CN206266393U - A kind of bio-contact oxidation sewage disposal system - Google Patents
A kind of bio-contact oxidation sewage disposal system Download PDFInfo
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- CN206266393U CN206266393U CN201621164228.5U CN201621164228U CN206266393U CN 206266393 U CN206266393 U CN 206266393U CN 201621164228 U CN201621164228 U CN 201621164228U CN 206266393 U CN206266393 U CN 206266393U
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- oxidation
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Abstract
The utility model discloses a kind of bio-contact oxidation sewage disposal system, filtering ponds including passing sequentially through pipeline connection, regulating reservoir, dosing reaction tank, preliminary sedimentation tank, hydrolysis acidification pool, contact-oxidation pool and second pond, hydrolysis acidification pool, contact-oxidation pool is respectively connected with aerator, second pond and preliminary sedimentation tank are provided with sludge outlet, sludge outlet is connected by sludge pump with sludge-tank pipeline, the inside of hydrolysis acidification pool and contact-oxidation pool is disposed with sludge outlet from the bottom to top, water inlet, distribution device, packing layer and delivery port, distribution device is connected with the aerator of outside, the filler in packing layer in hydrolysis acidification pool and contact-oxidation pool is selected from suspension type soft-filler, suspension Ball-type packing, half suspension Ball-type packing, at least one in polyhedron empty ball filler.The utility model has volumetric loading high, and biosolids amount is more in pond, with stronger water quality adaptability, does not exist sludge bulking problem after treatment, and floor space is small.
Description
Technical field
The utility model is related to sewage treatment area, more particularly to a kind of bio-contact oxidation sewage disposal system.
Background technology
At present, conventional sewage treatment process system has oxidation ditch system, sequencing batch activated sludge system (SBR).Oxidation
Though ditch technology is widely used in large- and-medium size cities sewage treatment plant, water quality treatment is good, and sludge age is long, the function with denitrogenation,
But compare with common Activated Sludge Process, high energy consumption itself, and floor space is big, it is big by place restricted influence, and operation
Middle high cost, is not easy to popularization and application；And the shortcoming of SBR technologies is that pond appearance and utilization rate of equipment and installations are low, floor space is big, operation pipe
Reason is complicated, and automatic control level requirement is high, i.e. its popularization and application are equally limited by factory site, at the same it is high to control accuracy requirement, and efficiency
It is low, also it is not easy to widespread adoption.Therefore, a kind of strong applicability, operational management simplicity are needed badly, floor space is small, and utilization rate is high
Sewage disposal system.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of bio-contact oxidation sewage disposal system, and the system is fitted
With property is strong, operational management is easy, floor space is small, and utilization rate is high.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is a kind of bio-contact oxidation sewage disposal system
System, including pass sequentially through filtering ponds, regulating reservoir, dosing reaction tank, preliminary sedimentation tank, hydrolysis acidification pool, the catalytic oxidation of pipeline connection
Pond, second pond, hydrolysis acidification pool, contact-oxidation pool are respectively connected with aerator, and filtering ponds are internally provided with grid, inside regulating reservoir
Submersible sewage pump is provided with, second pond and preliminary sedimentation tank are provided with sludge outlet, and sludge outlet is connected by sludge pump with sludge-tank pipeline
Connect, water inlet is provided with filtering ponds, and delivery port is provided with second pond, the inside of hydrolysis acidification pool and contact-oxidation pool is equal
Sludge outlet, water inlet, distribution device, packing layer and delivery port are disposed with from the bottom to top, and distribution device equably divides
It is distributed in contact-oxidation pool and hydrolysis acidification pool and is connected with outside aerator, filling out in hydrolysis acidification pool and contact-oxidation pool
Filler in the bed of material is selected from suspension type soft-filler, suspension Ball-type packing, half suspension Ball-type packing, polyhedron empty ball filler
At least one.
Preferably, the packing layer in hydrolysis acidification pool and/or contact-oxidation pool includes filler upper strata and filler lower floor, filler
Aperture of the aperture of the material of lower floor more than the material on filler upper strata.
It is further preferred that the filler in packing layer is fixed by suspension holdfast, suspension holdfast is respectively arranged at contact oxygen
Change the upper and lower part in pond, the suspension holdfast that filler is fixed on top forms filler upper strata, and filler is fixed on the suspension branch of bottom
Frame forms filler lower floor.
Preferably, regulating reservoir is internally provided with the dividing plate perpendicular to bottom of pond, and dividing plate both sides are provided with current boost motor.
Preferably, dosing reaction tank is internally provided with agitator, and is provided through outside it inside dosing reaction tank
Dispensing pipeline, dispensing pipeline is connected by measuring pump with filling pocket pipeline.
Preferably, it is provided with elevator pump on the pipeline between regulating reservoir and dosing reaction tank.
Preferably, the delivery port of second pond uses triangular-notch weir delivery port.
Using above-mentioned technical proposal, it is combined with catalytic oxidation treatment by by homogeneous, coagulation, hydrolysis acidification, first profit
Pond is set to homogenize with regulating reservoir, then by adding medicament so that SS, COD reaction etc. forms alumina blossom particles in dosing reaction tank
Thing, and then decomposed by hydrolysis acidification pool in bottom of pond by gravitational settling, it is that dissolubility is organic by insoluble hydrolysis of organic matter
Thing, the macromolecular substances of difficult for biological degradation is converted into the small-molecule substance of easily biological-degradable, finally by contact-oxidation pool
The action breaks of various bacteria are water, carbon dioxide etc..Packing specific area is big in contact-oxidation pool, and aerobic condition is good, contact
Oxidation pond has volumetric loading high, and biosolids amount is more in pond, with stronger water quality adaptability, strong applicability, treatment
Do not exist sludge bulking problem afterwards.
Brief description of the drawings
Fig. 1 is a kind of bio-contact oxidation sewage disposal system schematic flow sheet of the utility model.
Specific embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings.Herein it should be noted that
It is used to help understand the utility model for the explanation of these implementation methods, but does not constitute to restriction of the present utility model.This
Outward, as long as technical characteristic involved in the utility model disclosed below each implementation method does not constitute conflict each other
Can just be mutually combined.
A kind of bio-contact oxidation sewage disposal system, including pass sequentially through filtering ponds, regulating reservoir, the dosing of pipeline connection
Reaction tank, preliminary sedimentation tank, hydrolysis acidification pool, contact-oxidation pool, second pond.First, sewage enters filtering ponds by water inlet, filtering
Pond is internally provided with grid, is used to remove soft twister, larger solid particle debris and drift in sewage, so that after protecting
Continuous work water pump service life simultaneously reduces system treatment live load.Regulating reservoir is provided with submersible sewage pump, dividing plate and current boosting
Device, dividing plate is vertical with regulating reservoir bottom of pond after installation to be square, and can prevent sewage in pond internal short-circuit, and passes through to set latent dirt
Pump can be by the tear of the materials such as sewage medium-length fibre, bag, band, grass, cloth, cut-out, and then smooth discharge, further reduces follow-up water
The load of matter treatment, and being provided with beneficial to effluent cycle is made for current boost motor, make it homogenize.Sewage after the completion for the treatment of leads to
Cross elevator pump and be promoted to dosing reaction tank, the main effect of dosing reaction tank is to make SS, COD therein anti-by chemical agent
Should wait to form alumina blossom particles thing, dosing reaction tank is internally provided with agitator, and is provided through outside it in dosing reaction tank
The dispensing pipeline in portion, dispensing pipeline is connected by measuring pump with filling pocket pipeline.When need to add medicament, it is only necessary in filling pocket
Liquid is configured, measuring pump has been then turned on and is calculated input amount.After in flocculation sediment in dosing reaction tank, the sewage is then hydrolyzed
Acidification pool, is dissolved organic matter by insoluble hydrolysis of organic matter, and the macromolecular substances of difficult for biological degradation are converted into easy biology
The small-molecule substance of degraded.Two of hydrolysis acidification pool most basic effects are：One is to improve wastewater biodegradability, and macromolecular is had
Machine thing is converted into small molecule；Two is to remove the COD in waste water, partial organic substances degraded synthesis own cells.In this implementation, hydrolysis
The structure of acidification pool is consistent with the structure of contact-oxidation pool, is disposed with sludge outlet, water inlet, cloth inside it from the bottom to top
Device of air, packing layer and delivery port, but its running differs, and hydrolysis acidification belongs to half anaerobic digestion process, includes
Two processes of hydrolysis and acidifying, wherein acidifying belongs to the process of anaerobic digestion, but its target for being pursued with complete anaerobic digestion
Difference, its object is to non-dissolved organic matter in raw water is changed into dissolved organic matter, so as to contribute to the aerobic of later stage
Biological treatment, i.e. contact-oxidation pool.And in order to improve the effect for the treatment of, can be by inside hydrolysis acidification pool or/and contact-oxidation pool
Packing layer be arranged to filler upper strata and filler lower floor, wherein, filler lower floor be located at filler upper strata lower section, filling out in filler lower floor
Material is using the larger filler in aperture, and the filler on filler upper strata uses the less filler in aperture, and it is soft that filler may be selected from suspension type
One kind in filler, suspension Ball-type packing, half suspension Ball-type packing, polyhedron empty ball filler, or by various different fillers
Combination, forms combined stuffing, by the setting of the filling-material structure, otherwise can prevent that upper filler aperture setting is unreasonable causes stuffing hole
Block, otherwise the excessive effluent quality for causing in filler aperture is poor.Filler upper strata or filler lower floor are by the suspension of correspondence position
The filler that support is fixed and be fixed on suspension holdfast is formed, and suspension holdfast can be formed by connecting by common plastic tube.Cloth
Being provided with for device of air is beneficial to make sewage generation vortex flow, vortex flow to realize being stirred floc sludge or granule sludge
Mixing, keeps suspending, and prevents precipitation, makes sludge that mixing is frequently contacted with sewage, greatly improves treatment effeciency.Complete hydrolysis acidification
Afterwards, sewage carries out oxidation processes into contact-oxidation pool, and most small-molecule substance or dissolved organic matter resolve into water and two at last
Carbonoxide etc..Preliminary sedimentation tank is consistent with the structure of second pond, can use rectangular sedimentation tank, radical sedimentation basin and vertical-flow heavy
Any one in the type of shallow lake pond 3, although structure can be with identical, but effect is differed, and preliminary sedimentation tank is mainly used in
Oil removal and partial organic substances, and the effect of two hypostasis is to realize mud-water separation, and the delivery port of preliminary sedimentation tank and second pond
Triangular-notch weir delivery port can be used, stable water outlet rate is proposed.
Implementation method of the present utility model is explained in detail above in association with accompanying drawing, but the utility model is not limited to be retouched
The implementation method stated.For a person skilled in the art, it is right in the case where the utility model principle and spirit is not departed from
These implementation methods carry out various changes, modification, replacement and modification, still fall within protection domain of the present utility model.
Claims (7)
1. a kind of bio-contact oxidation sewage disposal system, it is characterised in that：Including passing sequentially through the filtering ponds of pipeline connection, adjusting
Section pond, dosing reaction tank, preliminary sedimentation tank, hydrolysis acidification pool, contact-oxidation pool and second pond, the hydrolysis acidification pool, contact oxygen
Change pond and be respectively connected with aerator, the filtering ponds are internally provided with grid, and the regulating reservoir is internally provided with submersible sewage pump, described two
Heavy pond and preliminary sedimentation tank are provided with sludge outlet, and sludge outlet is connected by sludge pump with sludge-tank pipeline, on the filtering ponds
Water inlet is provided with, delivery port is provided with the second pond, the inside of the hydrolysis acidification pool and contact-oxidation pool is under
Supreme to be disposed with sludge outlet, water inlet, distribution device, packing layer and delivery port, the distribution device equably divides
It is distributed in contact-oxidation pool and hydrolysis acidification pool and is connected with outside aerator, in the hydrolysis acidification pool and contact-oxidation pool
Packing layer in filler be selected from suspension type soft-filler, suspension Ball-type packing, half suspension Ball-type packing, polyhedron empty ball and fill out
At least one in material.
2. bio-contact oxidation sewage disposal system according to claim 1, it is characterised in that：The hydrolysis acidification pool
And/or the packing layer in contact-oxidation pool includes filler upper strata and filler lower floor, the aperture of the material of filler lower floor is more than filler
The aperture of the material on upper strata.
3. bio-contact oxidation sewage disposal system according to claim 2, it is characterised in that：Filling out in described filler layer
Material is fixed by suspension holdfast, and the suspension holdfast is respectively arranged at the upper and lower part of contact-oxidation pool, and filler is fixed on
The suspension holdfast in portion forms filler upper strata, and the suspension holdfast that filler is fixed on bottom forms filler lower floor.
4. the bio-contact oxidation sewage disposal system according to any one of claims 1 to 3, it is characterised in that：It is described
Regulating reservoir is internally provided with the dividing plate perpendicular to bottom of pond, and the dividing plate both sides are provided with current boost motor.
5. bio-contact oxidation sewage disposal system according to claim 4, it is characterised in that：In the dosing reaction tank
Portion is provided with agitator, and outside is provided through the dispensing pipeline inside dosing reaction tank, and the dispensing pipeline passes through measuring pump
It is connected with filling pocket pipeline.
6. bio-contact oxidation sewage disposal system according to claim 5, it is characterised in that：The regulating reservoir and dosing
Elevator pump is provided with pipeline between reaction tank.
7. bio-contact oxidation sewage disposal system according to claim 2, it is characterised in that：The water outlet of the second pond
Mouth uses triangular-notch weir delivery port.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621164228.5U CN206266393U (en) | 2016-10-25 | 2016-10-25 | A kind of bio-contact oxidation sewage disposal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621164228.5U CN206266393U (en) | 2016-10-25 | 2016-10-25 | A kind of bio-contact oxidation sewage disposal system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206266393U true CN206266393U (en) | 2017-06-20 |
Family
ID=59038856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621164228.5U Expired - Fee Related CN206266393U (en) | 2016-10-25 | 2016-10-25 | A kind of bio-contact oxidation sewage disposal system |
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| Country | Link |
|---|---|
| CN (1) | CN206266393U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108128981A (en) * | 2018-01-04 | 2018-06-08 | 民政部零研究所 | A kind of funeral parlor sewage treatment equipment |
| CN109879538A (en) * | 2019-03-18 | 2019-06-14 | 浙江双益环保科技发展有限公司 | A kind of high total nitrogen, high salinity antibiotics pharmacy waste water processing method |
| CN115028323A (en) * | 2022-07-08 | 2022-09-09 | 广东家怡生态环境股份有限公司 | High enriched sewage multi-stage treatment equipment |
-
2016
- 2016-10-25 CN CN201621164228.5U patent/CN206266393U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108128981A (en) * | 2018-01-04 | 2018-06-08 | 民政部零研究所 | A kind of funeral parlor sewage treatment equipment |
| CN109879538A (en) * | 2019-03-18 | 2019-06-14 | 浙江双益环保科技发展有限公司 | A kind of high total nitrogen, high salinity antibiotics pharmacy waste water processing method |
| CN115028323A (en) * | 2022-07-08 | 2022-09-09 | 广东家怡生态环境股份有限公司 | High enriched sewage multi-stage treatment equipment |
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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: 20170620 Termination date: 20171025 |
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| CF01 | Termination of patent right due to non-payment of annual fee |