CN205347151U - Integration sewage treatment retrieval and utilization device - Google Patents
Integration sewage treatment retrieval and utilization device Download PDFInfo
- Publication number
- CN205347151U CN205347151U CN201620072724.1U CN201620072724U CN205347151U CN 205347151 U CN205347151 U CN 205347151U CN 201620072724 U CN201620072724 U CN 201620072724U CN 205347151 U CN205347151 U CN 205347151U
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- Prior art keywords
- tank
- sewage treatment
- cistern
- water
- collecting
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- Expired - Fee Related
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 62
- 230000010354 integration Effects 0.000 title abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 238000000034 method Methods 0.000 claims abstract description 21
- 238000004062 sedimentation Methods 0.000 claims abstract description 19
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- 238000004064 recycling Methods 0.000 claims description 16
- 238000005273 aeration Methods 0.000 claims description 15
- 239000010802 sludge Substances 0.000 claims description 15
- 238000005842 biochemical reaction Methods 0.000 claims description 9
- 230000005484 gravity Effects 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 5
- 230000001737 promoting effect Effects 0.000 claims description 5
- 238000011001 backwashing Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 230000009189 diving Effects 0.000 claims description 2
- 230000006641 stabilisation Effects 0.000 abstract 1
- 238000011105 stabilization Methods 0.000 abstract 1
- 239000008400 supply water Substances 0.000 abstract 1
- 208000028659 discharge Diseases 0.000 description 8
- 239000000919 ceramic Substances 0.000 description 4
- 238000011049 filling Methods 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 230000018109 developmental process Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000029087 digestion Effects 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 210000005056 cell body Anatomy 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000000247 postprecipitation Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model provides an integration sewage treatment retrieval and utilization device, set up just zonulae occludens's catch basin, biological reaction pond, sedimentation tank, bological aerated filter and cistern including arranging in proper order, advance water piping connection and in catch basin department, supply water piping connection in cistern, sewage is equipped with the elevator pump from the inlet tube entering catch basin that flows automatically, catch basin bottom, and sewage promotes the back through the elevator pump and realizes flowing automatically, gets into biological reaction pond, sedimentation tank, bological aerated filter in proper order and is handled, reaches the reuse water standard after being handled, and the quilt is collected the entering cistern, establishes the working shaft promotion after the delivery pipe supplies directly to use to the user in utilizing the cistern. The utility model relates to a this kind of integrative sewage treatment device, the integrated zero clearance of five units combines the design, adopts tertiary sewage treatment technique, goes out water stabilization of water quality, and water quality standard is higher, satisfies sewage treatment completely as the requirement of using mixedly water quality of water.
Description
Technical field
This utility model relates to a kind of integrated sewage treatment recycling device, belongs to field of mechanical technique.
Background technology
Along with the accelerated development of Chinese society economy, the Regeneration Treatment of sewage utilizes the major technique direction having become China's present stage sewage disposal development.Technique is all complex, Chang Neige workshop section monomer is a lot of for current down-stream process and the process of regeneration treatment plant.And this type of technique and technology path are because of monomer too much, management requires higher, is not suitable for comparatively small-sized decentralized type sewage processing item.
Domestic current integrated sewage treating apparatus great majority are less based on sewage disposal to discharge standard, sewage disposal and recycling integrated device.Sewage disposal is relatively easy to discharge standard device technique, and waste water treating and reutilizing device is because of higher to water quality requirement, needs to arrange reuse pool and recycle-water equipment simultaneously and causes the drawbacks such as integrated level is not high, floor space big, monomer dispersion, complex management.After ultimately causing China's small-sized decentralized type sewage processing item sewage disposal, regeneration Popularization And Development is slow.
Utility model content
This utility model provides a kind of integrated sewage treating apparatus, and integrated level is high, it is achieved the seamless link of each workshop section of waste water treating and reutilizing so that the integral structure of device is compact, volume reduces, operation runs simple.Meanwhile, adopting three grades of sewage disposal technologies, stable effluent quality, water standard is higher, fully meets the sewage disposal requirement as miscellaneous water water quality.
Main technique technical scheme of the present utility model is: integrated sewage treatment recycling device includes being arranged in order setting and close-connected collecting-tank, biological reaction pool, sedimentation tank, BAF and cistern, water inlet pipe is connected to collecting-tank place, and feed pipe is connected to cistern；Sewage flows into collecting-tank certainly from water inlet pipe, elevator pump it is provided with bottom collecting-tank, the boosted pump of sewage realizes gravity flow after promoting, sequentially enter biological reaction pool, sedimentation tank, BAF be processed, recycle water standard is reached after processed, it is collected into cistern, utilizes to set in cistern after feed pump promotes and be supplied to user through feed pipe and directly use；Former stain disease is by flowing automatically or being lifted into integrated apparatus collecting-tank unit, the adjustment of water quality and the water yield is mainly completed at collecting-tank unit, meet the small-sized centralized sewage discharge water yield and the bigger objective condition of change of water quality so that sewage-treatment plant stable operation.Collecting-tank is as the anaerobic treatment workshop section of package unit simultaneously, rear end clarifier sludge is back to collecting-tank and carries out denitrification denitrogenation process and the dephosphorization of sewage, and excess sludge can discharge to be transported outward after arranging anaerobic tank Anaerobic Digestion nearby or arranging sludge dewatering facility processed voluntarily.This device only arranges one-level lifting water pump at collecting-tank and carries out the lifting of sewage, and follow-up workshop section all realizes flow by gravity, decreases the lifting of sewage to the full extent, saves and promotes power consumption and operating cost.
This integrated sewage treating apparatus that this utility model relates to, collecting-tank, biological reaction pool, sedimentation tank, BAF, five unit of cistern integrated gapless combine design；In processing procedure, sludge pump sludge reflux is to front end collecting-tank, enters anaerobic tank or transport outward by oneself outside excess sludge, and BAF backwashing water, from flowing into front end collecting-tank circular treatment, is arranged without outside waste water.
Accompanying drawing explanation
Fig. 1 is this utility model one integrated sewage treatment recycling device site plan；
Fig. 2 is this utility model one integrated sewage treatment recycling device upward view；
In figure, labelling is as follows: 1 collecting-tank, 2 biological reaction pools, 3 sedimentation tanks, 4 BAFs, 5 cisterns, 6 water inlet pipes, 7 feed pipes, 8 elevator pumps, 9 sludge pumps, 10 backwash pumps, 11 feed pumps, 12 filter tank Aeration fans, 13 filter tank recoil blower fans, 14 Aeration fans, 15 biological ropes, 16 ceramic aggregate biological filtrates.
Detailed description of the invention
As Figure 1-Figure 2, integrated sewage treatment recycling device includes being arranged in order setting and close-connected collecting-tank 1, biological reaction pool 2, sedimentation tank 3, BAF 4 and cistern 5, and water inlet pipe 6 is connected to collecting-tank place, and feed pipe 7 is connected to cistern；Sewage flows into collecting-tank certainly from water inlet pipe 6, it is provided with elevator pump bottom collecting-tank 1, the boosted pump of sewage realizes gravity flow after promoting, sequentially enter biological reaction pool 2, sedimentation tank 3, BAF 4 are processed, recycle water standard is reached after processed, it is collected into cistern 5, utilizes to set in cistern 5 after feed pump promotes and be supplied to user through feed pipe and directly use；Former stain disease is by flowing automatically or being lifted into integrated apparatus collecting-tank unit, the adjustment of water quality and the water yield is mainly completed at collecting-tank unit, meet the small-sized centralized sewage discharge water yield and the bigger objective condition of change of water quality so that sewage-treatment plant stable operation.Collecting-tank is as the anaerobic treatment workshop section of package unit simultaneously, rear end clarifier sludge is back to collecting-tank and carries out denitrification denitrogenation process and the dephosphorization of sewage, and excess sludge can discharge to be transported outward after arranging anaerobic tank Anaerobic Digestion nearby or arranging sludge dewatering facility processed voluntarily.This device only arranges one-level lifting water pump at collecting-tank and carries out the lifting of sewage, and follow-up workshop section all realizes flow by gravity, decreases the lifting of sewage to the full extent, saves and promotes power consumption and operating cost.
Being provided with backwash pump 10 bottom cistern 5, in sewage-treatment plant running, backwash pump is used for BAF water backwashing.
Biological rope it is provided with as bio-carrier in biological reaction pool 2.Sewage in collecting-tank 1 enters biochemical reaction tank through promoting in pond after immersible pump promotes, filling biological rope 15 filler in biochemical reaction tank, after filling biological rope, reaction tank volumetric loading is greatly improved so that biochemical reaction tank volume optimization reduces, and device area reduces, reduces cost.
Autocoupling type diving sludge pump 9 is set, for row outside clarifier sludge and collecting-tank backflow in sedimentation tank.
Biohaydite filter material 16 it is provided with as bio-carrier and physical filtering medium in BAF 4；Described Biohaydite filter material is connected with filter tank Aeration fan 14 and filter tank recoil blower fan 13, filter tank Aeration fan 12 supplies aerobic three grades of biochemistry for BAF 4 technique and physical filtering processes, and recoil blower fan 13 in filter tank is for BAF 4 gas backwash.Installing micro porous aeration head blast aeration at the bottom of pond, sewage completes one-level biochemical treatment in biological reaction pool and removes the major pollutants such as most COD, BOD, NH3-N.Sedimentation tank supernatant is from flowing into secondary biochemical treatment and filter station BAF 4, the built-in raising effect ceramic aggregate biological filtrate of BAF 4, ceramic aggregate biological filtrate specific surface area is big, and biological load is high, making BAF 4 actual volume only small, device area reduces, reduces cost.Filter tank adopts combined water and air backwash, timing automatic backwash, it is achieved unattended operation mode.After BAF 4 processes, dirty water pollutant is removed substantially, and filter tank water outlet enters cistern after filter tank bottom porous pipe is collected, and after adding chlorine tablets sterilization in cistern, water quality reaches Treated sewage reusing standard.Install back in cistern and can be supplied to user's use with water pump.
In biological reaction pool, biological rope be connected with Aeration fan, Aeration fan is used for biochemical reaction pool process aeration secondary biochemical treatment.Biological reaction pool water outlet, from flowing into sedimentation tank, is installed large aperture inclined tube, is increased sedimentation effect in sedimentation tank.
Concrete principle of the present utility model is as follows: sewage enters this utility model collecting-tank from water inlet pipe, carries out water quality and quantity adjustment and denitrification denitrogenation and anaerobism dephosphorization processes in collecting-tank.The boosted pump of rear sewage enters biochemical reaction tank after promoting, and biochemical reaction tank filling biological rope filler for fixation of microbe and increases cell body volumetric loading.Carry out in biochemical reaction tank the biochemical treatment of sewage remove that COD, BOD, NH3-N etc. are all kinds of can biochemical pollutant.Biochemical reaction tank mixed liquor, from flowing into post precipitation pond, realizes mixed liquor mud-water separation in precipitation.Supernatant is by feed pipe from flowing into sedimentation tank, and mud is delivered to front end collecting-tank by sludge pump in sedimentation tank and realizes anaerobic denitrifying denitrogenation and the dephosphorization process of sewage.Sedimentation tank water outlet certainly flows into BAF after water leg is collected, filling ceramic aggregate biological filtrate in BAF, further biochemical and physical filtering process is realized so that in sewage, all kinds of pollutant levels such as COD, BOD, NH3-N, SS are substantially reduced even substantially all removal in BAF.After effluent of aeration biological filter is collected by bottom porous pipe, connection enters cistern.BAF backwash pump is installed in cistern and runs water backwashing after some time for BAF, install in cistern and be delivered to each user through feed pipe after water is promoted by feed pump and use.
BAF backwash water source, from cistern, does not utilize other water source, and after backwash simultaneously, draining gravity flow enters front end collecting-tank, and the overall operation stage is without any discharge of wastewater, it is achieved the zero discharge treatment reuse of sewage.Realize the recycling of sewage to the full extent, realize and the basic goal of energy-conserving and environment-protective, saving water resource simultaneously.This integrated sewage treatment recycling device that this utility model relates to.
