CN206298403U - Integrative water purifying device - Google Patents
Integrative water purifying device Download PDFInfo
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- CN206298403U CN206298403U CN201621425936.XU CN201621425936U CN206298403U CN 206298403 U CN206298403 U CN 206298403U CN 201621425936 U CN201621425936 U CN 201621425936U CN 206298403 U CN206298403 U CN 206298403U
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- siphon
- sedimentation basin
- filter chamber
- purifying device
- water
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model provides a kind of integrative water purifying device, the characteristics of it has cost-effective, clean-up effect is excellent.Sedimentation basin, filter chamber are respectively provided with two groups, and two group precipitation ponds are respectively provided at the both sides of reaction tank, and Liang Zu filter chambers are respectively provided at the both side ends in two group precipitation ponds；Reaction tank, sedimentation basin, the outer of filter chamber are provided with the gutter of a ring shape；Reaction tank is provided with water inlet, and sedimentation basin is provided with mud discharging mouth, and filter chamber is provided with discharge outlet.The present apparatus by coagulation, reaction, precipitation, spoil disposal, recoil in one, solve that original facility process system mixes, efficiency is low, water quality is unstable, the shortcoming of unfavorable management；Purifier compact in design after improvement, floor space are few, stable effluent quality, convenient management simple to operate, save manpower and kinetic energy and water power consumption, and the turbidity and other index accommodations of water inlet are also wider, it is cost-effective by two groups of devices and for one group, reduce floor space.
Description
Technical field
The utility model is related to water treatment facilities, specifically integrates coagulation, reaction, precipitation, spoil disposal, recoils
Integrative water purifying device.
Background technology
In the last few years, all many-sides such as the every aspect that problem of environmental pollution spreads all in life, empty gas and water, food have
Involve, water also more and more obtains people as the important component closely bound up with people's life, its clean clean-up performance
Attention.Now, the industrial wastewater of many industrial enterprise is directly discharged into environment without treatment, a small number of enterprise's meetings
The treatment simplified is done to waste water, but the effect for the treatment of is not good, and the clean-up performance of requirement is reached far away, still can be to environment
Cause certain pollution.
The content of the invention
The utility model provide it is a kind of integrate coagulation, reaction, precipitation, spoil disposal, the integrative water purifying device that recoils,
The characteristics of it has cost-effective, clean-up effect is excellent.
The utility model realizes that above-mentioned purpose uses following technical scheme：
Integrative water purifying device, it includes：Reaction tank, sedimentation basin, filter chamber.
Sedimentation basin, filter chamber are respectively provided with two groups, and two group precipitation ponds are respectively provided at the both sides of reaction tank, Liang Zu filter chambers difference
It is located at the both side ends in two group precipitation ponds；Reaction tank, sedimentation basin, the outer of filter chamber are provided with the gutter of a ring shape；Reaction
Pond is provided with water inlet, and sedimentation basin is provided with mud discharging mouth, and filter chamber is provided with discharge outlet.
Vertical reaction dividing plate is provided with inside described reaction tank, to change the change of water velocity.
Described sedimentation basin middle part is provided with sedimentation device, and sludge hopper is provided with sedimentation basin bottom.
Described sedimentation device uses plastic sheet hot pressing hexagon nest pipe, and horizontal tilt angle is 60 degree, and inclined tube length is
1.5 meters, point two-layer is placed.
Described filter chamber middle part is provided with filter material layer, and the top of filter material layer is provided with filtered water tank, and the bottom of filter material layer is provided with clearly
Pool, filtered water tank and clear water zone are connected by the communicating pipe of side；The upper edge of the sedimentation basin corresponding with filter chamber is provided with
Elevated tank, elevated tank is communicated with corresponding sedimentation basin；Elevated tank is connected by U-shaped water inlet pipe from the bottom of filter material layer
To in filter material layer, the top of filter material layer is connected to the siphoning installation that filter chamber side is set by pipeline.
Described siphoning installation includes siphon tedge and siphon down-comer, and siphon down-comer fit is located at siphon tedge
Inside, blind plate is provided with the top of siphon tedge；The inside of siphon down-comer is provided with exhaust tube, is provided with the top of siphon down-comer
Auxiliary siphon tube outside towards pipe；The side wall of siphon tedge is provided with towards the siphon destructing tube inside filtered water tank.
Further, vertical downflow weir is provided with inside described elevated tank, the level height of downflow weir is higher than siphon
The height on down-comer top.
Further, the position of described U-shaped water inlet pipe is corresponding with the position of the pipeline for being communicated to siphoning installation.
Further, described filter chamber is provided with eight altogether, and four filter chambers are provided with accordingly per the outer of side sedimentation basin.
The utility model is had the advantages that using above-mentioned technical proposal：
The present apparatus by coagulation, reaction, precipitation, spoil disposal, recoil in one, solve original facility process system and mix, imitate
Rate is low, water quality is unstable, the shortcoming of unfavorable management；Purifier compact in design after improvement, floor space are few, effluent quality is steady
Fixed, convenient management simple to operate saves manpower and kinetic energy and water power consumption, and the turbidity intake and other index accommodations
Also it is wider.
It is cost-effective by two groups of devices and for one group, reduce floor space.
Brief description of the drawings
Fig. 1 is schematic diagram of the present utility model.
Fig. 2 is top view of the present utility model.
Specific embodiment
The utility model is described further below in conjunction with the accompanying drawings.
Integrative water purifying device as depicted in figs. 1 and 2, it includes：Reaction tank 1, sedimentation basin 2, filter chamber 3.
Sedimentation basin 2 is provided with two, and two sedimentation basins 2 are respectively provided at the both sides of reaction tank 1, and filter chamber 3 is provided with eight altogether, often
The outside of the sedimentation basin 2 of side is respectively provided with four filter chambers 3；Reaction tank 1, sedimentation basin 2, the outer of filter chamber 3 are provided with a ring shape
Gutter 4；Reaction tank 1 is provided with water inlet 501, and sedimentation basin 2 is provided with mud discharging mouth 502, and filter chamber 3 is provided with discharge outlet
503。
Vertical reaction dividing plate is provided with inside described reaction tank 1, to change the change of water velocity.
Reaction tank is made up of dividing plate reaction zone, and principle is quickly to change the change of water velocity, and speed ratio is 1：60, reaction
20 ~ 30 minutes time, its advantage is that reflection space is infinitely great, and feedwater and medicament create a good mutual collision opportunity,
It is to carry out hydraulic reverse using crest, trough to answer in course of reaction, water wadding in serial is spent greatly and in fact, increased itself proportion, by
In not having faceted portions in entirely designing, so wadding spends survivable, reaction is abundant, and being that mud chamber's creation one is good sinks
Form sediment, improve flocculation efficiency, substantial amounts of flocculant can be saved.
The middle part of sedimentation basin 2 is provided with sedimentation device 201, and sludge hopper 202 is provided with sedimentation basin bottom, and sedimentation device 201 is used
Plastic sheet hot pressing hexagon nest pipe, horizontal tilt angle is 60 degree, and inclined tube length is 1.5 meters, and point two-layer is placed.Particle precipitation speed
Degree 0.4mm/s, clear water zone rate of climb 3mm/s, its principle is, using shallow layer precipitating method, can to reduce the volume of equipment, makes list
Position aquifer yield increase, current are to use reverse flow, and water, mud go separate way, and are automatically separated, and separating rate is fast, it is ensured that effluent characteristics,
A good condition is created to next operation, mitigates the load in filter tank, while extending the backwashing period in filter tank；Under mud chamber
Portion is provided with sludge hopper, and mud is drowned oneself in being directly entered bucket type sludge hopper, reduces spoil disposal moisture content, extends sludge discharging period
The described middle part of filter chamber 3 is provided with filter material layer 301, and the top of filter material layer 301 is provided with filtered water tank 302, filter material layer 301
Bottom be provided with clear water zone 303, being connected communicating pipe 304 by side with clear water zone 303 of filtered water tank 302；With filter chamber 3
The upper edge of corresponding sedimentation basin 2 is provided with elevated tank 305, and elevated tank 305 is communicated with corresponding sedimentation basin 2；Elevated tank
305 are connected in filter material layer 301 by U-shaped water inlet pipe 306 from the bottom of filter material layer 301, and the top of filter material layer 301 is by pipe
Road is connected to the siphoning installation 6 of filter chamber side setting.
Described siphoning installation 6 includes siphon tedge 601 and siphon down-comer 602, and the fit of siphon down-comer 602 is located at
Inside siphon tedge 601, the top of siphon tedge 601 is provided with blind plate 603；The inside of siphon down-comer 602 is provided with pumping
Pipe 604, the top of siphon down-comer 602 is provided with the auxiliary siphon tube 605 towards outside pipe；Set on the side wall of siphon tedge 601
Have towards the siphon destructing tube 606 inside filtered water tank 302.
Vertical downflow weir is provided with inside described elevated tank 305, the level height of downflow weir is higher than siphon down-comer
The height on 602 tops.
The position of described U-shaped water inlet pipe 306 is corresponding with the position of the pipeline for being communicated to siphoning installation 6.
The overall working condition of equipment is to enter from the reaction zone at middle part, and water flow velocity is changed in reaction zone, is given
Water and medicament create good mutual collision opportunity, are that the sedimentation of next step lays the first stone, and the water in reaction zone is by two bottom sides
Sedimentation basin, current bottom up flow during settled in the presence of sedimentation device, soil settles into bottom
Sludge hopper, and by mud discharging mouth exclude, finally, by sedimentation basin settle water flow into both side ends filter chamber, passed through
Finally discharged after filter.
The operation principle of filter chamber is as follows：
1）The continuous operation of filtration in filter chamber, inside filtrate and surface, starts slowly to form the alluvial of filter residue.
Corresponding, gradually increased through the pressure required for filtrate by the water inlet of U-shaped water distributor.
2）What the water column between exceeding from elevated tank downflow weir to filter material surface through the pressure needed for filtrate was formed
During pressure, the water inlet in elevated tank will no longer pass through filtrate, but be directly entered siphon tedge（Law of connected vessels, it is high-order
Height of weir plate exceeds siphon down-comer tip height in water tank, in addition, siphon tedge before filtrate is not completely plugged just
Through there is water, also, siphon tedge elevation head+by the elevation head at the pressure head=downflow weir of filtrate.）
3）As the water level in siphon tedge constantly rises, when the water surface reaches the mouth of pipe of auxiliary siphon tube, water certainly should
Pipe falls, and gas effect is evacuated and held under the arm by current increases siphon pipe vacuum, meanwhile, the liquid level in siphon down-comer is due to vacuum
Effect, also can constantly rise, this further extruded in siphon pipe water surface contact, formed serial siphon effect.
4）With the carrying out of siphonage, the pressure drop on filtrate top in filter chamber, in bottom clear water zone, pressure is constant
In the case of, the clear water in the clear water zone of bottom begins to pass filter plate and enters filter material layer, and filter material layer is backwashed.It is same with this
When, the clear water in filtered water tank passes through communicating pipe to enter bottom clear water zone.The waste water for producing is backwashed by after siphon tedge, entering
Enter siphon down-comer, then drain.
5）With the carrying out of backwash, the water level in filtered water tank constantly declines, when its water level decreasing to siphon destructing tube pipe
When below mouthful, gas enters siphon destructing tube, the mouth of pipe and atmosphere, and this causes the vacuum breaking in siphon pipe, backwash to terminate,
Filtering restarts.
Claims (9)
1. integrative water purifying device, it includes：Reaction tank, sedimentation basin, filter chamber, it is characterised in that：Sedimentation basin, filter chamber respectively set
There are two groups, two group precipitation ponds are respectively provided at the both sides of reaction tank, Liang Zu filter chambers are respectively provided at the both side ends in two group precipitation ponds；
Reaction tank, sedimentation basin, the outer of filter chamber are provided with the gutter of a ring shape；Reaction tank is provided with water inlet, is set on sedimentation basin
There is mud discharging mouth, filter chamber is provided with discharge outlet.
2. integrative water purifying device according to claim 1, it is characterised in that：It is provided with vertical inside described reaction tank
Reaction dividing plate, to change the change of water velocity.
3. integrative water purifying device according to claim 1, it is characterised in that：Described sedimentation basin middle part is provided with sedimentation dress
Put, sludge hopper is provided with sedimentation basin bottom.
4. integrative water purifying device according to claim 3, it is characterised in that：Described sedimentation device is using plastic sheet warm
Pressure hexagon nest pipe, horizontal tilt angle is 60 degree, and inclined tube length is 1.5 meters, and point two-layer is placed.
5. integrative water purifying device according to claim 1, it is characterised in that：Described filter chamber middle part is provided with filtrate
Layer, the top of filter material layer is provided with filtered water tank, and the bottom of filter material layer is provided with clear water zone, filtered water tank connecting by side with clear water zone
Pipe is connected；The upper edge of the sedimentation basin corresponding with filter chamber is provided with elevated tank, elevated tank and corresponding sedimentation basin phase
It is logical；Elevated tank is connected in filter material layer by U-shaped water inlet pipe from the bottom of filter material layer, and the top of filter material layer is connected by pipeline
It is connected to the siphoning installation of filter chamber side setting.
6. integrative water purifying device according to claim 5, it is characterised in that：Described siphoning installation rises including siphon
Pipe and siphon down-comer, siphon down-comer fit are located inside siphon tedge, and blind plate is provided with the top of siphon tedge；Siphon
The inside of down-comer is provided with exhaust tube, and the auxiliary siphon tube towards outside pipe is provided with the top of siphon down-comer；Siphon tedge
Side wall is provided with towards the siphon destructing tube inside filtered water tank.
7. integrative water purifying device according to claim 5, it is characterised in that：It is provided with inside described elevated tank vertically
Downflow weir, the height of the level height of downflow weir higher than siphon down-comer top.
8. integrative water purifying device according to claim 5, it is characterised in that：The position of described U-shaped water inlet pipe with
The position for being communicated to the pipeline of siphoning installation is corresponding.
9. integrative water purifying device according to claim 1, it is characterised in that：Described filter chamber is provided with eight altogether, often
The outer of side sedimentation basin is provided with four filter chambers accordingly.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621425936.XU CN206298403U (en) | 2016-12-23 | 2016-12-23 | Integrative water purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621425936.XU CN206298403U (en) | 2016-12-23 | 2016-12-23 | Integrative water purifying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206298403U true CN206298403U (en) | 2017-07-04 |
Family
ID=59205436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621425936.XU Active CN206298403U (en) | 2016-12-23 | 2016-12-23 | Integrative water purifying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206298403U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107500434A (en) * | 2017-09-22 | 2017-12-22 | 江苏上塍环保科技有限公司 | A kind of sewage-treatment plant and tunnel Waste Water Treatment and method |
| CN112624489A (en) * | 2019-10-08 | 2021-04-09 | 天津科技大学 | Purify ecological dam device in black and odorous river course |
-
2016
- 2016-12-23 CN CN201621425936.XU patent/CN206298403U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107500434A (en) * | 2017-09-22 | 2017-12-22 | 江苏上塍环保科技有限公司 | A kind of sewage-treatment plant and tunnel Waste Water Treatment and method |
| CN112624489A (en) * | 2019-10-08 | 2021-04-09 | 天津科技大学 | Purify ecological dam device in black and odorous river course |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 471000 East No. 1 Zhongxin Avenue, Hanghe District, Luoyang City, Henan Province Patentee after: Luoyang Tiantai Environmental Technology Co., Ltd. Address before: 471000 East No. 1 Zhongxin Avenue, Hanghe District, Luoyang City, Henan Province Patentee before: Luoyang Tiantai Water Treatment Technology Co. Ltd. |
|
| CP01 | Change in the name or title of a patent holder |