CN208008524U - The comprehensive utilization device for water process of flocculating - Google Patents
The comprehensive utilization device for water process of flocculating Download PDFInfo
- Publication number
- CN208008524U CN208008524U CN201721694628.1U CN201721694628U CN208008524U CN 208008524 U CN208008524 U CN 208008524U CN 201721694628 U CN201721694628 U CN 201721694628U CN 208008524 U CN208008524 U CN 208008524U
- Authority
- CN
- China
- Prior art keywords
- flocculant
- water
- communicated
- flocculation
- run
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 238000000034 method Methods 0.000 title claims abstract description 21
- 230000003311 flocculating effect Effects 0.000 title description 3
- 238000005189 flocculation Methods 0.000 claims abstract description 33
- 230000016615 flocculation Effects 0.000 claims abstract description 33
- 238000004062 sedimentation Methods 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 239000002351 wastewater Substances 0.000 claims abstract description 17
- 238000007599 discharging Methods 0.000 claims abstract description 16
- 238000011282 treatment Methods 0.000 claims abstract description 13
- 239000010802 sludge Substances 0.000 claims description 15
- 238000004065 wastewater treatment Methods 0.000 abstract description 6
- 238000000746 purification Methods 0.000 abstract description 3
- 238000001556 precipitation Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 10
- 239000007787 solid Substances 0.000 description 9
- 239000000725 suspension Substances 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000008394 flocculating agent Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000375 suspending agent Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a kind of comprehensive utilization devices of flocculation water process, the comprehensive utilization device of the flocculation water process includes flocculant tank, flocculant adding mouth is provided at the top of flocculant tank, bottom is communicated with liquid discharging tube, flow control valve and flow pump are disposed on liquid discharging tube, the end of liquid discharging tube is communicated with the flocculation treatment pond for handling waste water, the bottom in flocculation treatment pond is communicated with sedimentation basin, the upper end of sedimentation basin is communicated with run-off, the top of run-off is communicated to the top of flocculant tank by return duct, and controlled valve is provided on return duct.The waste water for adding flocculant is precipitated by sedimentation basin, and the water purification of the final settling tanks of precipitation at the middle and upper levels is made to be flowed into run-off, the water conveying on run-off upper layer is returned in flocculant tank, water resource is not only saved, and also contain the flocculant not reacted in the water on run-off upper layer, it can continue to be added in waste water to use, reduce the use of flocculant, reduce cost for wastewater treatment.
Description
Technical field
The utility model is related to sewage treatment equipment technical fields, and in particular to a kind of comprehensive utilization dress of flocculation water process
It sets.
Background technology
In During Industrial Wastewater Treatment Process, usually contain solid suspension in pending waste water water body, these solids are outstanding
Float belongs to the harmful substance in water body, and some of which solid suspension can be removed by way of natural sedimentation, still
Some solid suspensions are difficult to remove by way of natural sedimentation, for the solid suspension of the type, it usually needs Xiang Shui
A certain concentration and the flocculant of ratio are added in body, pass through adherency mutual between solid suspension and flocculant, bridge formation and friendship
Connection acts on so that solid suspension is agglomerated and precipitated rapidly, and then is filtered out.
In the solid suspension that can not be precipitated in using flocculant removal water body, need first to be configured to wad a quilt with cotton by flocculation dilution agent
Solidifying agent solution, 0.01 ‰~0.1 ‰ mass are made at this point, need to add a certain proportion of flocculant into a large amount of water and be diluted
The solution of concentration, the solution are used for being added in sewage.Currently, during dilution configures flocculant solution, often
It needs to expend a large amount of water resource, after flocculant solution is added in waste water, the flocculation that is not partly combined with solid suspension
Agent can not recycle so that flocculant usage amount rises, and flocculant is more expensive, these all cause waste water flocculating processing cost
Increase.
For these reasons, it is necessary to which a kind of comprehensive utilization device of flocculation water process is provided.
Utility model content
It is existing to solve the technical problem to be solved by the present invention is to provide a kind of comprehensive utilization device of flocculation water process
Have when using flocculant process waste water in technology, causes water resource waste and the big technical problem of flocculant usage.
In order to solve the above technical problems, the technical solution adopted in the utility model is：
A kind of comprehensive utilization device of flocculation water process is provided, includes the flocculant tank for configuring flocculant solution, it should
Flocculant adding mouth is provided at the top of flocculant tank, bottom is communicated with liquid discharging tube, and flow control is disposed on the liquid discharging tube
Valve and flow pump processed, the end of the liquid discharging tube are communicated with the flocculation treatment pond for handling waste water, the bottom in the flocculation treatment pond
It is communicated with sedimentation basin, the upper end of the sedimentation basin is communicated with run-off, and the top of the run-off is communicated to this by return duct
The top of flocculant tank, and it is provided with controlled valve on the return line.
Preferably, sludge pipe is equipped among the bottom of the sedimentation basin, be disposed on the sludge pipe spoil disposal control valve and
The end of sludge pump, the sludge pipe is communicated with filter press, and the water outlet of the filter press is communicated to this by filter press outlet conduit
The front bottom end of sedimentation basin.
Preferably, blender is equipped in the flocculation treatment pond.
Preferably, the return duct is more than the height of the flocculant tank top with the Altitude of the run-off junction.
Preferably, the return duct corresponding position is provided with water pump, for the water in the run-off to be drawn into this
In flocculant tank.
Preferably, it is more than the Altitude at the top of the sedimentation basin in the Altitude of the water outlet of the filter press.
The advantageous effects of the utility model are：
Water resource is saved, and flocculant can be recycled, reduces the use of flocculant, reduces cost for wastewater treatment.This practicality
The comprehensive utilization device of the flocculation water process of novel offer precipitates the waste water for adding flocculant by sedimentation basin, and makes to sink
The water purification of the final settling tanks in shallow lake at the middle and upper levels is flowed into run-off, after further being precipitated in run-off, by run-off upper layer
Water conveying return in flocculant tank, not only saved water resource in this way, and also contain in the water on run-off upper layer do not occur it is anti-
The flocculant answered can continue to be added in waste water to use, reduce the use of flocculant after conveying returns in flocculant tank,
Greatly reduce cost for wastewater treatment.
Description of the drawings
Fig. 1 is the structural schematic diagram of the comprehensive utilization device embodiment 1 of the utility model flocculation water process.
In figure, each label is illustrated as：1- flocculants tank, 101- flocculants adding mouth, 102- liquid discharging tubes, 103- flow controls
Valve, 104- flow pumps, 2- flocculation treatments pond, 201- blenders, 3- sedimentation basins, 301- sludge pipes, 302- spoil disposals control valve, 303-
Sludge pump, 304- filter presses, 305- filter press outlet conduit 4- run-offs, 401- return ducts, 402- controlled valves.
Specific implementation mode
Illustrate specific embodiment of the present utility model with reference to the accompanying drawings and examples, but following embodiment only uses
It is described in detail the utility model, does not limit the scope of the utility model in any way.
Embodiment 1：
It please refers to Fig.1.
The comprehensive utilization device for the flocculation water process that the utility model embodiment provides includes for configuring flocculant solution
Flocculant tank 1, the top of flocculant tank 1 is provided with flocculant adding mouth 101, and bottom is communicated with liquid discharging tube 102, liquid discharging tube
Flow control valve 103 and flow pump 104 are disposed on 102, the end of liquid discharging tube 102 is communicated with the wadding for handling waste water
Solidifying processing pond 2, flocculation treatment pond 2 is interior to be equipped with blender 201, and blender 201 is used for powdered flocculant solution and waste water
It is sufficiently mixed, the bottom in flocculation treatment pond 2 is communicated with sedimentation basin 3, and the upper end of sedimentation basin 3 is communicated with run-off 4, run-off
4 top is communicated to the top of flocculant tank 1 by return duct 401, and controlled valve 402 is provided on return duct 401.
After flocculant is fully reacted with waste water in flocculation treatment pond 2, into sedimentation basin 3, by sedimentation basin 3 to addition
The waste water of flocculant is precipitated, and the water purification of the final settling tanks 3 of precipitation at the middle and upper levels is made to be flowed into run-off 4, in run-off 4
In further precipitate after, turn on the switch valve 402, the conveying of the water on 4 upper layer of run-off returned in flocculant tank 1, so not
Water resource has only been saved, and has also contained the flocculant not reacted in the water on 4 upper layer of run-off, conveying returns in flocculant tank
Afterwards, it can continue to be added in waste water to use, reduce the use of flocculant, reduce cost for wastewater treatment.
Return duct 401 and the Altitude of 4 junction of run-off are more than the height at 1 top of flocculant tank, so that overflow
Water in pond 4 can flow automatically in flocculant tank 1.Certainly, in other embodiments, water pump can also be set on return duct,
The water in run-off is drawn into flocculant tank by water pump.
Further, it is equipped with sludge pipe 301 among the bottom of sedimentation basin 3, spoil disposal control is disposed on sludge pipe 301
The end of valve 302 and sludge pump 303, sludge pipe 301 is communicated with filter press 304, and the water outlet of filter press 304 is gone out by filter press
Waterpipe 305 is communicated to the front bottom end of sedimentation basin 3.The Altitude of the water outlet of filter press 304 is more than 3 top of sedimentation basin
Altitude, so that the water in filter press 304 can flow automatically in sedimentation basin 3.Sludge pump 303 is by the mud of 3 bottom of sedimentation basin
Be transported in filter press 304, filter press 304 can promote to be separated by solid-liquid separation, make the water of separation enter in sedimentation basin 3 continue participate in follow
Ring is further reduced the usage amount of water resource.
Based on above example, the comprehensive utilization device of flocculation water process provided by the utility model includes for configuring wadding
The flocculant tank of solidifying agent solution, is provided with flocculant adding mouth at the top of flocculant tank, and bottom is communicated with liquid discharging tube, on liquid discharging tube
It is disposed with flow control valve and flow pump, the end of liquid discharging tube is communicated with the flocculation treatment pond for handling waste water, flocculation
The bottom of processing pond is communicated with sedimentation basin, and the upper end of sedimentation basin is communicated with run-off, and the top of run-off passes through return duct
It is communicated to the top of flocculant tank, and is provided with controlled valve on return duct, by using the comprehensive profit of the flocculation water process
With device, water resource is saved, and flocculant can be recycled, reduced the use of flocculant, reduced the cost of wastewater treatment.
The utility model is described in detail above in conjunction with drawings and examples, still, the skill of technical field
Art personnel, can also be to each specific in above-described embodiment it is understood that without departing from the purpose of the present invention
Parameter changes, and forms multiple specific embodiments, is the common variation range of the utility model, no longer detailed one by one herein
It states.
Claims (6)
1. a kind of comprehensive utilization device of flocculation water process, which is characterized in that include the flocculant for configuring flocculant solution
Tank is provided with flocculant adding mouth at the top of the flocculant tank, and bottom is communicated with liquid discharging tube, is set gradually on the liquid discharging tube
There are flow control valve and flow pump, the end of the liquid discharging tube to be communicated with the flocculation treatment pond for handling waste water, the flocculation
The bottom of processing pond is communicated with sedimentation basin, and the upper end of the sedimentation basin is communicated with run-off, and the top of the run-off is logical
It crosses return duct and is communicated to the top of the flocculant tank, and controlled valve is provided on the return duct.
2. the comprehensive utilization device of flocculation water process according to claim 1, which is characterized in that the bottom of the sedimentation basin
Centre is equipped with sludge pipe, and spoil disposal control valve and sludge pump, the end connection of the sludge pipe are disposed on the sludge pipe
There are filter press, the water outlet of the filter press to be communicated to the front bottom end of the sedimentation basin by filter press outlet conduit.
3. the comprehensive utilization device of flocculation water process according to claim 1, which is characterized in that in the flocculation treatment pond
Equipped with blender.
4. it is according to claim 1 flocculation water process comprehensive utilization device, which is characterized in that the return duct with it is described
The Altitude of run-off junction is more than the height of the flocculant tank top.
5. the comprehensive utilization device of flocculation water process according to claim 1, which is characterized in that be arranged on the return duct
There is water pump, for the water in the run-off to be drawn into the flocculant tank.
6. the comprehensive utilization device of flocculation water process according to claim 2, which is characterized in that the water outlet of the filter press
The Altitude of mouth is more than the Altitude at the top of the sedimentation basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721694628.1U CN208008524U (en) | 2017-12-08 | 2017-12-08 | The comprehensive utilization device for water process of flocculating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721694628.1U CN208008524U (en) | 2017-12-08 | 2017-12-08 | The comprehensive utilization device for water process of flocculating |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208008524U true CN208008524U (en) | 2018-10-26 |
Family
ID=63879880
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721694628.1U Expired - Fee Related CN208008524U (en) | 2017-12-08 | 2017-12-08 | The comprehensive utilization device for water process of flocculating |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208008524U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118878112A (en) * | 2024-06-28 | 2024-11-01 | 贵州瓮福蓝天氟化工股份有限公司 | Wastewater recovery and treatment device |
-
2017
- 2017-12-08 CN CN201721694628.1U patent/CN208008524U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118878112A (en) * | 2024-06-28 | 2024-11-01 | 贵州瓮福蓝天氟化工股份有限公司 | Wastewater recovery and treatment device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181026 Termination date: 20191208 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |