CN209010208U - Hi-effect coagulation integration apparatus - Google Patents
Hi-effect coagulation integration apparatus Download PDFInfo
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- CN209010208U CN209010208U CN201821349031.8U CN201821349031U CN209010208U CN 209010208 U CN209010208 U CN 209010208U CN 201821349031 U CN201821349031 U CN 201821349031U CN 209010208 U CN209010208 U CN 209010208U
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- inhalant region
- settling zone
- precipitation tank
- coagulative precipitation
- water
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Abstract
The utility model relates to a kind of hi-effect coagulation integration apparatus, including coagulative precipitation tank, water inlet pipe and sludge circulation pipe, the coagulative precipitation tank is according to the inhalant region that water (flow) direction includes that sequence is arranged, settling zone and baffle area, the inhalant region is located at coagulative precipitation tank upper end, the baffle area is located at coagulative precipitation tank upper end, the settling zone is located at the lower section of inhalant region and baffle area, the water inlet pipe is extend into inhalant region, it is provided with lock phosphorus agent on the water inlet pipe, branch pipe and flocculant/flocculation aid addition branch pipe is added, the sludge circulation pipe is drawn from settling zone bottom, and outlet is located above inhalant region, for by the sludge reflux in settling zone to inhalant region.Compared with prior art, the utility model is arranged using sludge circulation, improves deposition efficiency, reduces the occupied area of sedimentation basin.This equipment is reliable for operation, is applicable to the newly-built and old factory of the waterworks of large and medium-sized scale and taps the potential and upgrade technologically.
Description
Technical field
The utility model relates to a kind of sewage disposal devices, more particularly, to a kind of hi-effect coagulation integration apparatus.
Background technique
Sewage disposal process generally comprises the processes such as coagulation, flocculation, precipitating at present, and coagulation and flocculation refer to by waste water
Middle dosing coagulant makes micelle substance therein that cohesion and flocculation occur and separate, the method to purify waste water.The former is
Because adding electrolyte, reduce or eliminate micelle eletrokinetic potential, so that colloidal solid loss of stability, takes off steady micelle and mutually coalesce
And it generates；The latter is adsorbed by polymer substance to put up a bridge, and colloidal solid is made mutually to coalesce and generate.Precipitating is generated from liquid phase
The process of one separable solid phase, or indissoluble substance is precipitated from supersaturated solution, for application main in terms of sewage treatment
Be Solid-Liquid Separation principle, utilize self gravity suffered by solid phase particles influence, the principle of natural subsidence.
Application No. is 201420525670.0 Chinese patents to disclose a kind of novel tube settling all-in-one machine, wherein cabinet
Inside by being divided into coagulating basin, flocculation basin and sedimentation basin between first partition and second partition, be equipped in the side of second partition
Deflector is equipped with coagulating basin blender in the coagulating basin, and flocculation basin blender is located at the inside of flocculation basin, in sedimentation basin
Intermediate position is equipped with inclined tube filler, and overflow weir is located at the top of inclined tube filler, and W-shaped sludge hopper is located at the lower section of inclined tube filler,
The lower part of the W-shaped sludge hopper is equipped with sludge pipe.Though the patent realizes equipment integration, there are still coagulant, flocculant
Unevenness is mixed with sewage, coagulation, flocculating effect are bad, and indissoluble substance is not easy the problems such as being discharged in sedimentation basin.
Application No. is the Chinese patents of 201720269771.X to disclose a kind of the coagulation deposition integral equipment, including case
Body, the inside of cabinet are communicated on coagulating basin by being divided into coagulating basin, flocculation basin and sedimentation basin between first partition and second partition
For the coagulation dosing pipe of coagulant to be added, the flocculation chemical feed pipe for flocculation aid to be added, first partition are communicated on flocculation basin
Upper end level be not less than liquid level highest point, the lower end of first partition contacts fixation with cabinet, by coagulating basin, flocculation basin completely every
It opens, is connected between coagulating basin, flocculation basin by the coagulation pipeline for passing through first partition；Liquid medicine decentralized institution, wadding are equipped in flocculation basin
Solidifying chemical feed pipe is connect with liquid medicine decentralized institution；The lower end of second partition contacts fixation with cabinet, and the upper end level of second partition is low
In liquid level highest point, mud scraper is additionally provided in sedimentation basin.But its structure is more responsible for, treating capacity is little.
Utility model content
The purpose of this utility model is exactly to provide a kind of highly effective coagulation to overcome the problems of the above-mentioned prior art
Precipitation integral equipment.
The purpose of this utility model can be achieved through the following technical solutions:
A kind of hi-effect coagulation integration apparatus, including coagulative precipitation tank, water inlet pipe and sludge circulation pipe,
The coagulative precipitation tank according to water (flow) direction include sequence setting inhalant region, settling zone and baffle area, it is described into
Pool is located at coagulative precipitation tank upper end, and the baffle area is located at coagulative precipitation tank upper end, and the settling zone is located at inhalant region and resistance
The lower section of septal area,
The water inlet pipe is extend into inhalant region, lock phosphorus agent is provided on the water inlet pipe, branch pipe and flocculant/help is added
Branch pipe is added in solidifying agent,
The sludge circulation pipe is drawn from settling zone bottom, and is exported and be located above inhalant region, for will be in settling zone
Sludge reflux is to inhalant region.
The water inlet pipe is the connected U-tube of sequence, and by water (flow) direction, the lock phosphorus agent is added branch pipe and is arranged in preceding, institute
It states flocculant/flocculation aid and branch pipe setting is added rear.
It locks phosphorus agent branch pipe is added by lock phosphorus agent and be added, lock phosphorus agent plays effect by two kinds of approach, and one, lock phosphorus agent is at it
During sinking, absorb water body in soluble phosphate, two, when lock phosphorus agent pass through entire water body after, can be at water body bottom
One layer of cover film, the secondary pollution of anti-water-stop body are formed in portion's bed mud.
Flocculant, flocculation aid are added branch pipe by flocculant/flocculation aid and are added in water inlet pipe, mix, make in water with water inlet
Colloidal substance unstability, and be sufficiently mixed with medicament, form wadding body.
The connected u-tube structure of sequence is arranged so that medicament is contacted with water body and the reaction time is longer, composition reacting environment.
Sludge circulation pump is provided on the sludge circulation pipe.
Sludge circulation pipe exit is provided with hydrocyclone, and hydrocyclone from sludge for isolating sand
Come, and be allocated to inhalant region, for making the tiny suspended matter formed in the grains of sand and water body form the biggish suspension of specific gravity
Group, and further it is closely knit, become larger, in settling zone rapid subsidence, achieve the effect that separation of solid and liquid.
The baffle area includes screen, and the screen opens up the channel being obliquely installed, and for passing through for water body, while making dirt
Mud is snapped down to settling zone by gravity in the channel being obliquely installed, and is catch basin on the screen, is arranged at catch basin
Water outlet.
The bottom of the coagulative precipitation tank is provided with mud discharging mouth.
Coagulative precipitation tank position conical tank.
Untreated water enters from water inlet pipe, and lock phosphorus agent is added branch pipe by lock phosphorus agent and is added, and lock phosphorus agent passes through two kinds of ways
Diameter play effect, one, lock phosphorus agent during its sinking, absorb water body in soluble phosphate, two, when lock phosphorus agent pass through
After entire water body, one layer of cover film, the secondary pollution of anti-water-stop body can be formed in water bottom bed mud.Flocculant, help it is solidifying
Agent is added branch pipe by flocculant/flocculation aid and is added in water inlet pipe, mixes with water inlet, makes the colloidal substance unstability in water, and with
Medicament is sufficiently mixed, and forms wadding body, water body initially enters Jinshui District, and in Jinshui District, hydrocyclone separates sand from sludge
Out, and it is allocated to inhalant region, with biggish outstanding for making the tiny suspended matter formed in the grains of sand and water body form specific gravity
Floating group, and further it is closely knit, become larger.
Then the water body after forming closely knit more big flocculating body enters the settling zone of coagulative precipitation tank by precipitating, and sludge sinks,
It is precipitated by settling zone, flows through the channel of screen then up, floccule body is precipitated in screen channel and slided in the effect of gravity
Under, floccule body constantly settling zone bottom accumulate, formed sludge, the supernatant collection after mud-water separation into catch basin, from
Outlet outflow.
Settling zone configures dirt mud circulation pipe and is allocated to inhalant region for separating sand from sludge.The coagulation
The bottom of sedimentation basin is provided with mud discharging mouth.It is discharged when there are many sludge.
Compared with prior art, the utility model have the following advantages that and the utility model has the advantages that
1, the utility model water inlet pipe is the connected U-tube of sequence, the connected u-tube structure of sequence be arranged so that medicament with
Water body contact and reaction time are longer, constitute reacting environment.
2, branch pipe is added in the phosphorus agent of setting lock on water inlet pipe and branch pipe is added in flocculant/flocculation aid, and lock phosphorus agent passes through lock phosphorus
Agent is added branch pipe and is added, and lock phosphorus agent plays effect by two kinds of approach, one, lock phosphorus agent during its sinking, absorb water body
In soluble phosphate, two, when lock phosphorus agent pass through entire water body after, one layer of covering can be formed in water bottom bed mud
Film, the secondary pollution of anti-water-stop body.
3, it uses sludge circulation to be arranged, the grains of sand can increase the specific gravity of micro-floccule in sludge, improve deposition efficiency, subtract
The occupied area of small sedimentation basin.
4, the investment of this plant engineering is low, reliable for operation, is applicable to the newly-built and old factory of the waterworks of large and medium-sized scale
Tap the potential and upgrade technologically.
Detailed description of the invention
Fig. 1 is hi-effect coagulation integration apparatus structural schematic diagram.
Specific embodiment
The utility model is described in detail in the following with reference to the drawings and specific embodiments.
Embodiment
A kind of hi-effect coagulation integration apparatus, such as Fig. 1, including coagulative precipitation tank 1, water inlet pipe 2 and sludge circulation pipe
3, coagulative precipitation tank 1 is located at mixed according to inhalant region 4, settling zone 5 and the baffle area 6 that water (flow) direction includes that sequence is arranged, inhalant region 4
Solidifying 1 upper end of sedimentation basin, baffle area 6 are located at 1 upper end of coagulative precipitation tank, and settling zone 5 is located at the lower section of inhalant region 4 and baffle area 6, into
Water pipe 2 is extend into inhalant region 4, lock phosphorus agent is provided on water inlet pipe 2, branch pipe 7 and flocculant/flocculation aid addition branch pipe 8 is added,
Sludge circulation pipe 3 is drawn from 5 bottom of settling zone, and is exported and be located at the top of inhalant region 4, for by the sludge reflux in settling zone 5
To inhalant region 4.
Wherein, water inlet pipe 2 is the connected U-tube of sequence, by water (flow) direction, locks phosphorus agent and the setting of branch pipe 7 is added in preceding, flocculation
Agent/flocculation aid is added branch pipe 8 and is arranged rear.It locks phosphorus agent and the addition of branch pipe 7 is added by lock phosphorus agent, lock phosphorus agent passes through two kinds of approach hairs
Wave effect, one, lock phosphorus agent during its sinking, absorb the soluble phosphate in water body, two, when lock phosphorus agent pass through it is entire
After water body, one layer of cover film, the secondary pollution of anti-water-stop body can be formed in water bottom bed mud.Flocculant, flocculation aid are logical
It crosses flocculant/flocculation aid to be added in the addition water inlet pipe 2 of branch pipe 8, is mixed with water inlet, make the colloidal substance unstability in water, and and medicine
Agent is sufficiently mixed, and forms wadding body.The connected u-tube structure of sequence is arranged so that medicament is contacted with water body and the reaction time is longer,
Constitute reacting environment.
Sludge circulation pump 9 is provided on sludge circulation pipe 3.3 exit of sludge circulation pipe is provided with hydrocyclone 10, water
Power cyclone is allocated to inhalant region 4 for separating sand from sludge, for be formed in the grains of sand and water body
Tiny suspended matter forms biggish the suspensions group of specific gravity, and it is further it is closely knit, become larger, in settling zone rapid subsidence, reach solid-liquid
Isolated effect.
Baffle area 6 includes screen 12, and screen 12 opens up the channel being obliquely installed, for passing through for water body, while making sludge
It is snapped down to settling zone 5 by gravity in the channel being obliquely installed, is catch basin 13 on screen 12, is arranged at catch basin 13
Water outlet 11.
The bottom of coagulative precipitation tank 1 is provided with mud discharging mouth 14.1 conical tank of coagulative precipitation tank.
Untreated water enters from water inlet pipe, and lock phosphorus agent is added branch pipe 7 by lock phosphorus agent and is added, and lock phosphorus agent passes through two kinds of ways
Diameter play effect, one, lock phosphorus agent during its sinking, absorb water body in soluble phosphate, two, when lock phosphorus agent pass through
After entire water body, one layer of cover film, the secondary pollution of anti-water-stop body can be formed in water bottom bed mud.Flocculant, help it is solidifying
Agent is added branch pipe 8 by flocculant/flocculation aid and is added in water inlet pipe 2, mixes with water inlet, makes the colloidal substance unstability in water, and
It is sufficiently mixed with medicament, forms wadding body, water body initially enters Jinshui District, and in Jinshui District, hydrocyclone divides sand from sludge
It separates out and, and be allocated to inhalant region 4, with biggish for making the tiny suspended matter formed in the grains of sand and water body form specific gravity
Suspend group, and further it is closely knit, become larger.
Then the water body after forming closely knit more big flocculating body enters the settling zone 5 of coagulative precipitation tank 1 by precipitating, under sludge
It is heavy, it is precipitated by settling zone, flows through the channel of screen then up, floccule body precipitates in screen channel and in the effect of gravity
Slide, floccule body constantly settling zone bottom accumulate, formed sludge, the supernatant collection after mud-water separation into catch basin,
It is flowed out from outlet.
Settling zone configures dirt mud circulation pipe and is allocated to inhalant region for separating sand from sludge.Coagulating sedimentation
The bottom in pond 1 is provided with mud discharging mouth 14.It is discharged when there are many sludge.
It can understand the above description of the embodiments is intended to facilitate those skilled in the art and use practical
It is novel.Person skilled in the art obviously easily can make various modifications to these embodiments, and illustrating herein
General Principle be applied in other embodiments without having to go through creative labor.Therefore, the utility model is not limited to above-mentioned
Embodiment, those skilled in the art's announcement according to the present utility model, do not depart from improvement that the utility model scope is made and
Modification should be all within the protection scope of the utility model.
Claims (7)
1. a kind of hi-effect coagulation integration apparatus, which is characterized in that including coagulative precipitation tank (1), water inlet pipe (2) and sludge
Circulation pipe (3),
The coagulative precipitation tank (1) is according to the inhalant region (4) that water (flow) direction includes sequence setting, settling zone (5) and baffle area
(6), the inhalant region (4) is located at coagulative precipitation tank (1) upper end, and the baffle area (6) is located at coagulative precipitation tank (1) upper end, institute
The lower section that settling zone (5) is located at inhalant region (4) Yu baffle area (6) is stated,
The water inlet pipe (2) extend into inhalant region (4), lock phosphorus agent is provided on the water inlet pipe (2), branch pipe (7) are added and wad a quilt with cotton
Branch pipe (8) are added in solidifying agent/flocculation aid,
The sludge circulation pipe (3) is drawn from settling zone (5) bottom, and is exported and be located above inhalant region (4), is used for settling zone
(5) sludge reflux in is to inhalant region (4).
2. a kind of hi-effect coagulation integration apparatus according to claim 1, which is characterized in that the water inlet pipe (2)
For the connected U-tube of sequence, by water (flow) direction, the lock phosphorus agent is added branch pipe (7) and is arranged in preceding, the flocculant/flocculation aid
Branch pipe (8) are added to be arranged rear.
3. a kind of hi-effect coagulation integration apparatus according to claim 1, which is characterized in that the sludge circulation pipe
(3) sludge circulation pump (9) are provided on.
4. a kind of hi-effect coagulation integration apparatus according to claim 1, which is characterized in that the sludge circulation pipe
(3) exit is provided with hydrocyclone (10).
5. a kind of hi-effect coagulation integration apparatus according to claim 1, which is characterized in that the baffle area (6)
Including screen (12), the screen (12) opens up the channel being obliquely installed, and for passing through for water body, while sets sludge in inclination
It is snapped down to settling zone (5) in the channel set by gravity, is catch basin (13) on the screen (12), at catch basin (13)
It is arranged water outlet (11).
6. a kind of hi-effect coagulation integration apparatus according to claim 1, which is characterized in that the coagulative precipitation tank
(1) bottom is provided with mud discharging mouth (14).
7. a kind of hi-effect coagulation integration apparatus according to claim 1, which is characterized in that the coagulative precipitation tank
(1) position conical tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821349031.8U CN209010208U (en) | 2018-08-21 | 2018-08-21 | Hi-effect coagulation integration apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821349031.8U CN209010208U (en) | 2018-08-21 | 2018-08-21 | Hi-effect coagulation integration apparatus |
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| Publication Number | Publication Date |
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| CN209010208U true CN209010208U (en) | 2019-06-21 |
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ID=66831395
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| CN201821349031.8U Active CN209010208U (en) | 2018-08-21 | 2018-08-21 | Hi-effect coagulation integration apparatus |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108911086A (en) * | 2018-08-21 | 2018-11-30 | 上海景青绿环境科技有限公司 | A kind of hi-effect coagulation integration apparatus |
| CN110921886A (en) * | 2019-11-01 | 2020-03-27 | 象山德曼机械有限公司 | Concentration device for solid-liquid separation and dehydration |
| CN111170559A (en) * | 2020-01-07 | 2020-05-19 | 无锡市远洲环保科技有限公司 | Integrated sewage treatment equipment |
-
2018
- 2018-08-21 CN CN201821349031.8U patent/CN209010208U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108911086A (en) * | 2018-08-21 | 2018-11-30 | 上海景青绿环境科技有限公司 | A kind of hi-effect coagulation integration apparatus |
| CN110921886A (en) * | 2019-11-01 | 2020-03-27 | 象山德曼机械有限公司 | Concentration device for solid-liquid separation and dehydration |
| CN111170559A (en) * | 2020-01-07 | 2020-05-19 | 无锡市远洲环保科技有限公司 | Integrated sewage treatment equipment |
| CN111170559B (en) * | 2020-01-07 | 2022-02-18 | 无锡市远洲环保科技有限公司 | Integrated sewage treatment equipment |
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