CN209226744U - Integrated electrolysis equipment - Google Patents
Integrated electrolysis equipment Download PDFInfo
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- CN209226744U CN209226744U CN201822139740.XU CN201822139740U CN209226744U CN 209226744 U CN209226744 U CN 209226744U CN 201822139740 U CN201822139740 U CN 201822139740U CN 209226744 U CN209226744 U CN 209226744U
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- electrolysis
- flocculation sedimentation
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- outlet pipe
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Abstract
Integrated electrolysis equipment, the utility model relates to sewage treatment fields, and in particular to a kind of integrated electrolysis equipment.Provide it is a kind of integrate water inlet reaction, flocculation sedimentation, be discharged spoil disposal, good sewage processing effect integrated electrolysis equipment.The partition is equipped with the electrolysis outlet pipe of connection electrolytic cell and flocculation sedimentation tank, and one end of the electrolysis outlet pipe is fixed on partition, the other end is fixed on the steady flow pipe of center.The utility model had both had the electrochemical reaction of electrolytic cell, but also with the flocculation sedimentation of sedimentation basin, integrated water inlet reaction, flocculation sedimentation, water outlet spoil disposal；Sewage by electrolytic cell electrolysis flow to flocculation sedimentation by electrolysis outlet pipe, without using elevator pump, has not only saved cost, but also not will form excessive agitation influence precipitating；The center steady flow pipe in middle position is set in flocculation sedimentation tank, electrolysis outlet pipe is connected on the steady flow pipe of center, and not only sedimentation effect is good, but also bottom precipitation is uniformly dispersed, and is convenient for spoil disposal.
Description
Technical field
The utility model relates to sewage treatment fields, and in particular to a kind of integrated electrolysis equipment.
Background technique
Since environmental pollution is paid more and more attention, with the implementation of the Law on Environmental Protection of the People's Republic of China (2015),
Effluent-disposal standard is increasingly stringenter, and scale is increasing, with electrolysis method, flocculent precipitation carry out sewage treatment increasingly at
For the important component in sewage treatment process.Electrolysis method is so that harmful components in waste water is passed through electricity using the principle of electrolysis
Solution preocess is in the anti-raw oxidation of yin, yang the two poles of the earth difference and reduction reaction, to be converted into the process of innoxious substance.Flocculent precipitation
It is the process that particulate matter makees flocculation sedimentation in water, is flocculated using the Fe3+ that itself electrolysis generates, while can reduce in water
C 1 content.Reaction equation: Fe-3e- ~ Fe3+, 2Cl -2e- ~ Cl2↑.Existing sewage treatment have individually using electrolysis method or
Person's flocculent precipitation, also have while using electrolysis method and flocculent precipitation, individually uses electrolysis method or flocculent precipitation
Processing method sewage treatment capacity it is slightly weak, while using the processing method of electrolysis method and flocculent precipitation needing that electricity is respectively set
Xie Chi and flocculation sedimentation tank are further precipitated electrolysis treated sewage with pump promotion into flocculation sedimentation tank, because
The power of pump is larger, and it is just bigger to reach the sewage agitation in flocculation sedimentation tank from electrolytic cell, leads to sedimentation effect and bad.
Utility model content
The utility model in view of the above problems, provide it is a kind of integrate water inlet reaction, flocculation sedimentation, be discharged spoil disposal,
The integrated electrolysis equipment of good sewage processing effect.
The technical solution of the utility model is: including rack and the pond body being fixed on the rack, the pond body passes through partition
It is separated into electrolytic cell and flocculation sedimentation tank, the middle position at the top of the flocculation sedimentation tank is equipped with the center current stabilization extended downwardly
Pipe, the opposite side of the partition of the flocculation sedimentation tank be equipped with water outlet, the water outlet be equipped with L-type baffle, it is described go out
The mouth of a river is located at the top of the bottom plate of L-type baffle, and the L-type baffle and the side constitute water outlet weir notch, the flocculation sedimentation tank
The middle position of bottom is equipped with sludge pipe,
The partition is equipped with the electrolysis outlet pipe of connection electrolytic cell and flocculation sedimentation tank, one end of the electrolysis outlet pipe
It is fixed on partition, the other end is fixed on the steady flow pipe of center.
The electrolysis outlet pipe is located in the middle part of the steady flow pipe of center or the above position in middle part,
On the electrolytic cell, side that partition is opposite be equipped with water inlet pipe.
The electrolysis outlet pipe is horizontal or is arranged diagonally downward from the one end being located on partition.
The electrolysis outlet pipe from one end angle diagonally downward being located on partition be 0-30 °.
Be equipped with the vertical spaced anode plate and cathode plate of several difference in the electrolytic cell, several anode plates with
Cathode plate is set to the bottom of the adjustable support by several adjustable support connections being laterally arranged, described adjustable
Bracket includes cross bar, anode plate connecting rod and cathode plate connecting rod；The anode plate connecting rod is set to the cross bar and anode plate
Between, it is connect respectively with the cross bar and anode plate by hinged mode；The cathode plate connecting rod be set to the cross bar with
Between cathode plate, it is connect respectively with the cross bar and cathode plate by hinged mode；The both ends of the cathode plate connecting rod point
It is not hinged with the end of the anode plate connecting rod of sides adjacent.
The beneficial effects of the utility model are: the utility model had both had the electrochemical reaction of electrolytic cell, but also with
The flocculation sedimentation of sedimentation basin integrates water inlet reaction, flocculation sedimentation, water outlet spoil disposal；Sewage by electrolytic cell electrolysis passes through
Electrolysis outlet pipe flow to flocculation sedimentation, without using elevator pump, has not only saved cost, but also not will form excessive agitation shadow
Ring precipitating；The center steady flow pipe in middle position is set in flocculation sedimentation tank, electrolysis outlet pipe is connected on the steady flow pipe of center,
Not only sedimentation effect is good, but also bottom precipitation is uniformly dispersed, and is convenient for spoil disposal.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
1 is electrolytic cell in figure, and 11 be water inlet pipe, and 12 be anode plate, and 13 be cathode plate, and 14 be cross bar, and 15 be that anode plate connects
Extension bar, 16 be cathode plate connecting rod, and 17 be aeration tube, and 2 be flocculation sedimentation tank, and 21 be center steady flow pipe, and 22 be L-type baffle, 221
It is water outlet weir notch, 23 be sludge pipe, and 24 be electrolysis outlet pipe, and 25 be partition.
Specific embodiment
The utility model is illustrated with reference to the accompanying drawing.
As shown in Figure 1, the utility model includes rack and the pond body that is fixed on the rack, the pond body is divided by partition 25
It is divided into electrolytic cell 1 and flocculation sedimentation tank 2, (sedimentation effect is good, bottom dispersion in the middle position at the top of the flocculation sedimentation tank 2
Uniformly, it is convenient for spoil disposal) 21 lower end of the center center steady flow pipe 21(steady flow pipe extended downwardly is equipped with close to the bottom of flocculation sedimentation tank 2
Portion such as 10cm, 20cm, 30cm etc. avoid water outlet from forming agitation), on the opposite side of the partition 25 of the flocculation sedimentation tank 2
Equipped with water outlet, the water outlet is equipped with L-type baffle 22, and the water outlet is located at the top of the bottom plate of L-type baffle 22, described
L-type baffle 22 and the side constitute water outlet weir notch 221, and the middle position of the bottom of the flocculation sedimentation tank 2 is equipped with sludge pipe 23,
The bottom of the flocculation sedimentation tank 2 is infundibulate, is concentrated convenient for sludge, and the sludge pipe 23 is located at the bottom of funnel.
The partition 25 is equipped with the electrolysis outlet pipe 24 of connection electrolytic cell 1 and flocculation sedimentation tank 2, the electrolysis outlet pipe
24 one end is fixed on partition 25, the other end is fixed on center steady flow pipe 21,
On the electrolytic cell 1, side that partition 25 is opposite be equipped with water inlet pipe 11.
The electrolysis outlet pipe 24 is located at 21 middle part of center steady flow pipe or the above position in middle part.It mainly avoids and bottom
Drop is too big, and colleague also avoids closely being formed very much with bottom and stir, and influences to precipitate.
The electrolysis outlet pipe 24 is horizontal or is arranged diagonally downward from the one end being located on partition 25.
The electrolysis outlet pipe 24 from one end angle diagonally downward being located on partition 25 be 0-30 °.Tilt angle is such as
It is excessively high to will lead to position of the electrolysis outlet pipe 24 on partition 25 if fruit is excessive, influences to be discharged.
Several difference vertically spaced anode plate 12 and cathode plate 13, several sun are equipped in the electrolytic cell 1
Pole plate 12 is connect with cathode plate 13 by several adjustable supports being laterally arranged, and is set to the bottom of the adjustable support,
The adjustable support includes cross bar 14, anode plate connecting rod 15 and cathode plate connecting rod 16；The anode plate connecting rod 15 is set
Between the cross bar 14 and anode plate 12, it is connect respectively with the cross bar 14 and anode plate 12 by hinged mode；It is described
Cathode plate connecting rod 16 be set between the cross bar 14 and cathode plate 13, by hinged mode respectively with the cross bar 14 and sun
Pole plate 12 connects；The both ends of the cathode plate connecting rod 16 are hinged with the end of the anode plate connecting rod 16 of sides adjacent respectively, are in
Several section W types interconnected realize that the distance between any anode plate 12 and cathode plate 13 are adjusted, according to reality in operational process
Border needs to adjust the distance between electrode plate, and equipment is made to have stronger applicability, improves treatment effeciency.The anode plate 12 is
Titanium net.The cathode plate 13 is titanium plate.The bottom of the groove body is equipped with the aeration tube 17 being fixedly connected.
The utility model had both had the electrochemical reaction of electrolytic cell, but also with the flocculation sedimentation of sedimentation basin, collection water inlet
Reaction, flocculation sedimentation, water outlet spoil disposal are integrated, and not only save space, but also energy saving, good sewage processing effect；By electricity
The sewage of Xie Chi electrolysis flow to flocculation sedimentation by electrolysis outlet pipe, without using elevator pump, has not only saved cost, but also not
Will form excessive agitation influences precipitating；It is set in the center steady flow pipe in middle position in flocculation sedimentation tank, is electrolysed outlet pipe
It is connected on the steady flow pipe of center, not only sedimentation effect is good, but also bottom precipitation is uniformly dispersed, and is convenient for spoil disposal.
Claims (5)
1. integrated electrolysis equipment, which is characterized in that including rack and the pond body being fixed on the rack, the pond body passes through partition
It is separated into electrolytic cell and flocculation sedimentation tank, the middle position at the top of the flocculation sedimentation tank is equipped with the center current stabilization extended downwardly
Pipe, the opposite side of the partition of the flocculation sedimentation tank be equipped with water outlet, the water outlet be equipped with L-type baffle, it is described go out
The mouth of a river is located at the top of the bottom plate of L-type baffle, and the L-type baffle and the side constitute water outlet weir notch, the flocculation sedimentation tank
The middle position of bottom is equipped with sludge pipe,
The partition is equipped with the electrolysis outlet pipe of connection electrolytic cell and flocculation sedimentation tank, and one end of the electrolysis outlet pipe is fixed
On partition, the other end be fixed on the steady flow pipe of center,
On the electrolytic cell, side that partition is opposite be equipped with water inlet pipe.
2. integrated electrolysis equipment according to claim 1, which is characterized in that the electrolysis outlet pipe is located at center current stabilization
In the middle part of the pipe or above position in middle part.
3. integrated electrolysis equipment according to claim 1, which is characterized in that the electrolysis outlet pipe is horizontal or from position
It is arranged diagonally downward in one end on partition.
4. integrated electrolysis equipment according to claim 3, which is characterized in that the electrolysis outlet pipe is from partition
One end angle diagonally downward be 0-30 °.
5. integrated electrolysis equipment according to claim 1, which is characterized in that erected respectively in the electrolytic cell equipped with several
To spaced anode plate and cathode plate, several anode plates and cathode plate pass through several adjustable supports being laterally arranged
Connection, and it is set to the bottom of the adjustable support, the adjustable support includes that cross bar, anode plate connecting rod and cathode plate connect
Extension bar；The anode plate connecting rod be set between the cross bar and anode plate, by hinged mode respectively with the cross bar and
Anode plate connection；The cathode plate connecting rod be set between the cross bar and cathode plate, by hinged mode respectively with it is described
Cross bar is connected with cathode plate；The both ends of the cathode plate connecting rod are hinged with the end of the anode plate connecting rod of sides adjacent respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822139740.XU CN209226744U (en) | 2018-12-19 | 2018-12-19 | Integrated electrolysis equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822139740.XU CN209226744U (en) | 2018-12-19 | 2018-12-19 | Integrated electrolysis equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209226744U true CN209226744U (en) | 2019-08-09 |
Family
ID=67508441
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822139740.XU Active CN209226744U (en) | 2018-12-19 | 2018-12-19 | Integrated electrolysis equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN209226744U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111138030A (en) * | 2020-01-07 | 2020-05-12 | 温州威能环保科技有限公司 | Advanced oxidation sewage treatment equipment |
| CN113880199A (en) * | 2021-10-15 | 2022-01-04 | 山西碧海机械有限公司 | Drinking water defluorination device |
-
2018
- 2018-12-19 CN CN201822139740.XU patent/CN209226744U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111138030A (en) * | 2020-01-07 | 2020-05-12 | 温州威能环保科技有限公司 | Advanced oxidation sewage treatment equipment |
| CN113880199A (en) * | 2021-10-15 | 2022-01-04 | 山西碧海机械有限公司 | Drinking water defluorination device |
| CN113880199B (en) * | 2021-10-15 | 2024-02-13 | 山西碧海机械有限公司 | Fluorine removing device for drinking water |
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