Detailed description of the invention described in the utility model is not intended that the restriction to the application scope; within every spirit in this utility model design and principle, any amendment that one of skill in the art can make, equivalent replacement and improvement etc. should be included within protection domain of the present utility model.
Claims (7)
1. an integrated sewage treatment recycling device, it is characterised in that: including being arranged in order setting and close-connected collecting-tank, biological reaction pool, sedimentation tank, BAF and cistern, water inlet pipe is connected to collecting-tank place, and feed pipe is connected to cistern；Sewage flows into collecting-tank certainly from water inlet pipe, elevator pump it is provided with bottom collecting-tank, the boosted pump of sewage realizes gravity flow after promoting, sequentially enter biological reaction pool, sedimentation tank, BAF be processed, recycle water standard is reached after processed, it is collected into cistern, utilizes to set in cistern after feed pump promotes and be supplied to user through feed pipe and directly use.
2. a kind of integrated sewage treatment recycling device according to claim 1, it is characterised in that: described columns base is provided with backwash pump, and in sewage-treatment plant running, backwash pump is used for BAF water backwashing.
3. a kind of integrated sewage treatment recycling device according to claim 1, it is characterised in that: it is provided with biological rope in described biological reaction pool as bio-carrier.
4. a kind of integrated sewage treatment recycling device according to claim 1, it is characterised in that: set autocoupling type diving sludge pump in described sedimentation tank, for row outside clarifier sludge and collecting-tank backflow.
5. a kind of integrated sewage treatment recycling device according to claim 1, it is characterised in that: it is provided with Biohaydite filter material in described BAF as bio-carrier and physical filtering medium.
6. a kind of integrated sewage treatment recycling device according to claim 5, it is characterized in that: described Biohaydite filter material is connected with filter tank Aeration fan and filter tank recoil blower fan, filter tank Aeration fan supplies aerobic three grades of biochemistry for biological aerated filter process and physical filtering processes, and filter tank recoil blower fan is for BAF gas backwash.
7. a kind of integrated sewage treatment recycling device according to claim 3, it is characterised in that: in described biological reaction pool, biological rope be connected with Aeration fan, described Aeration fan is used for biochemical reaction pool process aeration secondary biochemical treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620072724.1U CN205347151U (en) | 2016-01-26 | 2016-01-26 | Integration sewage treatment retrieval and utilization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620072724.1U CN205347151U (en) | 2016-01-26 | 2016-01-26 | Integration sewage treatment retrieval and utilization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205347151U true CN205347151U (en) | 2016-06-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620072724.1U Expired - Fee Related CN205347151U (en) | 2016-01-26 | 2016-01-26 | Integration sewage treatment retrieval and utilization device |
Country Status (1)
| Country | Link |
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| CN (1) | CN205347151U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105481201A (en) * | 2016-01-26 | 2016-04-13 | 甘肃金桥水科技（集团）股份有限公司 | Integrated sewage treatment and reuse device |
| WO2020026275A3 (en) * | 2018-07-31 | 2020-04-30 | Goudarzi Reza | Automatic backwash filter |
-
2016
- 2016-01-26 CN CN201620072724.1U patent/CN205347151U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105481201A (en) * | 2016-01-26 | 2016-04-13 | 甘肃金桥水科技（集团）股份有限公司 | Integrated sewage treatment and reuse device |
| WO2020026275A3 (en) * | 2018-07-31 | 2020-04-30 | Goudarzi Reza | Automatic backwash filter |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 730000 No. 279, Jiuquan Road, Chengguan District, Gansu, Lanzhou Patentee after: Gansu Jinqiao water technology (Group) Co., Ltd. Address before: 730000 No. 279, Jiuquan Road, Chengguan District, Gansu, Lanzhou Patentee before: Gansu Jinqiao water science and Technology (Group) Limited by Share Ltd |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160629 Termination date: 20200126 |