CN206089269U - Device of ion more than needed and suspended solid in disposing of sewage - Google Patents
Device of ion more than needed and suspended solid in disposing of sewage Download PDFInfo
- Publication number
- CN206089269U CN206089269U CN201620981363.2U CN201620981363U CN206089269U CN 206089269 U CN206089269 U CN 206089269U CN 201620981363 U CN201620981363 U CN 201620981363U CN 206089269 U CN206089269 U CN 206089269U
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- CN
- China
- Prior art keywords
- overflow launder
- tank
- reaction tank
- sedimentation tank
- ion
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model provides a device of ion more than needed and suspended solid in disposing of sewage, including braced frame and separator, the separator is installed in braced frame, the separator is including the PH reaction tank that communicates in proper order, flocculation reaction tank, first sedimentation tank, reaction tank and second sedimentation tank thoughtlessly congeals, all be provided with the overflow launder on each reaction tank and the sedimentation tank, be provided with the water conservancy diversion through -hole on the overflow launder, through water conservancy diversion through -hole intercommunication between reaction tank and the reaction tank, water conservancy diversion through -hole on the reaction tank passes through gas -liquid separation pipe intercommunication in pipeline and the sedimentation tank, first sedimentation tank and thoughtlessly congeal the reaction tank through intercommunication pond intercommunication, be provided with the water inlet on the PH reaction tank, be provided with the delivery port on the second sedimentation tank, the sedimentation tank bottom all is provided with the silt export. The utility model discloses practiced thrift area and occupation space, reduced preparation material and cost simultaneously, avoided secondary pollution, improved flocculation ability, coagulability and sediment ability, finally made the aquatic pollute the ion and reduce an order of magnitude including the allowance.
Description
Technical field
This utility model is related to a kind of sewage-treatment plant, more particularly to it is a kind of process sewage in have more than needed ion and outstanding
The device of float.
Background technology
At present, the whole world is all worried for clean water crisis faces, although the gross amount of water resources of China occupies the 6th in the world
One of position, but still belong to serious hydropenia state.China is the country of a shortage of water resources, and water resource occupancy volume is not enough, people
Water resource only has three one-tenth of world average level, and China is industrial or agricultural big country again, huge, the numerous population of industrial or agricultural water consumption
Domestic water is also very huge, but China, using the inefficiency of water, most of contaminated water is directly discharged without process
To in rivers water system, water pollution is increasingly sharpened seriously, brings huge crisis to people's productive life.
It is with growth in the living standard and the development of economic society, increasing it was recognized that using water wisely and dirt
The importance of water process.Existing sewage disposal is through cement cesspool, coagulating basin, Aeration tank, sedimentation tank etc. mostly（Hereinafter close
Referred to as reaction tank）Several procedures are carried out, and sewage disposal process is fully exposed to outdoor, and cesspool abnormal smells from the patient is serious, easily causes attached
Band secondary pollution；Additionally, reaction tank all individualisms needed for every one procedure for processing of traditional wastewater so that total floor space with
The volume that always takes up space is big；Further, since each reaction tank is individually designed, and it is many between reaction tank to be connected with pipeline, need in process
High-pressure pump quantity and pipeline are more, need to consume extra instrument and equipment and electric power resource.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, there is provided it is a kind of process sewage in have more than needed ion and outstanding
The device of float, reduces floor space and shared spatial volume, while reducing making material and cost, it is to avoid second pollution,
Flocculation ability, coagulability and Precipitation Potential are improve, contaminated ion reduces an order of magnitude containing allowance in finally causing water.
