CN205556380U - Integral type sewage treatment unit - Google Patents
Integral type sewage treatment unit Download PDFInfo
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- CN205556380U CN205556380U CN201620099143.7U CN201620099143U CN205556380U CN 205556380 U CN205556380 U CN 205556380U CN 201620099143 U CN201620099143 U CN 201620099143U CN 205556380 U CN205556380 U CN 205556380U
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Abstract
The utility model belongs to the technical field of sewage treatment unit, a integral type sewage treatment unit is related to, being equipped with the grid on the inlet channel, the inlet channel is connected with the aeration grit chamber, and the aeration grit chamber is distinguished with the moving bed biofilm reactor anaerobism and is linked to each other, moving bed biofilm reactor includes anaerobism district, the anoxic zone oxygen district that becomes reconciled, and between anaerobism district and the anoxic zone, all be equipped with the logical mouth of a river between anoxic zone and the good oxygen district, good oxygen district is connected with aeration equipment, and the anaerobism is distinguished and good oxygen is equipped with interior circulation pipeline between distinguishing, oxygen district's intussuseption that the anaerobism is distinguished, become reconciled in the anoxic zone is filled with carrier of microorganism and packs, the good oxygen of moving bed biofilm reactor district is connected with denitrification biological activity filtering pond, and denitrification biological activity filtering pond is connected with the pond of disinfecting, be applicable to distributed treatment of domestic sewage places such as remote villages and small towns, can efficient handling of domestic sewage, go out hydroenergy and enough directly enter among the natural environment, solve traditional wastewater treatment process and controlled shortcomings such as complicated, with high costs.
Description
Technical field
The utility model belongs to sewage treatment unit technical field, specifically, relates to a kind of integral type sanitary sewage disposal
Device.
Background technology
According to " " 12 " whole nation urban wastewater treatment and the planning of regeneration Facilities Construction ", by the end of the year 2010, China city
Town sanitary sewage facility disposal ability has reached 1.25 billion cubic meters/day, " 12 " period, the cities and towns in the planned range of the whole nation
Newly-increased sewage disposal scale 4569 ten thousand steres/day.And along with the appearance of country's " water prevention and cure of pollution action plan ", water security
Have gone up as national strategy, the important step that sewage disposal recycles as water body environment protection and water resource, need efficiently,
Environmental protection, economic treatment technology and equipment.
Integral type sewage processing system is the important component part that domestic sewage factory focuses on pattern on a large scale, it is adaptable to villages and small towns,
The diversifications of markets such as foreign-going ship sewage disposal, and the existing usual treatment effeciency of integral type processing system is relatively low, run control complicated,
Financial cost is too high.
Utility model content
The purpose of this utility model is the shortcoming overcoming prior art to exist, and seeks to design a kind of one being applicable to remote countryside
Formula sewage treatment unit, improves the treatment effeciency of dispersed wastewater, reduces the cost of rural sewage treatment, simplifies sewage
Process technique.
To achieve these goals, the technical solution adopted in the utility model is:
A kind of integral type sewage treatment unit, including inlet channel, aerated grit chamber, MBBR, anti-nitre
Changing bioactivity filter, sterilization pool, described inlet channel is provided with grid, and inlet channel is connected with aerated grit chamber water inlet, aeration
The delivery port of setting pot is connected with the water inlet of MBBR anaerobic zone；Described MBBR includes
Anaerobic zone, anoxic zone and aerobic zone, anaerobic zone and anoxic zone wall altogether, it was provided with the mouth of a river, anoxic zone between anaerobic zone and anoxic zone
With aerobic zone wall altogether, being provided with outlet pass between anoxic zone and aerobic zone, described aerobic zone is connected with aerator, and anaerobic zone is with good
Oxygen is provided with inner loop pipeline between district；Described anaerobic zone and anoxic zone are filled with hard polyaminoester microbe carrier stuffing, described good
Soft polyurethane ester microbe carrier stuffing it is filled with in oxygen district；The delivery port of MBBR aerobic zone is raw with denitrification
The water inlet in thing activity filter tank connects, and the delivery port of denitrification bioactivity filter is connected with sterilization pool water inlet；Described sterilization pool
It is provided with online chemicals dosing plant.
Preferably, the grizzly bar gap of described grid is 0.5-5cm, enters, at sewage, remove before aerated grit chamber in sewage miscellaneous
Thing.
Preferably, between described anaerobic zone and aerobic zone, internal reflux ratio is 100%；
Preferably, in described denitrification activity filter tank, filter medium is particulate bioactive charcoal or polymer filtrate, under employing
Run to stream mode；
Integral type sewage treatment unit of the present utility model, sewage, after grid, first passes through aerated grit chamber, by drum
Blower fan aeration, phase mutual friction bear the shearing force of aeration between sand grains, the organic matter removal that will adhere on sand grains, the grains of sand are at eddy flow
Centrifugal action is lowered into the husky sand launder of collection；Meanwhile, the dissolved oxygen that aeration provides is also beneficial to partial organic substances and removes.
Then sewage passes through MBBR, and a large amount of microbe carrier of this area filling, carrier has higher ratio table
Area and bioaffinity, provide good apposition growth and the environment of propagation for sewage disposal microorganism, thus increase biomass,
Improve sewage treating efficiency.Compared with traditional activated sludge process, MBBR (MBBR) sewage treatment load
Height, excess sludge generation amount is few, it is adaptable to dispersant type domestic wastewater processes.Add specified microorganisms microbial inoculum, such as: denitrifying bacterium,
Nitrifier etc., on microbe carrier stuffing cultivate be suitable to strengthen sanitary sewage disposal microorganism species, utilize carrier filler and
The synergy of microbial bacterial agent, improves wastewater treatment efficiency further.
Sewage, through denitrification bioactivity filter, uses upward flow mode to run, and filtrate provides anaerobism for sewage disposal microorganism
Living environment, beneficially denitrifying bacterium growth and breeding, thus strengthened denitrification effect further.
Last sewage flows through sterile zones, carries out by disinfection by ultraviolet light or by the way of adding sodium hypochlorite online, and water outlet reaches standard
Can discharge.
The beneficial effects of the utility model are: be applicable to the distributing sanitary sewage disposal places such as remote villages and small towns, it is possible to efficiently process
Sanitary sewage, water outlet can be directly discharged in natural environment；Solve traditional waste water treatment process control complexity, high in cost of production lacks
Point
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model；
As shown in Figure 1: inlet channel 1, grid 2, aerated grit chamber 3, MBBR 4, denitrification biology are lived
Property filter tank 5, sterilization pool 6, inner loop pipeline 7, aerator 8.
Detailed description of the invention
Combine accompanying drawing below by specific embodiment the utility model is further described:
Embodiment 1
The integral type sewage treatment unit of the present embodiment, including inlet channel 1, aerated grit chamber 3, moving bed biological film reaction
Device 4, denitrification bioactivity filter 5, sterilization pool 6, described inlet channel 1 is provided with grid 2, inlet channel 1 and sediment by aeration
Pond 3 water inlet connects, and the delivery port of aerated grit chamber 3 is connected with the water inlet of MBBR 4 anaerobic zone；Institute
Stating MBBR 4 and include anaerobic zone, anoxic zone and aerobic zone, anaerobic zone and anoxic zone wall altogether, anaerobic zone is with scarce
It is provided with the mouth of a river, anoxic zone and aerobic zone wall altogether between oxygen district, between anoxic zone and aerobic zone, is provided with outlet pass, described aerobic zone
It is connected with aerator 8, between anaerobic zone and aerobic zone, is provided with inner loop pipeline 7；Described anaerobic zone and anoxic zone are filled with firmly
Matter polyurethane microbe carrier stuffing, is filled with soft polyurethane ester microbe carrier stuffing in aerobic zone；Moving bed biological film reaction
The delivery port of device 4 aerobic zone is connected with the water inlet of denitrification bioactivity filter 5, the water outlet of denitrification bioactivity filter 5
Mouth is connected with sterilization pool 6 water inlet；The grizzly bar gap of grid 2 is 0.5cm, removes dirt before sewage enters aerated grit chamber 3
Foreign material in water；Between anaerobic zone and aerobic zone, internal reflux ratio is 100%；In denitrification activity filter tank 5, filter medium is graininess
Biological activated carbon, runs to stream mode under employing；Sterilization pool 6 is provided with online chemicals dosing plant.
Embodiment 2
The integral type sewage treatment unit of the present embodiment, divided by lower difference outside, the other the same as in Example 1:
The grizzly bar gap of grid 2 is 5cm, removes the foreign material in sewage before sewage enters aerated grit chamber 3.
Claims (2)
1. integral type sewage treatment unit, it is characterised in that: include that inlet channel, aerated grit chamber, moving-bed biofilm are anti-
Answering device, denitrification bioactivity filter, sterilization pool, described inlet channel is provided with grid, inlet channel and aerated grit chamber water inlet
Connecting, the delivery port of aerated grit chamber is connected with the water inlet of MBBR anaerobic zone；Described moving-bed biofilm
Reactor includes anaerobic zone, anoxic zone and aerobic zone, anaerobic zone and anoxic zone wall altogether, is provided with water between anaerobic zone and anoxic zone
Mouthful, anoxic zone and aerobic zone wall altogether, it is provided with outlet pass between anoxic zone and aerobic zone, described aerobic zone is connected with aerator,
Inner loop pipeline it is provided with between anaerobic zone and aerobic zone；Described anaerobic zone and anoxic zone are filled with hard polyaminoester microbe carrier and fill out
Material, is filled with soft polyurethane ester microbe carrier stuffing in described aerobic zone；The delivery port of MBBR aerobic zone
Being connected with the water inlet of denitrification bioactivity filter, the delivery port of denitrification bioactivity filter is connected with sterilization pool water inlet,
Described sterilization pool is provided with online chemicals dosing plant.
Integral type sewage treatment unit the most according to claim 1, it is characterised in that: the grizzly bar gap of described grid
For 0.5-5cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620099143.7U CN205556380U (en) | 2016-01-31 | 2016-01-31 | Integral type sewage treatment unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620099143.7U CN205556380U (en) | 2016-01-31 | 2016-01-31 | Integral type sewage treatment unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205556380U true CN205556380U (en) | 2016-09-07 |
Family
ID=56820524
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620099143.7U Active CN205556380U (en) | 2016-01-31 | 2016-01-31 | Integral type sewage treatment unit |
Country Status (1)
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| CN (1) | CN205556380U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106830320A (en) * | 2017-02-27 | 2017-06-13 | 兰州理工大学 | A kind of method of integrated form biological bed and treatment rural scattered domestic sewage |
| CN109650652A (en) * | 2018-12-24 | 2019-04-19 | 浙江中昌水处理科技有限公司 | Biochemistry pool MBBR technique coupling denitrification deep-bed filter denitrification dephosphorization system and method |
| CN110655283A (en) * | 2019-11-12 | 2020-01-07 | 甘肃昊宇环保科技有限公司 | Novel rural domestic sewage treatment system of combination formula membrane reactor |
| CN110845073A (en) * | 2019-10-23 | 2020-02-28 | 常飞 | Method for treating rural domestic sewage through activated sludge |
| CN110902948A (en) * | 2019-11-29 | 2020-03-24 | 北京林业大学 | Rural distributed domestic sewage treatment process and system for strengthening phosphorus removal and recovery |
-
2016
- 2016-01-31 CN CN201620099143.7U patent/CN205556380U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106830320A (en) * | 2017-02-27 | 2017-06-13 | 兰州理工大学 | A kind of method of integrated form biological bed and treatment rural scattered domestic sewage |
| CN109650652A (en) * | 2018-12-24 | 2019-04-19 | 浙江中昌水处理科技有限公司 | Biochemistry pool MBBR technique coupling denitrification deep-bed filter denitrification dephosphorization system and method |
| CN110845073A (en) * | 2019-10-23 | 2020-02-28 | 常飞 | Method for treating rural domestic sewage through activated sludge |
| CN110655283A (en) * | 2019-11-12 | 2020-01-07 | 甘肃昊宇环保科技有限公司 | Novel rural domestic sewage treatment system of combination formula membrane reactor |
| CN110902948A (en) * | 2019-11-29 | 2020-03-24 | 北京林业大学 | Rural distributed domestic sewage treatment process and system for strengthening phosphorus removal and recovery |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20191108 Address after: 266000 Shandong province Qingdao City Taiping Road, No. 55 Patentee after: Qingdao Water Group Co., Ltd Address before: 266000 Shandong province Qingdao City, Harbin Road No. 61 Patentee before: SCIENCE AND TECHNOLOGY CENTER, QINGDAO WATER GROUP CO., LTD. |
|
| TR01 | Transfer of patent right |