CN206173054U - Be applied to electrochemistry scale removal device that circulating water can automatic snaking - Google Patents
Be applied to electrochemistry scale removal device that circulating water can automatic snaking Download PDFInfo
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- CN206173054U CN206173054U CN201621168932.8U CN201621168932U CN206173054U CN 206173054 U CN206173054 U CN 206173054U CN 201621168932 U CN201621168932 U CN 201621168932U CN 206173054 U CN206173054 U CN 206173054U
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- water
- minus plate
- casing
- anode
- recirculated water
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Abstract
The utility model discloses a be applied to electrochemistry scale removal device that circulating water can automatic snaking, it includes: box, anode screen, negative plate, the dirty device of collection, DC power supply, control system, collect dirty device and install in the box lower part, and communicate with each other with the export of the reacting chamber of box, anode screen, negative plate are installed in the reacting chamber of box, anode screen, negative plate electric connection in DC power supply, DC power supply is provided with the auto -change over device of changeable positive negative pole orientation, and this auto -change over device connects in control system, the reacting chamber of box is provided with pending water input port, collects dirty device and is provided with processing back water delivery outlet and incrustation scale export. The utility model discloses can discharge aquatic calcium magnesium ion precipitate form, reduce circulating water hardness, the positive pole can produce the chlorine, free radical of strong oxidizing property etc. Simultaneously, and steerable aquatic algae growth has the algae removal of disinfecting function.
Description
Technical field
The utility model is related to circulating water treatment electrochemical treatments technology and water saving field, is applied to more particularly, to one kind
Recirculated water can automatic scale-cleaning electrochemical descaling device.
Background technology
It is addition slow-release scale inhibitor, bactericide that at present cooling circulating water processes conventional method, and by regular moisturizing, draining
Operation, control circulating water quality maintains the stability of a system in management and control scope.But still the problems such as incrustation scale, corrosion is unavoidably produced,
And the outer water vent of recirculated water can be to environment.
Utility model content
The purpose of this utility model be provide it is a kind of be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, its
Can by calcium ions and magnesium ions in water with precipitated form discharge, reduce circulation the water hardness, while anode can produce strong oxidizing property chlorine,
Free radical etc., can control algal grown in water, with sterilization algae removal function.
To solve above-mentioned technical problem, embodiment of the present utility model is applied to recirculated water there is provided one kind can be automatically clear
The electrochemical descaling device of dirt, it includes：The dirty device of casing, anode network, minus plate, collection, dc source, control system；Collection dirt
Device is installed on lower box, and communicates with the reative cell outlet of casing；Anode network, minus plate are installed on the reative cell of casing
In；Anode network, minus plate are electrically connected at dc source；Dc source is provided with the switching device of changeable cathode and anode directions,
The switching device is connected to control system；The reative cell of casing is provided with accessing pending water input port, and the dirty device of collection is provided with after process
Water output and incrustation scale are exported.
Compared with prior art, the utility model provide it is a kind of be applied to recirculated water can automatic scale-cleaning electrochemical descaling
Device can precipitated form be discharged by calcium ions and magnesium ions in water, the circulation water hardness is reduced, while anode can produce strong oxidizing property
Chlorine, free radical etc., can control algal grown in water, with sterilization algae removal function.
Further, casing is cylindrical shape empty capsid, and lower box is provided with bracing frame, casing upper and lower difference
Lid, lower cover are provided with, between the dirty device of upper lid, lower cover, collection and casing insulated enclosure circle is provided with, accessing pending water input port is arranged
In casing right side lower end.
Further, the structure that dirty device is that a cross-sectional area is tapered into from top towards bottom is collected.
Further, it is a spherical structure or cone structure to collect dirty device.
Further, it is tubular structure to be arranged in the anode network of box house, minus plate, and be cylindrical in shape structure anode network,
Minus plate alternates nesting arrangement；It is pending when gap is left between the top of the minus plate being connected with lower cover and upper lid
Water from the gap from the inner side of the outer side inflow minus plate of minus plate；Extend at the top of the minus plate being connected with lower cover
Gai Shi, the minus plate is provided with the perforate and/or opening for allowing accessing pending water to pass through；The reative cell outlet is then located at most inner side
The space bottom gone along with sb. to guard him of anode network/minus plate.
Further, it is provided between adjacent cathode plate and allows accessing pending water in the turbine guide part of the indoor formation vortex of reaction.
Further, the anode network for being cylindrical in shape structure is provided with multiple anode terminals, and anode terminal upper end is by more
Individual insulation joint terminal through upper lid hole and stretch out casing, the minus plate and casing lower cover for being cylindrical in shape structure is connected, lower cover and
Minus plate constitutes negative electrode board component as an entirety, and the cathode terminal right side that the negative electrode board component is connected passes through casing
Side wall and stretch out casing.
Further, anode network and minus plate are provided with titanium alloy metal coating.
Further, water output is respectively arranged with the water inlet conduction for being connected to control system after accessing pending water input port, process
Instrument, water outlet conductivity apparatus, and water output, incrustation scale outlet are provided with control valve in accessing pending water input port, after processing.
Further, water output, the pipeline that picks out of incrustation scale outlet are provided with filter after process.
The device has the functions such as scale removal, anti-corrosion, sterilization, can by-pass flow be installed on circulating cooling pond or water return pipeline.
After the operation principle negative electrode of this device and anode switch on power, recirculated water is when equipment, it may occur that a series of changes
Change：Strong alkali environment is formed about in negative electrode, the calcium ions and magnesium ions in recirculated water is separated out from water, and be deposited on the negative electrode table of equipment
Face；Anode dissolved oxygen nearby in chlorion, water etc. is changed into free radical and hypochlorous acid, makes bacterium in water, algae direct
Kill.When electrochemical descaling device continuous processing for a period of time, after the dirty class being enriched near the negative electrode reaches certain thickness, system
Negative electrode and anode can be automatically inverted according to pre-set program.Incrustation scale gradually comes off, and leads to dirty device is collected with downelling
Cross blow-off pipe discharge.Incrustation scale switches to normal process program after removing.
Description of the drawings
Fig. 1 be it is a kind of be applied to recirculated water can automatic scale-cleaning electrochemical descaling apparatus structure schematic diagram；
Fig. 2 be it is a kind of be applied to recirculated water can automatic scale-cleaning electrochemical descaling device middle-jiao yang, function of the spleen and stomach polar net elevation；
Fig. 3 is that a kind of recirculated water that is applied to can minus plate elevation in the electrochemical descaling device of automatic scale-cleaning
Fig. 4 is that a kind of recirculated water that is applied to can omit part-structure in the electrochemical descaling device of automatic scale-cleaning at casing
Top view, the figure shows a kind of distribution form of anode network, cathode screen, anode terminal；
Fig. 5 is that a kind of recirculated water that is applied to can omit part-structure in the electrochemical descaling device of automatic scale-cleaning at casing
Top view, the figure shows another kind of distribution form of anode network, cathode screen, anode terminal.
Specific embodiment
In order that technological means, creation characteristic, reached purpose and effect that the utility model is realized are easy to understand, under
Face in conjunction with specific embodiments, is expanded on further the utility model.
Embodiment of the present utility model provide it is a kind of be applied to recirculated water can automatic scale-cleaning electrochemical descaling device,
Shown in Figure 1, it includes：Casing 1, upper lid 2, anode network 3, minus plate 4, anode terminal 5, negative electrode connect made by stainless steel
Terminal 6, collection dirt device 7, inlet valve 8, water inlet conductivity apparatus 9, flowing water Valve 10, water outlet conductivity apparatus that precipitation is concentrated for incrustation scale
11st, blowoff valve 12, dc source 13, control system 14.
Wherein, it is shown in Figure 1, it is easy to incrustation scale to concentrate the collection dirt device 7 of precipitation to be installed on the bottom of casing 1, and and casing
Reative cell outlet communicate, the dirty device of collection is provided with water output and incrustation scale outlet after process.For ease of precipitation, the dirty device of collection
7 gathering structures tapered into towards bottom from top for a cross-sectional area, such as the spherical structure shown in Fig. 1, certainly,
The version of the dirty device of this collection includes but are not limited to illustrated case, can also be the other structures type such as cone structure, water
Dirt falls because of deadweight, can be because the incrustation scale that the gathering structure and coming together in of collection dirt device is arranged on gathering structure bottom goes out
Mouthful, the incrustation scale outlet being provided with incrustation scale and picks out pipeline, the incrustation scale picks out pipeline and is provided with blowoff valve 12.
Shown in Figure 1, anode network 3, minus plate 4 are installed in the reative cell of casing, and anode network 3, minus plate 4 are electrical
Dc source 13 is connected to, the dc source is provided with the switching device of changeable cathode and anode directions, such as change-over switch, this is cut
Changing device is connected to control system.The reative cell of casing is provided with accessing pending water input port.
In addition, referring to Fig. 2-3, being arranged in the anode network 3 of box house, minus plate 4 and being tubular structure, and be cylindrical in shape structure
Anode network 3, minus plate 4 alternate nesting arrangement.
As a kind of embodiment, when not extending to upper lid at the top of the minus plate being connected with lower cover, pending water
Can pass through from the gap between minus plate top and upper lid, and another embodiment is, extends at the top of minus plate
During upper lid, now, minus plate is then provided with the water-bound excessively for allowing accessing pending water to pass through, for example, arrange in minus plate and open accordingly
Hole, or arrange opening from top to bottom that extends from the side wall of minus plate, mistake water-bound is also or said two devices structure
Combination, reative cell outlet is then located at the space bottom gone along with sb. to guard him of anode network/minus plate of most inner side, and figure 4 below and Fig. 5 are equal
Use and water-bound was set on minus plate, in an embodiment shown in fig. 4, including the two-layer (circle) of mutually nested arrangement
Anode network 3 and two-layer minus plate 4, certainly, layer (circle) number of anode network arrangement mutually nested with minus plate can with more, in order to
The treatment effect of more high-quality is obtained, and outermost is provided that one layer of (circle) anode network 3, most inner side is provided that one layer (circle)
Minus plate 4, two-layer (circle) minus plate cross water-bound be dislocation arrangement, in order to allow pending water to flow distance more
Long, pending water is entered after the reative cell, is sequentially passed through outermost anode network and then is crossed water through outermost layer minus plate
Structure, the most anode network of inner side, innermost layer minus plate cross water-bound, then from the dirty device of the outlet of reative cell flow direction collection.For
More preferably water treatment efficiency is obtained, the effect for forming vortex in reative cell is shown in Figure 5, in the embodiment, two-layer (circle)
Turbine guide plate is provided between minus plate, the turbine guide plate was close to be arranged at water-bound that the effect of arrangement was intended to
The accessing pending water of reative cell forms vortex, and the arrangement form of turbine guide plate includes but are not limited to illustrated case.
And, the anode network for being cylindrical in shape structure is provided with multiple anode terminals 5, and anode terminal upper end is by multiple
Insulation joint terminal through upper lid hole and stretch out casing, the minus plate and casing lower cover for being cylindrical in shape structure be connected, lower cover and the moon
Pole plate constitutes negative electrode board component as an entirety, and the right side of cathode terminal 6 that the negative electrode board component is connected passes through casing
Side wall and stretch out casing.And anode network and minus plate can arrange titanium alloy metal coating.
In addition, casing is cylindrical shape empty capsid, lower box is provided with bracing frame, bracing frame can be arranged into lift
Structure and/or travel mechanism, casing upper and lower is respectively arranged with lid, lower cover, between the dirty device of upper lid 2, lower cover, collection and casing
Insulated enclosure circle is provided with, accessing pending water input port is arranged at casing right side lower end.The lower cover center that casing is arranged is arranged
There is delivery port and lead to the dirty device of collection, water output is respectively arranged with and is connected to control system after accessing pending water input port, process
Water inlet conductivity apparatus 9, water outlet conductivity apparatus 11, and water output, incrustation scale outlet are provided with control in accessing pending water input port, after processing
Valve, be for example arranged at the inlet valve 8 of accessing pending water input port, be arranged at process after water output flowing water Valve 10 and set
It is placed in the blowoff valve 12 of incrustation scale outlet.
Utility model works flow process is as follows：Pending recirculated water is from the lower right side Jing inlet valves 8, water inlet conductance of casing 1
Instrument 9 enters casing reative cell.Box house is provided with guiding device.Anode network 3 fixes support by many anode terminals 5, sun
Stretch out casing, minus plate 4 and casing lower cover through the hole for being opened in lid 2 by multiple insulation joint ends in the upper end of pole binding post 5
Connection, integrally makees minus plate, and casing is stretched out in the right side of cathode terminal 6 through cylinder lower cover.Binding post is connected after dc source 13,
There is electrochemical reaction in pending recirculated water, calcium ions and magnesium ions are constantly analysed in the deposition of minus plate 4 in water in anode network 3 and minus plate 4
Go out, processed recirculated water water body.Water flows out from the bottom centre of casing 1 after process, and into the dirty device 7 of collection, Jing water conservancy diversion is closed
Blowoff valve 12, opens outlet valve 10, is detected after effluent quality by water outlet conductivity gauge 11, comes back to circulation.With place
Reason water is constantly carried out, and the dirty class of the enrichment of minus plate 4 is reached after certain thickness, the control switching of the Jing pre-set programs of control system 14
Device is inverted negative electrode and anode automatically.Incrustation scale gradually comes off, and closes flowing water Valve 10 to dirty device 7 is collected with downelling, opens
Open and discharged by blow-off pipe after blowoff valve 12.Incrustation scale switches to normal process program after removing.Control system 14 receives Inlet and outlet water
The signal of conductivity gauge, by logical operation the operational factor of electrochemical apparatus is changed automatically.
Used as another embodiment of the present utility model, water output, the pipeline that picks out of incrustation scale outlet set after process
Filter is equipped with, water after filter is crossed and is come back to cooling pond, further water saving.
It will be understood by those skilled in the art that the respective embodiments described above are to realize of the present utility model being embodied as
Example, and in actual applications, can in the form and details to it, various changes can be made, without departing from spirit of the present utility model
And scope.
Claims (10)
1. it is a kind of be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that it includes：Casing, anode
The dirty device of net, minus plate, collection, dc source, control system；
The collection dirt device is installed on lower box, and communicates with the reative cell outlet of casing；
The anode network, minus plate are installed in the reative cell of the casing；
The anode network, minus plate are electrically connected at the dc source；
The dc source is provided with the switching device of changeable cathode and anode directions, and the switching device is connected to the control system；
The reative cell of the casing is provided with accessing pending water input port, the collection dirt device be provided with after process water output and
Incrustation scale is exported.
2. it is according to claim 1 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that institute
It is cylindrical shape empty capsid to state casing, and lower box is provided with bracing frame, and the casing upper and lower is respectively arranged with
Lid, lower cover, between the dirty device of the upper lid, lower cover, collection and casing insulated enclosure circle is provided with, and the accessing pending water input port is arranged
In casing right side lower end.
3. it is according to claim 1 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that institute
State the structure that the dirty device of collection is that a cross-sectional area is tapered into from top towards bottom.
4. it is according to claim 3 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that institute
It is a spherical structure or cone structure to state the dirty device of collection.
5. it is according to claim 1 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that cloth
It is tubular structure to be placed in the anode network of box house, minus plate, and is cylindrical in shape the anode network of structure, minus plate and alternates nesting
Arrangement；
When gap is left between the top of the minus plate being connected with lower cover and upper lid, pending water is from the gap from minus plate
Outer side inflow minus plate inner side；
When extending to upper lid at the top of the minus plate being connected with lower cover, the minus plate is provided with opening of allowing accessing pending water to pass through
Hole and/or opening；
The reative cell outlet is then located at the space bottom that the anode network/minus plate of most inner side is gone along with sb. to guard him.
6. it is according to claim 5 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that phase
It is provided between adjacent minus plate and allows accessing pending water in the turbine guide part of the indoor formation vortex of reaction.
7. it is according to claim 5 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that be in
The anode network of tubular structure is provided with multiple anode terminals, and the anode terminal upper end passes through multiple insulation joint terminals
Casing is stretched out through the hole of upper lid, the minus plate for being cylindrical in shape structure is connected with casing lower cover, lower cover is with minus plate as one
Negative electrode board component is integrally constituted, case is stretched out in the cathode terminal right side that the negative electrode board component is connected through wall box
Body.
8. according to claim 1 or 5 or 7 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, its feature
It is that the anode network and minus plate are provided with titanium alloy metal coating.
9. it is according to claim 1 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, it is characterised in that institute
State water output after accessing pending water input port, process and be respectively arranged with water inlet conductivity apparatus, the water outlet conductivity apparatus for being connected to control system,
And water output, incrustation scale outlet are provided with control valve in accessing pending water input port, after processing.
10. according to claim 1 or 9 be applied to recirculated water can automatic scale-cleaning electrochemical descaling device, its feature exists
In water output, the pipeline that picks out of incrustation scale outlet are provided with filter after the process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621168932.8U CN206173054U (en) | 2016-11-02 | 2016-11-02 | Be applied to electrochemistry scale removal device that circulating water can automatic snaking |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621168932.8U CN206173054U (en) | 2016-11-02 | 2016-11-02 | Be applied to electrochemistry scale removal device that circulating water can automatic snaking |
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| Publication Number | Publication Date |
|---|---|
| CN206173054U true CN206173054U (en) | 2017-05-17 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621168932.8U Expired - Fee Related CN206173054U (en) | 2016-11-02 | 2016-11-02 | Be applied to electrochemistry scale removal device that circulating water can automatic snaking |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107043154A (en) * | 2017-06-16 | 2017-08-15 | 福州金慧健康科技有限公司 | A kind of free radical generation device |
| CN108609748A (en) * | 2018-07-18 | 2018-10-02 | 浙江大学 | Ion film electrodeposition device and deposition method for recirculated cooling water sofening treatment |
| CN110182975A (en) * | 2019-06-27 | 2019-08-30 | 管家洪 | The automatic descaling apparatus and sofening treatment system of sofening treatment are carried out to hard water |
| CN110182974A (en) * | 2019-06-21 | 2019-08-30 | 中国华能集团有限公司 | A kind of automatically cleaning immersion device for electrochemical water preparation and its operation method |
| CN111039474A (en) * | 2019-12-26 | 2020-04-21 | 西安泰金工业电化学技术有限公司 | Power plant circulating water treatment system and method |
| CN112174264A (en) * | 2020-10-21 | 2021-01-05 | 内蒙古蓝能环保科技有限公司 | Multifunctional remote control circulating water detection and treatment integrated machine |
| CN112919584A (en) * | 2021-03-01 | 2021-06-08 | 湘潭大学 | Full-automatic control circulating water descaling device and use method thereof |
-
2016
- 2016-11-02 CN CN201621168932.8U patent/CN206173054U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107043154A (en) * | 2017-06-16 | 2017-08-15 | 福州金慧健康科技有限公司 | A kind of free radical generation device |
| CN108609748A (en) * | 2018-07-18 | 2018-10-02 | 浙江大学 | Ion film electrodeposition device and deposition method for recirculated cooling water sofening treatment |
| CN108609748B (en) * | 2018-07-18 | 2021-10-29 | 浙江大学 | Ion membrane electrodeposition device and deposition method for softening treatment of circulating cooling water |
| CN110182974A (en) * | 2019-06-21 | 2019-08-30 | 中国华能集团有限公司 | A kind of automatically cleaning immersion device for electrochemical water preparation and its operation method |
| CN110182975A (en) * | 2019-06-27 | 2019-08-30 | 管家洪 | The automatic descaling apparatus and sofening treatment system of sofening treatment are carried out to hard water |
| CN111039474A (en) * | 2019-12-26 | 2020-04-21 | 西安泰金工业电化学技术有限公司 | Power plant circulating water treatment system and method |
| CN112174264A (en) * | 2020-10-21 | 2021-01-05 | 内蒙古蓝能环保科技有限公司 | Multifunctional remote control circulating water detection and treatment integrated machine |
| CN112919584A (en) * | 2021-03-01 | 2021-06-08 | 湘潭大学 | Full-automatic control circulating water descaling device and use method thereof |
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| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
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| CF01 | Termination of patent right due to non-payment of annual fee |