CN207175600U - A kind of pre- fouling apparatus for eliminating sludge of electrolytic - Google Patents
A kind of pre- fouling apparatus for eliminating sludge of electrolytic Download PDFInfo
- Publication number
- CN207175600U CN207175600U CN201721711394.7U CN201721711394U CN207175600U CN 207175600 U CN207175600 U CN 207175600U CN 201721711394 U CN201721711394 U CN 201721711394U CN 207175600 U CN207175600 U CN 207175600U
- Authority
- CN
- China
- Prior art keywords
- tank
- anodes
- electrolytic cell
- negative electrodes
- scraper device
- 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
It the utility model is related to a kind of pre- fouling apparatus for eliminating sludge of electrolytic.It can be such that the zwitterion of pipeline internal medium adsorbs respectively, in advance in electrode fouling, periodic cleaning, reduce the fouling condition in pipeline.The technical solution of the utility model includes electrolytic cell A, electrolytic cell B；Tank A anodes and tank A negative electrodes are laid with described electrolytic cell A, the both positive and negative polarity of tank A anodes and tank A negative electrodes respectively with high-frequency electrolysis power supply is connected, tank B anodes and tank B negative electrodes are laid with described electrolytic cell B, the both positive and negative polarity of tank B anodes and tank B negative electrodes respectively with high-frequency electrolysis power supply is connected, described scraper device A is connected with tank A anodes and tank A negative electrodes and can slided on tank A anodes and tank A negative electrodes, and described scraper device B is connected with tank B anodes and tank B negative electrodes and can slided on tank B anodes and tank B negative electrodes；Feed tube, drain pipe and sewage draining exit are connected on described electrolytic cell A and electrolytic cell B.
Description
Technical field
It the utility model is related to a kind of pre- fouling apparatus for eliminating sludge of electrolytic.
Background technology
Oil field sewage, profit, crude oil etc. conveying in, using inside pipe wall after a period of time due to conveying liquid in negative and positive from
Son reaction, deposition form dirt so that steel pipe aperture reduces, and transporting resistance increase, conveying capacity reduces, it is necessary to steel pipe inner wall
Carry out dirty removing processing.In current pipeline scale removal work progress, mainly carried out using chemical dosing and mechanical descaling, both sides
Formula has the following disadvantages：
1. chemical dosing method scale removal is acids or the alkali electroless examination from Suitable formulations according to the chemical composition of dirty layer
Agent dissolves into the interim scale removal of row.It is the method that one or more of chemical agents remove dirt in pipeline, by cleaning agent pair
Body surface pollutant or coverage rate carry out chemical conversion, dissolving, stripping to reach the effect of scale removal and decontamination.Its shortcoming is rotten
Erosion reduces the service life of pipeline, and the waste liquid of cleaning causes to environment necessarily to be polluted, it is necessary to put into a large amount of manpowers and medicament
Expense.
2. mechanical system scale removal is hydraulically to promote wiper to be moved forward in pipeline, the scraper on wiper is dirt
Wipe off.Its shortcoming is to need to stop pipeline work to carry out constructing operation, and the easy blocking of wiper causes the accident in pipeline, applies
Work cost is high.
Utility model content
Fouling is serious in pipeline in order to solve in the pipelines such as crude oil, sewage for the utility model, susceptible to plugging to ask
Topic, there is provided a kind of pre- fouling apparatus for eliminating sludge of electrolytic, it can be such that the zwitterion of pipeline internal medium adsorbs respectively, in advance in electrode
Fouling, periodic cleaning, reduce the fouling condition in pipeline.
To solve the problems, such as that prior art is present, the technical solution of the utility model is：A kind of pre- fouling scale removal of electrolytic
Device, it is characterised in that：Including electrolytic cell A, electrolytic cell B, high-frequency electrolysis power supply, scraper device A and scraper device B；
Be laid with tank A anodes and tank A negative electrodes in described electrolytic cell A, tank A anodes and tank A negative electrodes respectively with high-frequency electrolysis
The both positive and negative polarity connection of power supply, is laid with tank B anodes and tank B negative electrodes in described electrolytic cell B, tank B anodes and tank B negative electrodes respectively with
The both positive and negative polarity connection of high-frequency electrolysis power supply, described scraper device A be connected with tank A anodes and tank A negative electrodes and can in tank A anodes and
Slided on tank A negative electrodes, described scraper device B is connected with tank B anodes and tank B negative electrodes and can slided on tank B anodes and tank B negative electrodes
It is dynamic；Feed tube, drain pipe and sewage draining exit are connected on described electrolytic cell A and electrolytic cell B.
Described scraper device A is identical with scraper device B structure, by guide plate, scrapes dirty ring gear and lift cylinder group
Into；Described dirty ring gear of scraping is provided with two, is embedded on guide plate, and the piston rod of lift cylinder is vertical with guide plate to be set
Put；
Two of scraper device A scrape dirty ring gear and are sheathed on respectively on tank A anodes and tank A negative electrodes；
Two of scraper device B scrape dirty ring gear and are sheathed on tank B anodes and tank B negative electrodes respectively.
Tank A inlet valves and tank B inlet valves are respectively arranged with described electrolytic cell A and electrolytic cell B feed tube.
Tank A outlet valves and tank B outlet valves are respectively arranged with described electrolytic cell A and electrolytic cell B drain pipe.
Tank A blowoff valves and tank B blowoff valves are respectively arranged with described electrolytic cell A and electrolytic cell B liquid outlet.
The current regulation of described high-frequency electrolysis power supply is in the range of 8~30A.
Compared with prior art, it is as follows the advantages of the utility model：
1. the utility model, by being electrolysed, the incrustation ion in water is deposited in cathode surface and is removed in advance, electrolysis is anti-
The operating current for remaining certain in room is answered, the hydroxide ion of high concentration is formed about in negative electrode, this environment allows easy fouling
The advance fouling of mineral matter, and being separated out from water, is adsorbed on electrode, is struck off by striking off system and discharged；
2. the utility model is in the presence of electric field, the increased activity of water, active water is become by general water, due to moisture
The dipole moment increase of son increases the hydratability of it and the positive and negative ion of salt, increases the solubility of water, accelerates dirty in water
Solvability, serve the purpose of scale removal, antiscale.
Brief description of the drawings
Fig. 1 is the utility model structure diagram；
Fig. 2 is scraper device B facade structures figures in the utility model；
Fig. 3 is scraper device B plane structure charts in the utility model；
1- feed tubes, 2- tank B inlet valves, 3- tank A inlet valves, 4- electrolytic cells B, 5- high-frequency electrolysis power supply, 6- electrolytic cell A,
7- tank B anodes, 8- tank A anodes, 9- scraper devices A, 10- scraper device B, 11- tank A negative electrodes, 12- tank B negative electrodes, 13- tank A blowdowns
Valve, 14- tank B blowoff valves, 15- tank A outlet valves, 16- tank B outlet valves, 17- drain pipes, 18- guide plates, 19- scrape dirty ring gear, 20-
Lift cylinder.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining
The utility model, it is not used to limit the utility model.
The present embodiment provides a kind of pre- fouling apparatus for eliminating sludge of electrolytic（Referring to Fig. 1）, including feed tube 1, tank B inlet valves 2,
Tank A inlet valves 3, electrolytic cell B4, high-frequency electrolysis power supply 5, electrolytic cell A6, tank B anodes 7, tank A anodes 8, scraper device A9, scrape dirt
Device B10, tank A negative electrodes 11, tank B negative electrodes 12, tank A blowoff valves 13, tank B blowoff valves 14, tank A outlet valves 15, tank B outlet valves 16,
Drain pipe 17.
Be laid with tank A anodes 8 and tank A negative electrodes 11 in described electrolytic cell A6, tank A anodes 8 and tank A negative electrodes 11 respectively with height
The both positive and negative polarity of frequency electrolysis power 5 is connected, and tank B anodes 7 and tank B negative electrodes 12, the He of tank B anodes 7 are laid with described electrolytic cell B4
Tank B 12 both positive and negative polarities respectively with high-frequency electrolysis power supply 5 of negative electrode are connected, described scraper device A9 and tank A anodes 8 and tank A negative electrodes
11 connect and can be slided on tank A anodes 8 and tank A negative electrodes 11, described scraper device B10 and tank B anodes 7 and tank B negative electrodes 12
Connect and can be slided on tank B anodes 7 and tank B negative electrodes 12；Feed liquor is connected on described electrolytic cell A6 and electrolytic cell B4
Pipe 1, drain pipe 17 and sewage draining exit.
Described scraper device A9 is identical with scraper device B10 structure, by guide plate 18, scrapes dirty ring gear 19 and lifting
Cylinder 20 forms；Described dirty ring gear 19 of scraping is provided with two, is embedded on guide plate 18, the piston rod of lift cylinder 20 with
Guide plate 18 is vertically arranged；
Two of scraper device A9 scrape dirty ring gear 19 and are sheathed on respectively on tank A anodes 8 and tank A negative electrodes 11；
Two of scraper device B10 scrape dirty ring gear 19 and are sheathed on tank B anodes 7 and tank B negative electrodes 12 respectively.
Lift cylinder 20 is fixed on electrolytic cell B4, and pole type tank B anodes 7 and tank B negative electrodes 12 are installed on and scrape dirty ring gear 19
It is interior.
Guide plate 18 and scrape dirty ring gear 19 in the presence of the piston rod of lift cylinder 20 and can move up and down, by scraping dirty tooth
Ring 19 moves up and down scrapes discharge, scraper device A9 knots the fouling on tank B anodes 7 and tank B negative electrodes 12 and adion object
Structure action is identical with this.
Tank A inlet valves 3 and tank B inlet valves 2 are respectively arranged with described electrolytic cell A6 and electrolytic cell B4 feed tube.
Tank A outlet valves 15 and tank B outlet valves 16 are respectively arranged with described electrolytic cell A6 and electrolytic cell B4 drain pipe.
Tank A blowoff valves 13 and tank B blowoff valves 14 are respectively arranged with described electrolytic cell A6 and electrolytic cell B4 liquid outlet.
The course of work of the present utility model：During normal work, two electrolytic cells work simultaneously, tank A inlet valves 3, tank A outlets
Valve 15, tank B inlet valves 2, tank B outlet valves 16 are opened simultaneously, and tank A blowoff valves 13 and tank B blowoff valves 14 are closed.High-frequency electrolysis power supply
5 are powered, and both positive and negative polarity is connected with tank A anodes 8, tank A negative electrodes 11, tank B anodes 7, tank B negative electrodes 12 respectively, and current regulation is in 8~30A
Between, the anion CL in medium solution-、CO3 2-、SO4 2-Absorption is in anode, Ca2+、Mg2+、Fe2+、Ba2+、Sr2+Inhaled Deng cation
It is attached to negative electrode and produces anionic reactive fouling with catholyte, is separated out from solution and be deposited on cathode surface.
After being electrolysed work for a period of time, tank A inlet valves 3, tank A outlet valves 15 are closed respectively successively, open tank A blowoff valves
13, scraper device A9 are slided and the scale-forming ion on tank A anodes 8, tank A negative electrodes 11 are scraped, and are excluded by tank A blowoff valves 13, tank B
Operate identical.
It is described above, preferred embodiment only of the present utility model, it is not intended to limit protection of the present utility model
Scope, every equivalent structure change done using specification of the present utility model and accompanying drawing content, should be included in practical new
In the scope of patent protection of type.
Claims (6)
- A kind of 1. pre- fouling apparatus for eliminating sludge of electrolytic, it is characterised in that：Including electrolytic cell A（6）, electrolytic cell B（4）, high-frequency electrolysis Power supply（5）, scraper device A（9）With scraper device B（10）；Described electrolytic cell A（6）Inside it is laid with tank A anodes（8）With tank A negative electrodes（11）, tank A anodes（8）With tank A negative electrodes（11）Point Not with high-frequency electrolysis power supply（5）Both positive and negative polarity connection, described electrolytic cell B（4）Inside it is laid with tank B anodes（7）With tank B negative electrodes （12）, tank B anodes（7）With tank B negative electrodes（12）Respectively with high-frequency electrolysis power supply（5）Both positive and negative polarity connection, described scraper device A （9）With tank A anodes（8）With tank A negative electrodes（11）Connection simultaneously can be in tank A anodes（8）With tank A negative electrodes（11）Upper slip, described scrapes Dirty device B（10）With tank B anodes（7）With tank B negative electrodes（12）Connection simultaneously can be in tank B anodes（7）With tank B negative electrodes（12）Upper slip； Described electrolytic cell A（6）With electrolytic cell B（4）On be connected to feed tube（1）, drain pipe（17）And sewage draining exit.
- A kind of 2. pre- fouling apparatus for eliminating sludge of electrolytic according to claim 1, it is characterised in that：Described scraper device A （9）With scraper device B（10）Structure it is identical, by guide plate（18）, scrape dirty ring gear（19）And lift cylinder（20）Composition；Institute That states scrapes dirty ring gear（19）Two are provided with, is embedded in guide plate（18）On, lift cylinder（20）Piston rod and guide plate （18）It is vertically arranged；Scraper device A（9）Two scrape dirty ring gear（19）Tank A anodes are sheathed on respectively（8）With tank A negative electrodes（11）On；Scraper device B（10）Two scrape dirty ring gear（19）Tank B anodes are sheathed on respectively（7）With tank B negative electrodes（12）.
- A kind of 3. pre- fouling apparatus for eliminating sludge of electrolytic according to claim 1 or 2, it is characterised in that：Described electrolytic cell A （6）With electrolytic cell B（4）Feed tube on be respectively arranged with tank A inlet valves（3）With tank B inlet valves（2）.
- A kind of 4. pre- fouling apparatus for eliminating sludge of electrolytic according to claim 3, it is characterised in that：Described electrolytic cell A（6） With electrolytic cell B（4）Drain pipe on be respectively arranged with tank A outlet valves（15）With tank B outlet valves（16）.
- A kind of 5. pre- fouling apparatus for eliminating sludge of electrolytic according to claim 4, it is characterised in that：Described electrolytic cell A（6） With electrolytic cell B（4）Liquid outlet on be respectively arranged with tank A blowoff valves（13）With tank B blowoff valves（14）.
- A kind of 6. pre- fouling apparatus for eliminating sludge of electrolytic according to claim 5, it is characterised in that：Described high-frequency electrolysis electricity Source（5）Current regulation in the range of 8~30A.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721711394.7U CN207175600U (en) | 2017-12-11 | 2017-12-11 | A kind of pre- fouling apparatus for eliminating sludge of electrolytic |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721711394.7U CN207175600U (en) | 2017-12-11 | 2017-12-11 | A kind of pre- fouling apparatus for eliminating sludge of electrolytic |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207175600U true CN207175600U (en) | 2018-04-03 |
Family
ID=61745803
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721711394.7U Active CN207175600U (en) | 2017-12-11 | 2017-12-11 | A kind of pre- fouling apparatus for eliminating sludge of electrolytic |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207175600U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111675364A (en) * | 2020-06-22 | 2020-09-18 | 江西省萍乡市迪尔化工填料有限公司 | Coking wastewater electrolysis device |
| CN113941567A (en) * | 2020-07-15 | 2022-01-18 | 湖南中天青鼎工程科技股份有限公司 | Drainage pipeline scale inhibition and removal method for phosphogypsum tailings recycling |
-
2017
- 2017-12-11 CN CN201721711394.7U patent/CN207175600U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111675364A (en) * | 2020-06-22 | 2020-09-18 | 江西省萍乡市迪尔化工填料有限公司 | Coking wastewater electrolysis device |
| CN113941567A (en) * | 2020-07-15 | 2022-01-18 | 湖南中天青鼎工程科技股份有限公司 | Drainage pipeline scale inhibition and removal method for phosphogypsum tailings recycling |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203498136U (en) | Progressive three-stage electrochemical water treatment equipment | |
| CN209367873U (en) | A kind of automatic desludging device for electrochemical water preparation | |
| CN106745832B (en) | High-pressure water-flushing type rotary circulating water electrolysis descaling device and descaling method | |
| CN107555547B (en) | Coking wastewater electrolysis device with back flush function | |
| CN104787842B (en) | A kind of model electrochemical/photocatalysis circulating water cooling treatment equipment | |
| CN207175600U (en) | A kind of pre- fouling apparatus for eliminating sludge of electrolytic | |
| CN211644716U (en) | Rotary descaling device with functions of descaling, electrolysis, sterilization and descaling | |
| CN104211235B (en) | A kind of method of electrochemistry incrustation scale removal device and removal incrustation scale | |
| CN104291450B (en) | A kind of electrochemistry incrustation scale removal device | |
| CN105923797A (en) | Full automatic descaling and sterilizing device for water body with high flow | |
| CN107512805A (en) | A kind of coking chemical waste water electrolysis unit that can extend electrode life | |
| CN203545745U (en) | Gradual secondary electrochemical water treatment equipment | |
| CN105540955A (en) | Electrochemical descaling device | |
| CN112110577A (en) | System and method for chlorine and scale removal by combining electrochemistry and ozone | |
| CN203498137U (en) | Progressive four-stage electrochemical water treatment equipment | |
| CN201770515U (en) | Sewage purifying and descaling equipment adopting electrode adsorption and ultrasonic wave combination | |
| CN108455711B (en) | Circulating water sterilization electrolysis descaling system | |
| CN106315870B (en) | A kind of industrial circulating cooling water sterilization hardness removing device and processing method | |
| CN110563165A (en) | electrochemistry circulating cooling water purification installation | |
| CN204198499U (en) | A kind of electrochemistry incrustation scale removal device | |
| CN210122500U (en) | Rotary electrochemical circulating water treatment device | |
| CN108911055A (en) | A kind of electrochemistry sewage-treatment plant and its electrode cleaning mechanism | |
| CN214634267U (en) | Mud scraping device of sewage sedimentation tank | |
| CN202576054U (en) | Three-dimensional electrode reaction device | |
| CN104229954B (en) | A kind of automatic descaling type electro adsorption technology |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |