CN206720929U - Electrochemical composite type chlorine dioxide water treatment facilities - Google Patents
Electrochemical composite type chlorine dioxide water treatment facilities Download PDFInfo
- Publication number
- CN206720929U CN206720929U CN201720374906.9U CN201720374906U CN206720929U CN 206720929 U CN206720929 U CN 206720929U CN 201720374906 U CN201720374906 U CN 201720374906U CN 206720929 U CN206720929 U CN 206720929U
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- CN
- China
- Prior art keywords
- chlorine dioxide
- reaction tube
- electrochemical
- composite type
- water treatment
- 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.)
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- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 title claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 239000004155 Chlorine dioxide Substances 0.000 title claims abstract description 25
- 235000019398 chlorine dioxide Nutrition 0.000 title claims abstract description 25
- 239000002131 composite material Substances 0.000 title claims abstract description 13
- 238000006243 chemical reaction Methods 0.000 claims abstract description 31
- 239000007788 liquid Substances 0.000 claims abstract description 11
- 238000003487 electrochemical reaction Methods 0.000 claims abstract description 10
- 239000003814 drug Substances 0.000 claims abstract description 9
- 239000012528 membrane Substances 0.000 claims abstract description 8
- 238000004891 communication Methods 0.000 claims abstract description 4
- 230000005540 biological transmission Effects 0.000 claims description 8
- 230000008602 contraction Effects 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 4
- 239000003818 cinder Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 10
- 238000005260 corrosion Methods 0.000 abstract description 7
- 238000012545 processing Methods 0.000 abstract description 7
- 238000004140 cleaning Methods 0.000 abstract description 6
- 241000195493 Cryptophyta Species 0.000 abstract description 4
- 230000033228 biological regulation Effects 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 4
- 230000005764 inhibitory process Effects 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 3
- 239000013049 sediment Substances 0.000 abstract description 3
- 230000001954 sterilising effect Effects 0.000 abstract description 3
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 3
- 238000013461 design Methods 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 3
- 239000000645 desinfectant Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model belongs to water-treatment technology field.A kind of electrochemical composite type chlorine dioxide water treatment facilities, including hydraulic pipeline, electrochemical reaction component and chlorine dioxide dosing component, the electrochemical reaction component includes reaction tube, electrode column, negative pole sleeve pipe, NF membrane, water inlet and delivery port and the slag-drip opening for being arranged on reaction tube bottom；The chlorine dioxide dosing component includes the connection cylindrical shell being arranged on hydraulic pipeline and the medicine liquid tank set with housing by loading pipeline communication.The utility model has the effect of good antiscaling, descaling, sterilization algae removal and inhibition anti-corrosion, can play preferable energy-saving and water-saving effect, while is easy to the cleaning and maintenance of equipment, is easy to cleaning and processing to sediment, avoids secondary pollution；Chlorine dioxide dosing component in the application, Venturi effect can be used, realizes negative pressure autofeed, with reference to the control of conductivity sensor and flow sensor, Reasonable Regulation And Control dosage.
Description
Technical field
The utility model belongs to water-treatment technology field, and in particular to a kind of electrochemical composite type chlorine dioxide water process dress
Put.
Background technology
Recirculated water after usage, Ca2+, Mg2+, HCO3-, SO42-, Cl- plasma in water, dissolved solid and suspension
Thing accordingly increases, pollutants in air such as dust, debris and heat exchanger material from leakage etc., can enter circulating cooling water system
System, makes the equipment and corrosion of piping in circulating water water system, water makes institute's saliferous in water in cyclic process by evaporation
Class concentrates, and just produces the scale problems of cooling system, while the warm and humid environmental benefits of circulation are in the growth of bacterium algae.Ask above
Topic can cause the reduction of heat exchanger heat transfer efficiency, cross water section face and reduce, or even equipment and pipeline corrosion is perforated.Circulating cooling water system
Fouling, corrosion and microbial reproduction in system are to be mutually related, and dirt and microorganism viscosity mud can cause underdeposit corrosion, and rotten
Erosion product forms dirt again, to solve these problems of recirculating cooling water system, it is necessary to carry out the comprehensive regulation.
In addition need to be passed through disinfectant during circulating water treatment, and the size of the intake of disinfectant directly determines water
The quality of processing, therefore the addition for disinfectant needs rationally control.
The content of the invention
The purpose of this utility model is to be directed to above-mentioned problem and shortage, there is provided it is a kind of reasonable in design, compact,
Electrochemical composite type processing effectively can be carried out to recirculated water, ensure water quality, improve the stability for the treatment of effeciency and whole equipment
Electrochemical composite type chlorine dioxide water treatment facilities.
To reach above-mentioned purpose, adopted the technical scheme that：
A kind of electrochemical composite type chlorine dioxide water treatment facilities, including hydraulic pipeline, be sequentially communicated and be arranged on hydraulic pipeline
On electrochemical reaction component and chlorine dioxide dosing component, the electrochemical reaction component include reaction tube, be arranged on reaction
Cylinder in electrode column, be arranged on reaction tube inwall negative pole sleeve pipe, be arranged in the middle part of reaction tube NF membrane, be separately positioned on
Water inlet and delivery port and the slag-drip opening for being arranged on reaction tube bottom above and below NF membrane in the reaction tube side wall of both sides, institute
State and be provided with lid at the top of reaction tube, electric cabinet is provided with upper lid, electrode column is connected by positive pole power transmission line with electric cabinet, institute
Negative pole sleeve pipe is stated to be connected with electric cabinet by negative pole power transmission line；The chlorine dioxide dosing component is arranged on water-supply-pipe including connection
Cylindrical shell on road and the medicine liquid tank set with housing by loading pipeline communication, the housing are included positioned at middle part
Contraction section and the expansion segment positioned at both ends, the liquid inlet joint connected with medicine liquid tank is provided with the outer wall of the contraction section；Follow
Ring current direction, support frame is provided with the expansion segment inwall of rear end, is pivotally connected on support frame and is provided with disturbance impeller, before being located at
Conductivity sensor and flow sensor are provided with the expansion segment at end, is provided with flow control valve on the loading pipeline, institute
State the flow that conductivity sensor and flow sensor control flow control valve by control system.
Middle rotating shaft and drive mechanism are provided with the upper lid, middle rotating shaft bottom is provided with scraper plate, the scraper plate and reaction
The inwall matching fitting of cylinder bottom.
Two branch lines are provided with the loading pipeline, flow control valve is provided with two branch lines, wherein
Delivery pump is provided with and communicated with one branch line.
The slag-drip opening is connected with filter press.
2 ~ 4 electrode columns are provided with the reaction tube.
Using above-mentioned technical proposal, acquired beneficial effect is：
The utility model is reasonable in design, and it has good antiscale by the structure design of electrochemical reaction component
The effect of scale removal, sterilization algae removal and inhibition anti-corrosion, preferable energy-saving and water-saving effect can be played, while be easy to the cleaning of equipment
And maintenance, it is easy to the cleaning and processing to sediment, avoids secondary pollution；Chlorine dioxide dosing component in the application, can
Using Venturi effect, negative pressure autofeed is realized, with reference to the control of conductivity sensor and flow sensor, Reasonable Regulation And Control is given
Dose, the water quality after guarantee processing meet the requirements, and meet production and the living needs of next step.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of the chlorine dioxide dosing component in Fig. 1.
Sequence number in figure：10 it is hydraulic pipeline, 20 be chlorine dioxide dosing component, 201 be housing, 202 is medicine liquid tank, 203
It is expansion segment for contraction section, 204,205 be liquid inlet joint, 206 be support frame, 207 be disturbance impeller, 208 is conductivity sensors
Device, 209 be flow sensor, 210 flow control valves, 211 be delivery pump, 30 be electrochemical reaction component, 301 be reaction tube,
302 it is electrode column, 303 be negative pole sleeve pipe, 304 be NF membrane, 305 be water inlet, 306 be delivery port, 307 is slag-drip opening, 308
For it is upper lid, 309 be electric cabinet, 310 be positive pole power transmission line, 311 be negative pole power transmission line, 312 be middle rotating shaft, 313 be drive mechanism,
314 be scraper plate.
Embodiment
Specific embodiment of the present utility model is elaborated below in conjunction with accompanying drawing.
Referring to Fig. 1 and Fig. 2, a kind of electrochemical composite type chlorine dioxide water treatment facilities of the utility model, including hydraulic pipeline
10th, the electrochemical reaction component 30 being arranged on hydraulic pipeline and chlorine dioxide dosing component 20, the electrochemistry are sequentially communicated
Reaction component 30 includes reaction tube 301, the electrode column 302 being arranged in reaction tube, the negative pole set being arranged on reaction tube inwall
Pipe 303, the NF membrane 304 being arranged in the middle part of reaction tube, it is separately positioned on NF membrane entering in the reaction tube side wall of both sides up and down
The mouth of a river 305 and delivery port 306 and the slag-drip opening 307 for being arranged on reaction tube bottom, the reaction tube top are provided with lid
308, electric cabinet 309 is provided with upper lid, and electrode column is connected by positive pole power transmission line 310 with electric cabinet, and the negative pole sleeve pipe leads to
Negative pole power transmission line 311 is crossed to be connected with electric cabinet；The chlorine dioxide dosing component includes the post that connection is arranged on hydraulic pipeline
Shape housing 201 and the medicine liquid tank 202 set with housing by loading pipeline communication, the housing include the receipts positioned at middle part
Contracting section 203 and the expansion segment 204 positioned at both ends, the liquid inlet joint connected with medicine liquid tank is provided with the outer wall of the contraction section
205；Along circulation current direction, support frame 206 is provided with the expansion segment inwall of rear end, is pivotally connected on support frame and is provided with disturbance
Impeller 207, is provided with conductivity sensor 208 and flow sensor 209 on the expansion segment of front end, on the loading pipeline
Flow control valve 210 is provided with, the conductivity sensor and flow sensor control flow control valve by control system
Flow.
Middle rotating shaft 312 and drive mechanism 313 are provided with the upper lid, middle rotating shaft bottom is provided with scraper plate 314, described to scrape
Plate is bonded with the inwall matching of reaction tube bottom.
In the present embodiment, two branch lines are provided with its loading pipeline, flow is provided with two branch lines
Control valve, wherein delivery pump 211 is provided with and communicated with a branch line, so as to enter automatically by Venturi effect negative pressure
It medicine, can also be pumped, be used according to different sewage disposal types and Xining selection, the slag-drip opening is connected with pressure by active
Filter, 2 ~ 4 electrode columns are provided with reaction tube.
The utility model is reasonable in design, and it has good antiscale by the structure design of electrochemical reaction component
The effect of scale removal, sterilization algae removal and inhibition anti-corrosion, preferable energy-saving and water-saving effect can be played, while be easy to the cleaning of equipment
And maintenance, it is easy to the cleaning and processing to sediment, avoids secondary pollution；Chlorine dioxide dosing component in the application, can
Using Venturi effect, negative pressure autofeed is realized, with reference to the control of conductivity sensor and flow sensor, Reasonable Regulation And Control is given
Dose, the water quality after guarantee processing meet the requirements, and meet production and the living needs of next step.
General principle, principal character and the advantages of the present invention of the present invention has been shown and described above.The technology of the industry
For personnel it should be appreciated that the present invention is not limited to the above embodiments, that described in above-described embodiment and specification is the present invention
Principle, various changes and modifications of the present invention are possible without departing from the spirit and scope of the present invention, these change and
Improvement is both fallen within the range of claimed invention.The protection domain of application claims by appended claims and its
Equivalent defines.
Claims (5)
- A kind of 1. electrochemical composite type chlorine dioxide water treatment facilities, it is characterised in that：Including hydraulic pipeline, it is sequentially communicated and is arranged on Electrochemical reaction component and chlorine dioxide dosing component on hydraulic pipeline, the electrochemical reaction component include reaction tube, set The negative pole sleeve pipe that put the electrode column in reaction tube, is arranged on reaction tube inwall, the NF membrane being arranged in the middle part of reaction tube, point Water inlet and delivery port and the row that is arranged on reaction tube bottom of the NF membrane up and down in the reaction tube side wall of both sides are not arranged on Cinder notch, the reaction tube top are provided with lid, electric cabinet are provided with upper lid, electrode column passes through positive pole power transmission line and electric cabinet Connection, the negative pole sleeve pipe are connected by negative pole power transmission line with electric cabinet；The chlorine dioxide dosing component includes connection and set Cylindrical shell on hydraulic pipeline and the medicine liquid tank set with housing by loading pipeline communication, the housing include position Contraction section in middle part and the expansion segment positioned at both ends, the feed liquor connected with medicine liquid tank is provided with the outer wall of the contraction section and is connect Head；Along circulation current direction, support frame is provided with the expansion segment inwall of rear end, is pivotally connected on support frame and is provided with disturbance leaf Wheel, conductivity sensor and flow sensor are provided with the expansion segment of front end, flow is provided with the loading pipeline Control valve, the conductivity sensor and flow sensor control the flow of flow control valve by control system.
- 2. electrochemical composite type chlorine dioxide water treatment facilities according to claim 1, it is characterised in that：Set on the upper lid Middle rotating shaft and drive mechanism are equipped with, middle rotating shaft bottom is provided with scraper plate, and the scraper plate is bonded with the inwall matching of reaction tube bottom.
- 3. electrochemical composite type chlorine dioxide water treatment facilities according to claim 1, it is characterised in that：The loading pipeline On be provided with two branch lines, be provided with flow control valve on two branch lines, wherein on a branch line connect set There is delivery pump.
- 4. electrochemical composite type chlorine dioxide water treatment facilities according to claim 1, it is characterised in that：The slag-drip opening connects It is connected to filter press.
- 5. electrochemical composite type chlorine dioxide water treatment facilities according to claim 1, it is characterised in that：In the reaction tube It is provided with 2 ~ 4 electrode columns.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720374906.9U CN206720929U (en) | 2017-04-11 | 2017-04-11 | Electrochemical composite type chlorine dioxide water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720374906.9U CN206720929U (en) | 2017-04-11 | 2017-04-11 | Electrochemical composite type chlorine dioxide water treatment facilities |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206720929U true CN206720929U (en) | 2017-12-08 |
Family
ID=60504248
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720374906.9U Expired - Fee Related CN206720929U (en) | 2017-04-11 | 2017-04-11 | Electrochemical composite type chlorine dioxide water treatment facilities |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206720929U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110542021A (en) * | 2019-01-29 | 2019-12-06 | 深圳海油工程水下技术有限公司 | Submarine pipeline medicament injection device and method |
-
2017
- 2017-04-11 CN CN201720374906.9U patent/CN206720929U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110542021A (en) * | 2019-01-29 | 2019-12-06 | 深圳海油工程水下技术有限公司 | Submarine pipeline medicament injection device and method |
| CN110542021B (en) * | 2019-01-29 | 2021-08-13 | 深圳海油工程水下技术有限公司 | Submarine pipeline medicament injection device and method |
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Legal Events
| 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: 20171208 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |