CN208087278U - A kind of wastewater electrolytic tank - Google Patents
A kind of wastewater electrolytic tank Download PDFInfo
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- CN208087278U CN208087278U CN201820390352.6U CN201820390352U CN208087278U CN 208087278 U CN208087278 U CN 208087278U CN 201820390352 U CN201820390352 U CN 201820390352U CN 208087278 U CN208087278 U CN 208087278U
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- electrolytic cell
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- wastewater
- electrolytic tank
- dirt
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Abstract
The utility model is related to technical field of waste water processing, in particular a kind of wastewater electrolytic tank, including electrolytic cell, the gas gathering mask at the top of electrolytic cell, the blowdown funnel mounted on electrolysis pot bottom and the electrolysis unit that is arranged inside electrolytic cell.The wastewater electrolytic tank, since isocon is with a narrow upper and lower width trapezoidal, when water source flows through isocon, water velocity is accelerated, and increases the scouring force of water, while aeration tube is blown upwards, and water source is driven to rise, the dirt on cathode bar surface is washed away, the cleaning ability on cathode bar surface is improved;Stirring wheel is rotated with the movement at water source in connecting plate, break process is carried out to larger dirt by crushing teeth, solves the problem of that larger dirt falls directly into blowdown funnel and be easy to cause blowdown funnel blocking, be conducive to that dirt decompose to be crushed, improve the efficiency of blowdown.
Description
Technical field
The utility model is related to technical field of waste water processing, specially a kind of wastewater electrolytic tank.
Background technology
Electrochemical oxidation wastewater processing technology is to make pollutant that Direct Electrochemistry reaction occur on the electrode pollutant is made to send out
Raw redox transformation, or make contaminant degradation using the strong oxidizing property active material that electrode surface generates.Electrochemistry oxygen
Changing process waste water, to have many advantages, such as not generate secondary pollution, energy efficiency height, electrolysis installation and operating method simple, is locating
It is used widely in terms of reason indegradable industrial effluent.In electrolytic process, pollutant anode surface aoxidized be converted to it is small
Molecular substance achievees the purpose that remove pollutant, and reduction reaction can occur in cathode surface and generate a large amount of OH-, and in water
Some Ca2+, Mg2+ ions generate Ca (OH) 2 and Mg (OH) 2, reacted with CO32- under aeration condition be converted into CaCO3 and
MgCO3 is attached to cathode surface, and is constantly thickened with the progress of cell reaction.
But existing wastewater electrolytic tank, as cell reaction works, cathode surface generates a large amount of dirt, it is difficult to it handles,
Energy consumption increase, treatment effeciency is caused to reduce and shorten pole plate service life, while larger dirt falls directly into blowdown funnel,
It is be easy to cause blowdown funnel blocking, influences contaminant removal effectiveness.In consideration of it, it is proposed that a kind of wastewater electrolytic tank.
Utility model content
The purpose of this utility model is to provide a kind of wastewater electrolytic tanks, to solve cathode mentioned above in the background art
Surface generates a large amount of dirt, it is difficult to the problem of handling and blowdown funnel is caused to block.
To achieve the above object, the utility model provides the following technical solutions:
A kind of wastewater electrolytic tank, including electrolytic cell, the gas gathering mask at the top of the electrolytic cell, be mounted on the electrolysis
The blowdown funnel of pot bottom and the electrolysis unit being arranged inside the electrolytic cell, the electrolysis tank wall upper and lower ends are set respectively
It is equipped with water inlet pipe and drainpipe, the electrolysis top tank structure is provided with sluicing cover close to described gas gathering mask one end, the cover that sluices
Including inverted draw cut, the bottom of the inverted draw cut is equipped with fluid dividing cover, and the bottom of the fluid dividing cover is provided with several discharge outlet, the top
Slot is internally provided with several through-holes, and the fluid dividing cover inside top is provided with flow distribution plate, and the bottom of the flow distribution plate is provided with
Several isocons, the electrolysis unit includes anode stub, is arranged in the cathode bar of described anode stub one end and for for institute
State the working power of anode stub and cathode bar power supply.
Preferably, the positive terminal of the working power and the anode stub are electrically connected, the negative pole end of the working power
It is electrically connected with the cathode bar.
Preferably, the flow distribution plate and the isocon communicate.
Preferably, the section of the isocon is with a narrow upper and lower width trapezoidal.
Preferably, the electrolysis top tank structure is provided with stirring cover, the stirring cover inner wall two close to described blowdown funnel one end
End is respectively arranged with mounting base, connecting plate is provided between two mounting bases, the connecting plate is internally provided with several
The surface of stirring wheel, the stirring wheel is provided with several crushing teeths, and the bottom of the blowdown funnel is provided with aeration tube, the electricity
It is provided with air pump on the outside of solution tank.
Preferably, the output end of the air pump is connected with the input end of the aeration tube.
Preferably, the section of the stirring cover is in up-narrow and down-wide trapezoidal.
Compared with prior art, the beneficial effects of the utility model:
1, the wastewater electrolytic tank, since isocon is with a narrow upper and lower width trapezoidal, when water source flows through isocon, water velocity adds
Soon, the scouring force for increasing water washes away the dirt on cathode bar surface, while aeration tube is blown upwards, and drives on water source
It rises, the dirt on cathode bar surface is washed away, scouring force when intaking is increased by isocon, and generate by aeration tube
Water source is risen, cathode bar surface is washed away, improves the cleaning ability on cathode bar surface.
2, the wastewater electrolytic tank, stirring wheel is rotated with the movement at water source in connecting plate, by crushing teeth to larger
Dirt carries out break process, solves the problem of that larger dirt falls directly into blowdown funnel and be easy to cause blowdown funnel blocking, favorably
It is broken in dirt decompose, improve the efficiency of blowdown.
Description of the drawings
Fig. 1 is the overall structure diagram of the utility model;
Fig. 2 is the sluicing cover structure schematic diagram of the utility model;
Fig. 3 is the inverted draw cut structural schematic diagram of the utility model;
Fig. 4 is the electrolysis unit structural schematic diagram of the utility model;
Fig. 5 is the stirring cover structure schematic diagram of the utility model.
In figure:1, electrolytic cell;11, water inlet pipe;12, drainpipe;13, sluice cover;131, inverted draw cut;132, fluid dividing cover;133,
Discharge outlet;134, through-hole;135, flow distribution plate;136, isocon;14, stirring cover;141, mounting base;142, connecting plate;143, it stirs
Mix wheel;144, crushing teeth;15, aeration tube;16, air pump;2, gas gathering mask;3, blowdown funnel;4, electrolysis unit;41, anode stub;42,
Cathode bar;43, working power.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
- 5 are please referred to Fig.1, the utility model provides a kind of technical solution:
A kind of wastewater electrolytic tank, as shown in Figure 1, Figure 2, Figure 3 and Figure 4, including electrolytic cell 1, mounted on the top of electrolytic cell 1
Gas gathering mask 2, the blowdown funnel 3 mounted on 1 bottom of electrolytic cell and the electrolysis unit 4 that is arranged inside electrolytic cell 1, outside electrolytic cell 1
Wall upper and lower ends are respectively arranged with water inlet pipe 11 and drainpipe 12, and 1 inner wall of electrolytic cell is provided with sluicing cover close to 2 one end of gas gathering mask
13, the cover 13 that sluices includes inverted draw cut 131, and the bottom of inverted draw cut 131 is equipped with fluid dividing cover 132, if the bottom of fluid dividing cover 132 is provided with
Dry discharge outlet 133, inverted draw cut 131 are internally provided with several through-holes 134, and 132 inside top of fluid dividing cover is provided with flow distribution plate
135, the bottom of flow distribution plate 135 is provided with several isocons 136, and electrolysis unit 4 includes anode stub 41, is arranged in anode stub 41
The cathode bar 42 of one end and for for anode stub 41 and cathode bar 42 power supply working power 43, the positive terminal of working power 43
It is electrically connected with anode stub 41, the negative pole end and cathode bar 42 of working power 43 are electrically connected, flow distribution plate 135 and isocon 136
It communicates, the section of isocon 136 is with a narrow upper and lower width trapezoidal.
In the present embodiment, discharge outlet 133 and electrolysis unit 4 are located on the same line, the scouring force declined using water source
Dirt to sticking in 42 surface of cathode bar is cleared up.
In the present embodiment, spacing between anode stub 41 and cathode bar 42 is 10mm, be anode stub 41 and cathode bar 42 it
Between certain space is provided, be convenient for treatment of dirt.
In the present embodiment, working power 43 is direct current, convenient for providing electric current for anode stub 41 and cathode bar 42 and carrying out electricity
Solve work.
As shown in Figure 1 and Figure 5,1 inner wall of electrolytic cell is provided with stirring cover 14, stirring 14 inner walls of cover close to 3 one end of blowdown funnel
Both ends are respectively arranged with mounting base 141, and connecting plate 142 is provided between two mounting bases 141, and connecting plate 142 is internally provided with
The surface of several stirring wheels 143, stirring wheel 143 is provided with several crushing teeths 144, and the bottom of blowdown funnel 3 is provided with aeration
The outside of pipe 15, electrolytic cell 1 is provided with air pump 16, and the output end of air pump 16 is connected with the input end of aeration tube 15, stirring cover
14 section is in up-narrow and down-wide trapezoidal.
In the present embodiment, stirring wheel 143 is rotatablely connected by shaft and connecting plate 142, is being connected by stirring wheel 143
It is rotated on plate 142, dirt is cut, avoid the problem that larger dirt results in blockage.
In the present embodiment, crushing teeth 144 is made of angle steel material, and crushing teeth 144 is tapered, and angle steel material is hard,
144 structural rigidity of crushing teeth is improved, while convenient for carrying out crushing operation to dirt.
In the present embodiment, air pump 16 is that the gas that aeration tube 15 exports is nitrogen, can reduce electrochemical treatment of wastewater process
The generation of middle dirt layer.
The wastewater electrolytic tank of the present embodiment is added to from water inlet pipe 11 inside electrolytic cell 1 when in use, by waste water, waste water stream
It flows into sluicing cover 13 and from the through-hole 134 inside inverted draw cut 131, and is flowed to from electrolysis unit 4 from discharge outlet 133, pass through work
Power supply 43 is that anode stub 41 and cathode bar 42 are powered, and pollutant is aoxidized on 41 surface of anode stub is converted to small-molecule substance, reaches
To the purpose of removal pollutant, while dirt is adsorbed on the surface of cathode bar 42, when water source enters sluicing 13 inside of cover, water
Source is further separated into from flow distribution plate 135 into isocon 136, and since isocon 136 is with a narrow upper and lower width trapezoidal, water source flows through point
When flow tube 136, water velocity is accelerated, and increases the scouring force of water, is washed away to the dirt on 42 surface of cathode bar, while by air pump
16 access alternating currents, realize that aeration tube 15 is blown upwards, and water source is driven to rise, are washed away to the dirt on 42 surface of cathode bar,
It solving cathode surface and generates a large amount of dirt, it is difficult to the problem of handling increases scouring force when intaking by isocon 136, and
It is generated by aeration tube 15 and rises water source, 42 surface of cathode bar is washed away, improve the cleaning ability on 42 surface of cathode bar;It is dirty
Dirt enters in stirring cover 14, stirring wheel 143 is as the movement at water source is in connecting plate 142 at this time after cathode bar 42 falls off
Rotation carries out break process to larger dirt by crushing teeth 144, solves larger dirt and fall directly into blowdown funnel, hold
The problem of blowdown funnel blocks is easily caused, is conducive to that dirt decompose to be crushed, improves the efficiency of blowdown.
Basic principles, main features, and advantages of the present invention has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the present utility model is not limited to the above embodiments, described in above embodiments and description
Be only the utility model preference, be not intended to limit the utility model, do not departing from the spirit and scope of the utility model
Under the premise of, the utility model also has various changes and improvements, these changes and improvements both fall within this claimed practicality
In novel range.The protection scope of the present invention is defined by the appended claims and their equivalents.
Claims (7)
1. a kind of wastewater electrolytic tank, including electrolytic cell (1), be mounted at the top of the electrolytic cell (1) gas gathering mask (2), be mounted on
In the electrolysis unit (4) of the electrolytic cell (1) inside, feature exists for the blowdown funnel (3) of electrolytic cell (1) bottom and setting
In:Electrolytic cell (1) the outer wall upper and lower ends are respectively arranged with water inlet pipe (11) and drainpipe (12), and the electrolytic cell (1) is interior
Wall is provided with sluicing cover (13) close to the gas gathering mask (2) one end, and the cover (13) that sluices includes inverted draw cut (131), the top
The bottom of slot (131) is equipped with fluid dividing cover (132), and the bottom of the fluid dividing cover (132) is provided with several discharge outlet (133),
The inverted draw cut (131) is internally provided with several through-holes (134), and fluid dividing cover (132) inside top is provided with flow distribution plate
(135), the bottom of the flow distribution plate (135) is provided with several isocons (136), and the electrolysis unit (4) includes anode stub
(41), setting is in the cathode bar (42) of the anode stub (41) one end and for being the anode stub (41) and the cathode bar
(42) working power (43) powered.
2. wastewater electrolytic tank according to claim 1, it is characterised in that:The positive terminal of the working power (43) and described
Anode stub (41) is electrically connected, and the negative pole end and the cathode bar (42) of the working power (43) are electrically connected.
3. wastewater electrolytic tank according to claim 1, it is characterised in that:The flow distribution plate (135) and the isocon
(136) it communicates.
4. wastewater electrolytic tank according to claim 1, it is characterised in that:It presents under width in the section of the isocon (136)
Narrow is trapezoidal.
5. wastewater electrolytic tank according to claim 1, it is characterised in that:Electrolytic cell (1) inner wall is close to the blowdown
Bucket (3) one end is provided with stirring cover (14), and the stirring cover (14) inner wall both ends are respectively arranged with mounting base (141), two institutes
It states and is provided with connecting plate (142) between mounting base (141), the connecting plate (142) is internally provided with several stirring wheels
(143), the surface of the stirring wheel (143) is provided with several crushing teeths (144), and the bottom of the blowdown funnel (3) is provided with
Aeration tube (15) is provided with air pump (16) on the outside of the electrolytic cell (1).
6. wastewater electrolytic tank according to claim 5, it is characterised in that:The output end and the aeration of the air pump (16)
The input end of pipe (15) is connected.
7. wastewater electrolytic tank according to claim 5, it is characterised in that:The section of the stirring cover (14) is in up-narrow and down-wide
It is trapezoidal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820390352.6U CN208087278U (en) | 2018-03-21 | 2018-03-21 | A kind of wastewater electrolytic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820390352.6U CN208087278U (en) | 2018-03-21 | 2018-03-21 | A kind of wastewater electrolytic tank |
Publications (1)
Publication Number | Publication Date |
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CN208087278U true CN208087278U (en) | 2018-11-13 |
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ID=64060076
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CN201820390352.6U Expired - Fee Related CN208087278U (en) | 2018-03-21 | 2018-03-21 | A kind of wastewater electrolytic tank |
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CN (1) | CN208087278U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110304361A (en) * | 2018-03-27 | 2019-10-08 | 中国石油天然气股份有限公司 | Liquid container |
CN116514235A (en) * | 2023-07-04 | 2023-08-01 | 太原科技大学 | Electrolysis device for sewage treatment |
-
2018
- 2018-03-21 CN CN201820390352.6U patent/CN208087278U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110304361A (en) * | 2018-03-27 | 2019-10-08 | 中国石油天然气股份有限公司 | Liquid container |
CN110304361B (en) * | 2018-03-27 | 2021-06-01 | 中国石油天然气股份有限公司 | Liquid container |
CN116514235A (en) * | 2023-07-04 | 2023-08-01 | 太原科技大学 | Electrolysis device for sewage treatment |
CN116514235B (en) * | 2023-07-04 | 2023-09-22 | 太原科技大学 | Electrolysis device for sewage treatment |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181113 |
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CF01 | Termination of patent right due to non-payment of annual fee |