In order to achieve the above object, the technical solution adopted in the utility model is：
A kind of device of ion and the float of having more than needed in process sewage, including support frame and separator, separator peace
It is mounted in support frame, separator includes that PH reaction tanks, flocculation tank, the first sedimentation tank, coagulation reaction tank and second are heavy
Shallow lake pond, is provided with described PH reaction tanks, flocculation tank, the first sedimentation tank, coagulation reaction tank and the second sedimentation tank
Overflow launder, is provided with stirring operation platform, described PH in described PH reaction tanks, flocculation tank and coagulation reaction tank
Water inlet is provided with reaction tank, PH reaction tanks are connected with flocculation tank by the water conservancy diversion through hole a arranged on overflow launder a, institute
State and on the overflow launder b of flocculation tank, be provided with water conservancy diversion through hole b, the gas-liquid arranged in water conservancy diversion through hole b and first sedimentation tank
The pipe shaft connection of separating pipe a, the first described sedimentation tank are connected with coagulation reaction tank by the water conservancy diversion through hole c on overflow launder c, institute
The gas-liquid separation pipe a upper ports stated are extended to above overflow launder c, be provided with water conservancy diversion and lead on the overflow launder d of the coagulation reaction tank
Hole d, water conservancy diversion through hole d are connected with the pipe shaft of the gas-liquid separation pipe b arranged in second sedimentation tank, it is described second precipitation overflow
Outlet is provided with chute e, described gas-liquid separation pipe b upper ports are extended to above overflow launder e, the first described sedimentation tank
Sludge outlet is provided with the second sedimentation tank bottom.
As preferred embodiment of the present utility model, PH reaction tanks described in the utility model, flocculation tank and mixed
Buffer board a, buffer board b and buffer board c are respectively arranged with solidifying reaction tank.
As preferred embodiment of the present utility model, the floor level face of overflow launder described in the utility model from high in the end according to
It is secondary for overflow launder a, overflow launder b, overflow launder c, overflow launder d, overflow launder e.
Used as preferred embodiment of the present utility model, overflow launder described in the utility model is set to zigzag.
As preferred embodiment of the present utility model, between coagulation reaction tank described in the utility model and the first sedimentation tank
It is provided with connection pond.
As preferred embodiment of the present utility model, overflow launder a described in the utility model, overflow launder b and overflow launder d
It is arranged on one face of pool wall.
Used as preferred embodiment of the present utility model, overflow launder c described in the utility model and overflow launder e is provided around
Pool wall one week.
Compared with prior art, the beneficial effects of the utility model are：Whole technique stream is completed by crossing a set of separator
Journey, reduces total floor space and shared spatial volume, while reducing making material and cost；Sewage is reduced using PH reaction tanks to steam
Send out second pollution for causing；Make water velocity uniform using zigzag overflow launder, preferably protect reaction tank and precipitation
The stability of precipitate, coagulum or flocculate in pond, it is to avoid each component is produced and rippled in each reaction tank, improves sedimentation tank
Precipitation Potential；Gas-liquid separation is opened using gas-liquid separation pipe, it is to avoid bubble is entered in water and impacts the impurity for having flocculated, having precipitated
Ion, reduces precipitating ion air supporting and gets up, improve the sedimentation effect of sedimentation tank.
Description of the drawings
Fig. 1 is top view of the present utility model；
Fig. 2 is this utility model reaction tank structural representation；
Fig. 3 is this utility model sedimentation tank structural representation；
Fig. 4 is this utility model overall structure diagram.
1. PH reaction tanks in figure, 2. flocculation tank, 3. the first sedimentation tank, 4. coagulation reaction tank, 5. the second sedimentation tank,
6. pond is connected, 7. stirring operation platform, 81. overflow launder a, 82 overflow launder b, 83 overflow launder c, 84. overflow launder d, 85. overflow launders
E, 91. water conservancy diversion through hole a, 92. water conservancy diversion through hole b, 93. water conservancy diversion through hole c, 94. water conservancy diversion through hole d, 10. gas-liquid separation pipe a, 11. gas-liquids
Separating pipe b, 12 water inlets, 13. outlets, 14, buffer board a, 15. buffer board b, 16. buffer board d, 17. sludge outlets,
18. support frames.
Specific embodiment
Purport of the present utility model is to overcome the deficiencies in the prior art, there is provided it is a kind of process sewage in have more than needed ion and outstanding
The device of float, reduces floor space and shared spatial volume, while reducing making material and cost, it is to avoid second pollution,
Flocculation ability, coagulability and Precipitation Potential are improve,
It is described in detail with reference to embodiment referring to the drawings, to enter to technical characteristic of the present utility model and advantage
Row deeper into annotation.
Structural representation of the present utility model as shown in accompanying drawing 1-4, it is a kind of process sewage in have more than needed ion and float
Device, including support frame 18 and separator, separator are arranged in support frame, and separator includes PH reaction tanks 1, flocculation
Reaction tank 2, the first sedimentation tank 3, coagulation reaction tank 4 and the second sedimentation tank 5, PH reaction tanks 1, flocculation tank 2 and coagulation
Be provided with stirring operation platform 7 in reaction tank 4, PH reaction tanks, flocculation tank, the first sedimentation tank, coagulation reaction tank and
Overflow launder is provided with second sedimentation tank, water inlet 12 on PH reaction tanks, is provided with, PH reaction tanks 1 are by overflow launder a81
The water conservancy diversion through hole a91 of setting is connected with flocculation tank 2, and water conservancy diversion through hole b92 is provided with the overflow launder b82 of flocculation tank,
Water conservancy diversion through hole b is connected with the pipe shaft of the gas-liquid separation pipe a10 arranged in the first sedimentation tank 3 by pipeline, and the first sedimentation tank passes through
Water conservancy diversion through hole c93 on overflow launder c83 is connected with coagulation reaction tank, and gas-liquid separation pipe a upper ports are extended to above overflow launder c,
It is provided with water conservancy diversion through hole d94 on the overflow launder d84 of coagulation reaction tank, water conservancy diversion through hole d is set by pipeline is interior with the second sedimentation tank 5
The pipe shaft connection of the gas-liquid separation pipe b11 for putting, is provided with outlet 13 on the overflow launder e95 of the second precipitation, on gas-liquid separation pipe b
Port is extended to above overflow launder e95, and the first sedimentation tank and the second sedimentation tank bottom are provided with sludge outlet 17.Sewage is from PH
The water inlet 12 arranged on reaction tank pool wall enters PH reaction tanks, carries out acid-alkali treatment, when in PH reaction tanks, the water surface exceedes overflow
During the horizontal plane of groove a, current are entered in flocculation tank by the water conservancy diversion through hole a arranged on the wall of overflow launder a sides, and same works as wadding
When waterborne in solidifying reaction tank is increased to up to overflow launder b horizontal planes, the water for processing is led to by the water conservancy diversion arranged on overflow launder b bottoms
Hole b, through Pipeline transport in gas-liquid separation pipe a, gas-liquid separation pipe a upper ports extend to the overflow launder c of the first sedimentation tank
Top, pipeline are presented " T " zag manner with gas-liquid separation pipe a connections and are connected, and the sewage processed through flocculation tank contains
The solid that flocculation is produced, can form substantial amounts of bubble during flowing and dissolve portion gas, when treatment sewage is from pipe
When road is flowed into up to gas-liquid separation pipe a, separating pipe upper end can be flowed to as gas density is little, gas is upper from gas-liquid separation pipe a's
Port is overflowed, and sewage and other density of solid conferences enter first from gas-liquid separation pipe a lower ends stream to dirty with gas-liquid separation pipe
In sedimentation tank, after precipitating after-bay and processing, lower floor's mud is excluded by sludge outlet, and the supernatant is increased to up to overflow launder c
During horizontal plane, the supernatant is entered in coagulation reaction tank by the water conservancy diversion through hole c arranged on the wall of overflow launder c sides, is contained after coagulation
The liquid of full-blown flowers from overflow launder d overflow, the liquid of spilling via Pipeline transport in gas-liquid separation pipe b, gas-liquid separation pipe b upper ends
Mouth is extended to above overflow launder d, and pipeline is equally connected with " T " zag manner with gas-liquid separation pipe b, and in water, gas is from gas-liquid separation
Pipe b mouths overflow, and water is entered in the second sedimentation tank from gas-liquid separation pipe b lower ports, and in the second sedimentation tank, lower floor's mud goes out from mud
Mouth discharge, upper strata is given off also by outlet clearly.In addition, PH reaction tanks 1, flocculation tank 2 and coagulation reaction tank 4 are processed
During sewage, the blender installed on stirring operation platform 7 starts simultaneously at work.
Buffer board a14, buffer board are respectively arranged with described PH reaction tanks, flocculation tank and coagulation reaction tank
B15 and buffer board c16, enters PH reaction tanks, flocculation tank and coagulating water by water conservancy diversion through hole stream, first passes through
Enter back into after buffer board in cell body, the hydraulic impact that buffer board is flowed in pond is less, reduce each component in each reaction tank and produce
Life is rippled, and makes reactant in reaction tank more more stable, naturally it is also possible to which, in water conservancy diversion through hole connecting line, pipeline opening is arranged
It is that, by the pool wall of the reaction tank for entering, multiple openings can be set on pipeline towards liquid, liquid is slowly flowed down along pool wall.
The floor level face of the overflow launder be followed successively by from high in the end overflow launder a81, overflow launder b82, overflow launder c83, overflow
Chute d84, overflow launder e85, after sewage enters device, fewer through the more discharges for the treatment of process, overflow launder is set accordingly
Put highly also more and more lower, floor level face refers to overflow launder tooth mouth floor level face.
Overflow launder is set to zigzag, and pool inner water amount increases, and horizontal plane is raised, when internal liquid horizontal plane reaches overflow launder
During tooth mouth floor level face, current will be overflowed from overflow tooth mouth, and the zigzag fashion of overflow launder can make water velocity uniform,
Preferably keep the stability of precipitate, coagulum or flocculate in reaction tank and sedimentation tank, it is to avoid precipitate ripples, improve heavy
The sedimentation effect in shallow lake pond.
It is provided between described coagulation reaction tank and the first sedimentation tank and connects pond 6, overflows to come after the process of the first sedimentation tank
Liquid by water conservancy diversion through hole c Jing enter to connection pond in, then again by connect pond on enter into coagulation reaction tank.
Described overflow launder a, overflow launder b and overflow launder d are arranged on one face of pool wall, certainly also can be in reactor
On multiple faces, overflow launder is set.
Described overflow launder c and overflow launder e is provided around pool wall one week, naturally it is also possible to only in a face of sedimentation tank
Upper setting overflow launder.
In this utility model, water inlet of the sewage from PH reaction tanks is entered in pond, in PH reaction tanks after buffer board a
Acid-alkali treatment is carried out inside, after the liquid after process increases to the horizontal plane of overflow launder aa, by water conservancy diversion through hole a through buffer board b
Flocculation tank is entered afterwards, after liquid increases to the horizontal plane of overflow launder b, by water conservancy diversion through hole b via Pipeline transport to gas-liquid
Separating pipe a, in liquid, gas is overflowed from gas-liquid separation pipe a upper ends, and liquid enters the first sedimentation tank from lower end, and liquid increases to excessive
After the horizontal plane of chute c, entered in connection pond by water conservancy diversion through hole c, lower floor's mud is excluded by sludge outlet, the supernatant
Entered into after buffer board c in coagulation reaction tank by connection pond, liquid increases to the horizontal plane of overflow launder d, it is logical by water conservancy diversion
Via Pipeline transport to gas-liquid separation pipe b, in liquid, gas overflows hole b from gas-liquid separation pipe b upper ends, and liquid enters the from lower end
Two sedimentation tanks, the second sedimentation tank lower floor mud are excluded by sludge outlet, after the supernatant exceedes overflow launder e horizontal planes, from going out
Discharge at the mouth of a river.
This utility model, can complete whole technological process by a set of separator, reduce total floor space and institute's duty
Between volume, while reducing making material and cost；Second pollution that sewage evaporation is caused is reduced using PH reaction tanks；Using saw
The overflow launder of profile of tooth makes water velocity uniform, preferably protects precipitate, coagulum or flocculate in reaction tank and sedimentation tank
Stability, it is to avoid in each reaction tank each component produce ripple, improve the Precipitation Potential of sedimentation tank；Made using gas-liquid separation pipe
Obtain gas-liquid to separate, it is to avoid bubble enters and the foreign ion for having flocculated, having precipitated is impacted in water, reduce precipitating ion air supporting and rise
Come, improve the sedimentation effect of sedimentation tank.
Clear, complete description is carried out to this utility model by the technical scheme in above example, it is clear that described
Embodiment be this utility model part embodiment, rather than the embodiment of whole.Based on the enforcement in this utility model
Example, the every other embodiment obtained under the premise of creative work is not made by those of ordinary skill in the art are belonged to
The scope of this utility model protection.
Claims (8)
1. a kind of device for processing ion more than needed and float in sewage, including support frame（18）And separator, separator
Installed in support frame（18）It is interior, it is characterised in that：Separator includes pH reaction tanks（1）, flocculation tank（2）, first precipitation
Pond（3）, coagulation reaction tank（4）And second sedimentation tank（5）, described pH reaction tanks（1）, flocculation tank（2）, first precipitation
Pond（3）, coagulation reaction tank（4）And second sedimentation tank（5）Overflow launder, described pH reaction tanks are provided with inside（1）, flocculation it is anti-
Ying Chi（2）And coagulation reaction tank（4）Stirring operation platform is provided with inside（7）.
2. the device of ion and the float of having more than needed in process sewage according to claim 1, it is characterised in that：The overflow
Groove includes overflow launder a（81）, overflow launder b（82）, overflow launder c（83）, overflow launder d（84）, overflow launder e（85）；Described pH is anti-
Ying Chi（1）On be provided with water inlet（12）, pH reaction tanks are by overflow launder a（81）The water conservancy diversion through hole a of upper setting（91）With flocculation
Reaction tank（2）Connection, the flocculation tank（2）Overflow launder b（82）On be provided with water conservancy diversion through hole b（92）, water conservancy diversion through hole b
（92）With first sedimentation tank（3）The gas-liquid separation pipe a of interior setting（10）Pipe shaft connection, the first described sedimentation tank（3）
By overflow launder c（83）On water conservancy diversion through hole c（93）With coagulation reaction tank（4）Connection, described gas-liquid separation pipe a（10）Upper end
Mouth extends to overflow launder c（83）Top, the overflow launder d of the coagulation reaction tank（84）On be provided with water conservancy diversion through hole d（94）, lead
Opening d（94）With the gas-liquid separation pipe b arranged in second sedimentation tank（11）Pipe shaft connection, it is described second precipitation overflow
Chute e（85）On be provided with outlet（13）, described gas-liquid separation pipe b（11）Upper port extends to overflow launder e（85）Top,
The first described sedimentation tank and the second sedimentation tank bottom are provided with sludge outlet（17）.
3. the device of ion and the float of having more than needed in process sewage according to claim 2, it is characterised in that：Described pH
Buffer board a is respectively arranged with reaction tank, flocculation tank and coagulation reaction tank（14）, buffer board b（15）And buffer board c
（16）.
4. the device of ion and the float of having more than needed in process sewage according to claim 3, it is characterised in that：The overflow
The floor level face of groove is followed successively by overflow launder a from high in the end（81）, overflow launder b（82）, overflow launder c（83）, overflow launder d（84）、
Overflow launder e（85）.
5. the device of ion and the float of having more than needed in process sewage according to claim 4, it is characterised in that：The overflow
Groove is set to zigzag.
6. the device of ion and the float of having more than needed in process sewage according to claim 5, it is characterised in that：Described is mixed
Solidifying reaction tank（4）With the first sedimentation tank（3）Between be provided with connection pond（6）.
7. the device of ion and the float of having more than needed in process sewage according to claim 6, it is characterised in that：Described overflows
Chute a（81）, overflow launder b（82）And overflow launder d（84）It is arranged on the same face of pool wall.
8. the device of ion and the float of having more than needed in process sewage according to claim 7, it is characterised in that：Described overflows
Chute c（83）With overflow launder e（85）It is provided around pool wall one week.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620981363.2U CN206089269U (en) | 2016-08-30 | 2016-08-30 | Device of ion more than needed and suspended solid in disposing of sewage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620981363.2U CN206089269U (en) | 2016-08-30 | 2016-08-30 | Device of ion more than needed and suspended solid in disposing of sewage |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206089269U true CN206089269U (en) | 2017-04-12 |
Family
ID=58474766
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620981363.2U Expired - Fee Related CN206089269U (en) | 2016-08-30 | 2016-08-30 | Device of ion more than needed and suspended solid in disposing of sewage |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206089269U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112939290A (en) * | 2021-04-20 | 2021-06-11 | 四川省太易净科技有限公司 | Advanced oxidation reactor for industrial sewage treatment |
-
2016
- 2016-08-30 CN CN201620981363.2U patent/CN206089269U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112939290A (en) * | 2021-04-20 | 2021-06-11 | 四川省太易净科技有限公司 | Advanced oxidation reactor for industrial sewage treatment |
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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: 20170412 Termination date: 20170830 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |