CN204529407U - The electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation - Google Patents
The electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation Download PDFInfo
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- CN204529407U CN204529407U CN201520194919.9U CN201520194919U CN204529407U CN 204529407 U CN204529407 U CN 204529407U CN 201520194919 U CN201520194919 U CN 201520194919U CN 204529407 U CN204529407 U CN 204529407U
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- electricity flocculation
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Abstract
The utility model relates to the electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation, comprise reactor, water inlet pipe, inlet pipe and blow-off pipe, reactor upper end open lower end closed, and the both sides of reactor upper port are respectively equipped with the deslagging chamber and drain chamber that are communicated with reactor, reactive tank is provided with in reactor, the sidewall of reactor is provided with water-in and inlet mouth, water inlet pipe to be stretched in reactor by water-in and is inserted in reactive tank, inlet pipe to be stretched in reactor by inlet mouth and is inserted in reactive tank, the bottom of reactor is provided with sewage draining exit, blow-off pipe is provided with valve, and blow-off pipe to be stretched in reactor by sewage draining exit and is communicated with reactive tank, the inwall both sides of reactive tank are respectively equipped with electrode, electrode is connected with external high pressure power electric.Device of the present utility model solves battery lead plate in electrolytic process can be deposited thing covering, causes the defect of pole plate passivation, overcomes the drawback that the electric flotation of traditional electrolyte equipment electricity flocculation separately processes.
Description
Technical field
The utility model relates to mechanical field, particularly relates to the electric flotation integrated device of high-voltage bidirectional electricity flocculation.
Background technology
At present, in existing electrolyzer, widely used mainly low-voltage electrolysis (24V or 36V) and middle piezoelectricity solution (220V), these device voltages are low, and electric current is large, and during operation, power consumption is large, battery lead plate wear rate is fast, and the phenomenon of ubiquity pole plate passivation.Again because of subnormal voltage operation, reach treatment effect needs longer reaction times, and therefore the processing power of single device is low, generally the highlyest can only reach 10m3/h.In addition, there is battery lead plate passivation phenomenon, after using for some time, battery lead plate is deposited thing and covers, make pole plate insulating, cannot electrolytic reaction be proceeded, for this reason, need a kind of energy of exploitation high-pressure electrolysis device, can power consumption be reduced, prevent battery lead plate passivation, scum silica frost can be struck off discharge again, be separated with waste water, timely device for transferring bottom deposit mud.
Utility model content
Technical problem to be solved in the utility model is to provide the electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation, solve battery lead plate in electrolytic process and can be deposited thing covering, cause the defect of pole plate " passivation ", overcome the drawback that the electric flotation of traditional electrolyte equipment electricity flocculation separately processes.
The technical scheme that the utility model solves the problems of the technologies described above is as follows: the electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation, comprise reactor, water inlet pipe, inlet pipe and blow-off pipe, described reactor upper end open lower end closed, and the both sides of described reactor upper port are respectively equipped with the deslagging chamber and drain chamber that are communicated with described reactor, reactive tank is provided with in described reactor, the sidewall of described reactor is provided with water-in and inlet mouth, described water inlet pipe to be stretched in described reactor by described water-in and is inserted in described reactive tank, described inlet pipe to be stretched in described reactor by described inlet mouth and and be inserted in described reactive tank, the bottom of described reactor is provided with sewage draining exit, described blow-off pipe is provided with valve, and described blow-off pipe to be stretched in described reactor by described sewage draining exit and is communicated with described reactive tank, the inwall both sides of described reactive tank are respectively equipped with electrode, described electrode is connected with external high pressure power electric.
The beneficial effects of the utility model are: the electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation of the present utility model, by increasing slag scraper, scum silica frost is scraped, is separated with waste water, pass into high pressure aeration additionally by inlet pipe, timing automatic aeration washes away, in time the settling be attached on electrode is washed away, avoid sedimental accumulation and cause motor passivation, setting up sewage draining exit in bottom of device, timing blowdown, avoids the normal operation that bottom deposit mud affects equipment.
Accompanying drawing explanation
Fig. 1 is the electric flotation integrated device structural representation of a kind of high-voltage bidirectional electricity flocculation of the present utility model.
In accompanying drawing, the list of parts representated by each label is as follows:
1, reactor, 2, water inlet pipe, 3, inlet pipe, 4, blow-off pipe, 5, deslagging chamber, 6, drain chamber, 7, reactive tank, 8, valve, 9, motor;
51, slag scraper, 52, slag-drip opening, 61, regulation of level valve, 62, water outlet.
Embodiment
Be described principle of the present utility model and feature below in conjunction with accompanying drawing, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
As shown in Figure 1, the electric flotation integrated device structural representation of a kind of high-voltage bidirectional electricity flocculation, comprise reactor 1, water inlet pipe 2, inlet pipe 3 and blow-off pipe 4, described reactor 1 upper end open lower end closed, and the both sides of described reactor 1 upper port are respectively equipped with the deslagging chamber 5 and drain chamber 6 that are communicated with described reactor 1, reactive tank 7 is provided with in described reactor 1, the sidewall of described reactor 1 is provided with water-in and inlet mouth, described water inlet pipe 2 to be stretched in described reactor 1 by described water-in and is inserted in described reactive tank 7, described inlet pipe 3 to be stretched in described reactor 1 by described inlet mouth and and be inserted in described reactive tank 7, the bottom of described reactor 1 is provided with sewage draining exit, described blow-off pipe 4 is provided with valve 8, and described blow-off pipe 4 to be stretched in described reactor 1 by described sewage draining exit and is communicated with described reactive tank 7, the inwall both sides of described reactive tank 7 are respectively equipped with electrode 9, the upper port of described reactor 1 is stretched out in the upper end of each described electrode 9, and described electrode 9 is connected with external high pressure power electric.
Wherein, the lower end of described reactive tank 7 is back taper, and described blow-off pipe 4 is communicated with the drift angle place of described reactive tank 7 lower end back taper.Due to equipment operationally, have a large amount of flco and produce, these flcos are understood some and are deposited on bottom described reactive tank 7, and after long-play, the mud of described reactive tank 7 bottom deposit is cumulative, finally can flood pole plate, cause equipment to be paralysed.We arrange described sewage draining exit at described reactor bottom, and can regularly be discharged by the sewage in reactive tank 7 by described valve 8, avoid the normal operation that bottom deposit mud affects equipment.
In the present embodiment, be provided with slag scraper 51 in described investigation chamber 5, be provided with slag-drip opening 52 bottom described deslagging chamber 5, described slag scraper 5 is struck off the scum silica frost of fluid surface in reactive tank 7 and is discharged by scum silica frost by described slag-drip opening 52, scum silica frost is separated with waste water, reaches the function of air supporting scrubbing.
It should be noted that, described slag scraper 51 only scrapes the scum silica frost of very little a part of liquid level, and in reactive tank 7, most of liquid level is all covered by scum silica frost, forms the reaction compartment of a semi-hermetic type, the residence time of ion in waste water that electrolysis produces can be increased to greatest extent, make reaction more abundant.
In the present embodiment, being provided with the regulation of level valve 61 for controlling water level in reactive tank 7, being provided with water outlet 62 bottom described drain chamber 6 in described drain chamber 6, the liquid in described reactive tank 7 can by the outer row of described water outlet 62.In reality, we can regulate the position of regulation of level valve 61 as required, can control the water level in described reactive tank 7.
In the present embodiment, the part that described water inlet pipe 2 inserts in described reactive tank 7 is provided with multiple inlet through hole.Can to water filling in described reactive tank 7 by described inlet through hole, to upgrade the reaction solution in described reactive tank 7.
Preferably, described multiple inlet through hole uniform intervals is arranged.By the water flowed into from described water inlet pipe 2 can be made like this to enter into uniformly in described reactive tank 7, make the reaction in reactive tank 7 more even.
In the present embodiment, described inlet pipe 3 part inserted in described reactive tank 7 is provided with multiple air inlet through hole.In actually operating, we can pass into high pressure aeration by the timing of described inlet pipe 3 in described reactive tank, are washed away by the settling be attached on electrode timely, avoid sedimental accumulation and cause electrode passivation.
Preferably, described multiple air inlet through hole uniform intervals is arranged.By the high pressure aeration passed into from described inlet pipe 3 can be made like this to enter into uniformly in described reactive tank 7, make in described reactive tank 7 electrode 9 wash away more even, without dead angle, guarantee that any position on electrode 9 does not have sediment pile.
In the prior art, when equipment runs, the two sides of one cube electrode 9 is anode and negative electrode respectively, and anode surface can continue to consume, and cathode plane does not consume, after running for some time, electrode 9 one side consumes serious, and another side does not consume, and causes electrode 9 plate to be out of shape, usually about have the pole plate of 1/3 not use just to be replaced, to cause great waste.
In the present embodiment, preferably, described electrode 9 is connected to outside automatic switchover high-voltage power supply by us, the positive and negative electrode of auto switching electric source, by negative electrode and the anode of the described electrode 9 of the switching of described external high pressure time power source.Such as starting most electrode 9 front is anode, and reverse side is negative electrode, and after equipment runs for some time, by outside auto switching electric source, electrode 9 front becomes negative electrode, and the reverse side of electrode 9 becomes anode, the negative electrode of periodical change electrode 9 like this and anode.In this way, the consumption that can make described electrode 9 two sides is uniform, and ensure that electrode 9 plate face can not be out of shape, final electrode 9 can be used up entirely, can not cause the waste of electrode 9.
The electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation of the present utility model, by increasing slag scraper, scum silica frost is scraped, is separated with waste water, pass into high pressure aeration additionally by inlet pipe, timing automatic aeration washes away, in time the settling be attached on electrode is washed away, avoid sedimental accumulation and cause motor passivation, setting up sewage draining exit in bottom of device, timing blowdown, avoids the normal operation that bottom deposit mud affects equipment.
The electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation of the present utility model, high-tension current is adopted to carry out electrolysis as power supply, during operation, voltage can regulate arbitrarily between 0 ~ 530V, electric current can regulate arbitrarily between 0 ~ 150A, greatly reduce reaching the electric energy consumed with low-tension current same treatment effect, and greatly reduce the reaction times, the device processes ability of same capacity promotes greatly.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (9)
1. the electric flotation integrated device of high-voltage bidirectional electricity flocculation, it is characterized in that: comprise reactor (1), water inlet pipe (2), inlet pipe (3) and blow-off pipe (4), described reactor (1) upper end open lower end closed, and the both sides of described reactor (1) upper port are respectively equipped with the deslagging chamber (5) and drain chamber (6) that are communicated with described reactor (1), reactive tank (7) is provided with in described reactor (1), the sidewall of described reactor (1) is provided with water-in and inlet mouth, described water inlet pipe (2) to be stretched in described reactor (1) by described water-in and is inserted in described reactive tank (7), described inlet pipe (3) to be stretched in described reactor (1) by described inlet mouth and is inserted in described reactive tank (7), the bottom of described reactor (1) is provided with sewage draining exit, described blow-off pipe (4) is provided with valve (8), and described blow-off pipe (4) to be stretched in described reactor (1) by described sewage draining exit and is communicated with described reactive tank (7), the inwall both sides of described reactive tank (7) are respectively equipped with electrode (9), described electrode (9) is connected with external high pressure power electric.
2. according to claim 1 high-voltage bidirectional electricity flocculation electric flotation integrated device, it is characterized in that: the lower end of described reactive tank (7) is back taper, and described blow-off pipe (4) is communicated with the drift angle place of described reactive tank (7) lower end back taper.
3. according to claim 1 high-voltage bidirectional electricity flocculation electric flotation integrated device, it is characterized in that: in described (5), be provided with slag scraper (51), described deslagging chamber (5) bottom is provided with slag-drip opening (52), and described slag scraper (5) is struck off the scum silica frost of reactive tank (7) interior fluid surface and discharged by scum silica frost by described slag-drip opening (52).
4. according to claim 1 high-voltage bidirectional electricity flocculation electric flotation integrated device, it is characterized in that: in described drain chamber (6), be provided with the regulation of level valve (61) for controlling reactive tank (7) interior water level, described drain chamber (6) bottom is provided with water outlet (62), and the liquid in described reactive tank (7) can be arranged outward by described water outlet (62).
5. according to claim 1 high-voltage bidirectional electricity flocculation electric flotation integrated device, it is characterized in that: the upper port of described reactor (1) is stretched out in the upper end of each described electrode (9).
6. according to claim 1 high-voltage bidirectional electricity flocculation electric flotation integrated device, it is characterized in that: the part that described water inlet pipe (2) inserts in described reactive tank (7) is provided with multiple inlet through hole.
7. the electric flotation integrated device of high-voltage bidirectional electricity flocculation according to claim 6, is characterized in that: described multiple inlet through hole uniform intervals is arranged.
8. according to claim 1 high-voltage bidirectional electricity flocculation electric flotation integrated device, it is characterized in that: described inlet pipe (3) part inserted in described reactive tank (7) is provided with multiple air inlet through hole.
9. the electric flotation integrated device of high-voltage bidirectional electricity flocculation according to claim 8, is characterized in that: described multiple air inlet through hole uniform intervals is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520194919.9U CN204529407U (en) | 2015-04-01 | 2015-04-01 | The electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520194919.9U CN204529407U (en) | 2015-04-01 | 2015-04-01 | The electric flotation integrated device of a kind of high-voltage bidirectional electricity flocculation |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105540758A (en) * | 2016-03-02 | 2016-05-04 | 四川悦承环保节能科技有限公司 | Multipole type electric flocculation and electroflotation integrated device |
| CN106277218A (en) * | 2016-08-12 | 2017-01-04 | 四川悦承环保节能科技有限公司 | A kind of device for removing phosphorous by electrolysis |
| CN108395025A (en) * | 2018-05-10 | 2018-08-14 | 长沙矿冶研究院有限责任公司 | A kind of the electric flocculation deep treatment method and electric flocculation device of waste water containing thallium |
-
2015
- 2015-04-01 CN CN201520194919.9U patent/CN204529407U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105540758A (en) * | 2016-03-02 | 2016-05-04 | 四川悦承环保节能科技有限公司 | Multipole type electric flocculation and electroflotation integrated device |
| CN106277218A (en) * | 2016-08-12 | 2017-01-04 | 四川悦承环保节能科技有限公司 | A kind of device for removing phosphorous by electrolysis |
| CN108395025A (en) * | 2018-05-10 | 2018-08-14 | 长沙矿冶研究院有限责任公司 | A kind of the electric flocculation deep treatment method and electric flocculation device of waste water containing thallium |
| CN108395025B (en) * | 2018-05-10 | 2024-03-22 | 长沙矿冶研究院有限责任公司 | Electric flocculation advanced treatment method and electric flocculation device for thallium-containing wastewater |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150805 Termination date: 20170401 |