, and 0~50V of voltage is adjustable, electric current
0~200A is adjustable.
According to the present embodiment, a kind of method of organic stain disease of efficient process is provided, the sewage water treatment method is using upper
Reactor is stated to be efficiently treated through organic stain disease.Described method includes following steps:
Pre-processing device 7-1 is arranged, by organic dirt in S1 before the organic sewage and waste water treatment device of the rotary-type electrode of the cylinder
Waste water introduces the pre-processing device 7-1, and is adjusting the PH of water body between 5~9 in the pre-processing device 7-1, mistake
Filter adjusts water temperature to room temperature；
It is organic will to import the rotary-type electrode of the cylinder by water inlet 2 by the pretreated stain disease of S1 step by S2
Sewage and waste water treatment device 7-2 carries out degradation catalyzing, oxidizing and purifying processing to pollutant in water body in the reactor 7-2；
S2 step purge treated water body is collected by water outlet 3 by drainage equipment 7-3 by S3；Further mistake
It is discharged after filter；
It can be system power supply by power equipment 7-4 such as Fig. 4.
Comparative example 1
Using the organic sewage and waste water treatment device of the rotary-type electrode of the cylinder of the utility model above-described embodiment and tradition electrification
Oxidation unit is learned to handle the waste water containing high concentration perfluorinated sulfonic acid (PFOS).
1) conductivity of waste water >=1600 μ S/cm；
2) diving pump discharge is 2~4t/h；
3) voltage≤20V, electric current≤50mA/cm2；
4) bubble elimination device working frequency is 10~12 times/h.
Condition is not specified referring to Conventional electrochemical oxidation unit typical processing conditions in other.
Comparing result is shown in Table 1.
Table 1: conventional apparatus and the utility model reactor for treatment perfluorinated sulfonic acid (PFOS) waste water Comparative result
Comparative example 2
Using the organic sewage and waste water treatment device of the rotary-type electrode of the cylinder of the utility model above-described embodiment and tradition electrification
Oxidation unit is learned to handle sanitary sewage.
1) conductivity of waste water >=1200 μ S/cm；
2) diving pump discharge is 3~4t/h；
3) voltage≤20V, electric current≤50mA/cm2；
4) bubble elimination device working frequency is 12~15 times/h.
Condition is not specified referring to Conventional electrochemical oxidation unit typical processing conditions in other.
Comparing result is as follows:
Conventional electrochemical oxidation unit:
CODCr: 2571.4mg L-1It is down to 985.1mg L-1；
Ammonia nitrogen: 131.2mg L-1It is down to 29.5mg L-1；
Total phosphorus: 14.8mg L-1It is down to 7.4mg L-1；
The utility model reactor:
CODCr: 2571.4mg L-1It is down to 69.1mg L-1；
Ammonia nitrogen: 131.2mg L-1It is down to 7.8mg L-1；
Total phosphorus: 14.8mg L-1It is down to 2.1mg L-1；
By above-mentioned comparative example 1 and 2 as it can be seen that the perfluorinated sulfonic acid (PFOS) and sanitary sewage of same concentrations are handled, using this reality
More waste water are handled within the unit time than conventional apparatus with novel reactor, treatment effeciency is obviously improved, and energy consumption is decreased obviously.
In continuous operation, have no that anode plate surface organic carbon precipitates, and conventional apparatus is during continuous operation, treatment effeciency decline
Obviously, anode plate surface organic carbon deposit buildup.And through examining, ammonia-nitrogen content significantly reduces stain disease after treatment, this
The enhancing of utility model reactor for treatment significant effect, and operating status is good, plant maintenance is convenient.
The preferable specific embodiment of the above, only the utility model, but the protection scope of the utility model is not
It is confined to this, anyone skilled in the art within the technical scope disclosed by the utility model, can readily occur in
Change or replacement, should be covered within the scope of the utility model.Therefore, the protection scope of the utility model should be with
Subject to the scope of protection of the claims.
Claims (8)
1. a kind of organic sewage and waste water treatment device of rotary-type electrode of cylinder, which is characterized in that including shell, water inlet and water outlet
Mouthful, the shell is cylinder type and forms reactive tank, and rotation system is equipped in reactive tank, connects electric system and pad system, described
Rotation system includes the setting insulation stirring shaft of the heart and the insulation stirring shaft connecting with the insulation stirring shaft bottom within the barrel
It holds, the height of the insulation stirring shaft and the height of the cylinder are of substantially equal；It is described connect electric system be enclosed in it is described absolutely
Edge stirring shaft connects electric bushing and connects the electrode that electric bushing is electrically connected with described and connect fulgurite, and the pad system includes that setting exists
Cartridge type positive plate in the inner walls radiates outwardly extending several groups pole plate load-bearing axle and described from connecing electric bushing
The rotation polar plate group being arranged in pole plate load-bearing axle, every group of pole plate load-bearing axle include 1-5 root pole plate load-bearing axle, the pole plate load-bearing axle
Every equal length and to cartridge type positive plate have a distance H, the rotation polar plate group by every group of pole plate load-bearing axle along cylinder
Spaced radial is arranged and forms with the several layers arc surface positive plate of the insulation stirring shaft coaxial line and arc surface negative plate, and
And the arc surface positive plate being arranged in every group of pole plate load-bearing axle is identical with the number of plies of arc surface negative plate, the identical, interlamellar spacing of sequence
Equal and end is disposed as the arc surface negative plate opposite with cartridge type positive plate.
2. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that all poles
Interlamellar spacing is distance H between arc surface positive plate in plate load-bearing axle and arc surface negative plate.
3. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that every group of pole plate is held
Arc surface positive plate and arc surface negative plate on solid axle and the arc surface on the corresponding level in adjacent sets pole plate load-bearing axle are just
It is all provided with and has the gap between pole plate and arc surface negative plate.
4. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that each group pole plate is held
Angle between arc surface positive plate on solid axle and the arc surface radial centre lines of arc surface negative plate is equal.
5. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that the pole of rotation
Board group includes 2 arc surface positive plates, 3 arc surface negative plates, 5 groups of pole plate load-bearing axles and every group include 3 by
Up to the pole plate load-bearing axle of lower alignment setting, the arc surface positive plate and arc surface negative plate are with the same institute of grafting or welding manner
It states pole plate load-bearing axle to be connected, and respectively connects fulgurite with electrode and be electrically connected, every group of pole plate load-bearing axle includes at least one group of electrode and connect
Fulgurite, and the electrode connects fulgurite and at least one pole plate load-bearing axle parallel side-by-side is arranged, the electrode connects fulgurite, pole plate load-bearing
Axis connects electric bushing with described in grafting or welding manner and is connected, and the electric bushing that connects socket-connects with the insulation stirring shaft.
6. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that outside the shell
Electric handle is connect equipped with positive plate, external power supply is powered to cartridge type positive plate；Connect that electric bushing is connect described in fulgurite is external by the electrode
Power supply is powered to the rotation polar plate group, and the positive board group energization in parallel with negative plate group difference.
7. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that the positive plate
For titanium-based zinc doping lead dioxide electrode plate, the negative plate is the modified titanium pole plate of oxalic acid.
8. the organic sewage and waste water treatment device of the rotary-type electrode of cylinder as described in claim 1, which is characterized in that the water inlet
The outside of the lower part of the housing is set, and the water inlet direction of the water inlet is from the bottom to top, and inverse in the rotation polar plate group
Rotation direction；The edge of the case top is equipped with weir-type water outlet, is equipped with water outlet in the outer side-lower of the weir-type water outlet
Diversion trench, the water outlet are located at the outside of the water outlet diversion trench.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822031135.0U CN209322529U (en) | 2018-12-04 | 2018-12-04 | A kind of organic sewage and waste water treatment device of rotary-type electrode of cylinder |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822031135.0U CN209322529U (en) | 2018-12-04 | 2018-12-04 | A kind of organic sewage and waste water treatment device of rotary-type electrode of cylinder |
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| CN209322529U true CN209322529U (en) | 2019-08-30 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336226A (en) * | 2018-12-04 | 2019-02-15 | 江苏智诚达环保科技有限公司 | A kind of rotation electrode reactor and organic stain disease processing method |
| CN110731367A (en) * | 2019-10-28 | 2020-01-31 | 江苏经贸职业技术学院 | High-pressure plasma sterilization device for kinds of meat products |
-
2018
- 2018-12-04 CN CN201822031135.0U patent/CN209322529U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336226A (en) * | 2018-12-04 | 2019-02-15 | 江苏智诚达环保科技有限公司 | A kind of rotation electrode reactor and organic stain disease processing method |
| CN110731367A (en) * | 2019-10-28 | 2020-01-31 | 江苏经贸职业技术学院 | High-pressure plasma sterilization device for kinds of meat products |
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