CN209210593U - A kind of town sewage treatment system - Google Patents
A kind of town sewage treatment system Download PDFInfo
- Publication number
- CN209210593U CN209210593U CN201822052829.2U CN201822052829U CN209210593U CN 209210593 U CN209210593 U CN 209210593U CN 201822052829 U CN201822052829 U CN 201822052829U CN 209210593 U CN209210593 U CN 209210593U
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- Prior art keywords
- tank
- pond
- town sewage
- sewage treatment
- treatment system
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 239000010865 sewage Substances 0.000 title claims abstract description 43
- 239000010802 sludge Substances 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 10
- 230000001954 sterilising Effects 0.000 claims abstract description 7
- 238000001914 filtration Methods 0.000 claims abstract description 6
- 238000007599 discharging Methods 0.000 claims abstract description 5
- 230000000694 effects Effects 0.000 claims abstract description 4
- 239000006004 Quartz sand Substances 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 9
- 241000216843 Ursus arctos horribilis Species 0.000 claims description 5
- 238000004062 sedimentation Methods 0.000 claims description 5
- 239000000706 filtrate Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 239000002957 persistent organic pollutant Substances 0.000 claims description 3
- 239000004576 sand Substances 0.000 claims description 3
- 238000007790 scraping Methods 0.000 claims description 3
- 239000002356 single layer Substances 0.000 claims description 3
- 239000000047 product Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 8
- 238000004065 wastewater treatment Methods 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 4
- 239000003344 environmental pollutant Substances 0.000 abstract description 3
- 231100000719 pollutant Toxicity 0.000 abstract description 3
- OSVXSBDYLRYLIG-UHFFFAOYSA-N Chlorine dioxide Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 6
- 239000004155 Chlorine dioxide Substances 0.000 description 3
- 235000019398 chlorine dioxide Nutrition 0.000 description 3
- 230000000249 desinfective Effects 0.000 description 3
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound [N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 239000003818 cinder Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000010954 inorganic particle Substances 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N Iron(III) oxide Chemical compound O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- -1 and treated Substances 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 235000012970 cakes Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910000460 iron oxide Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 210000000056 organs Anatomy 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000001376 precipitating Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Abstract
The utility model discloses a kind of town sewage treatment systems, belong to technical field of sewage.The system includes sequentially connected grid, setting pot, anaerobic pond, anoxic pond, aerobic tank, secondary settling tank, filtering ponds and sterilization pool, and the aerobic tank is connected with the anoxic pond, and the mud discharging mouth of the secondary settling tank is connect with the anaerobic pond；The mud discharging mouth of the secondary settling tank is connect with sludge concentration tank, and the sludge concentration tank is connect with sludge dewatering equipment and the setting pot respectively, and the sludge dewatering equipment is connect with the setting pot.The process town sewage that the utility model uses materialization+biochemistry+materialization to combine, have the advantages that rational technology, treatment effect are stable, water outlet can reach " urban wastewater treatment firm pollutant emission standard " (GB18918-2002) level-one A standard.
Description
Technical field
The utility model belongs to technical field of sewage, more specifically to a kind of town sewage treatment system.
Background technique
With the development of economy with the growth of population, ur- banization speed constantly accelerates, and consequent is town sewage
Constantly discharge and its processing problem.To solve to alleviate the pressure of environment, the processing problem of town sewage is must in urbanization process
One of need face and solve the problems, such as.
Town sewage includes town dweller's sanitary sewage, organ, school, hospital, commerce services mechanism and various public is set
Draining is applied, and industrial wastewater and initial rainwater for allowing to be discharged into town sewage collection system etc., has the following characteristics that (1) people
Mouth is few, and water supply standard is lower, sewage treatment small scale；(2) industrial structure region particular differences, influenced and water consumption by rainy season
Hourly variation factor is larger, therefore sewage water, change of water quality are big；(3) level of economic development is relatively low, and ability to shoulder economically is weak, can
Selective applicable technology is few；(4) cause expense for construction and operating cost excessively high since treatment scale is small；(5) maintenance pipe
Manage technical staff and operational management experience there is a serious shortage of.Currently, China there is no, for Sewage Treatment Project, (treatment scale is small
In 20,000 ton per days, focus mostly in 2000~5000 ton per days) adaptable treatment process.
Publication date is that the Chinese patent 201210302700.7 on November 14th, 2012 discloses a kind of urban wastewater treatment
System and method, the system include being sequentially connected logical grid sewage-treatment plant, setting pot, anoxic pond, MBR aerobic tank, interior
The adsorption filter and sterilization pool of compound adsorbent of the portion filled with nano hydrated ferric oxide, wherein the aerobic bottom of pond portion of MBR is equipped with
For the sludge outlet of sludge to be discharged, the corresponding processing method of the processing system includes being suspended with the removal of grid sewage-treatment plant
Object is handled, with setting pot precipitating inorganic particle, denitrification denitrogenation processing, with MBR membrane module deep purifying with nano hydrated oxidation
Iron adsorbent carries out dephosphorization processing and carries out disinfection processing to the processing water Jing Guo above-mentioned steps, wherein MBR membrane module depth
The partial sludge of purified treatment is back in denitrification denitrogenation processing.Greatest problem existing for the technology is to need to contain using technology
Higher inorganic agent is measured, application and maintenance there are higher technical requirements, be not suitable for the processing of town sewage.
Summary of the invention
Goal of the invention: in view of the above-mentioned problems existing in the prior art, the purpose of this utility model is to provide a kind of cities and towns
Sewage disposal system.
Technical solution: to solve the above-mentioned problems, technical solution used by the utility model is as follows:
A kind of town sewage treatment system, including sequentially connected grid, setting pot, biological processing unit, secondary settling tank, mistake
Filter tank and sterilization pool, the biological processing unit are used to remove most organic pollutants using biochemical treatment, and described two is heavy
The mud discharging mouth in pond is connect with sludge concentration tank, and the sludge concentration tank connects with sludge dewatering equipment and the setting pot respectively
It connects, the sludge dewatering equipment is connect with the setting pot.
The main body biological processing unit includes sequentially connected anaerobic pond, anoxic pond and aerobic tank, the aerobic tank with
The anoxic pond is connected, and the mud discharging mouth of the secondary settling tank is connected with the anaerobic pond.
The filtering ponds are V-type filter tank, and the V-type filter tank uses micro- resistance water distribution system, and filtrate is that single layer quartz sand is equal
Matter filtrate, 1.2 meters of quartz sand thickness, the effective grain size of quartz sand is 0.90~1.20mm.
The grid includes coarse rack and fine fack, and the grizzly bar gap of the coarse rack is 30mm, the grid of the fine fack
Interspace is 8mm.
The setting pot is aerated grit chamber.
The secondary settling tank is radical sedimentation basin, and scraping and sucking machine is arranged in pond.
Anaerobic pond, anoxic pond, the volumetric ratio of aerobic tank are 1:1:3.
The utility model has the advantages that compared with the prior art, the utility model uses materialization+biochemistry (anaerobe-oxygen deficient+aerobic)+materialization
The process combined, handles town sewage, and treated, and sewage meets " urban wastewater treatment firm pollutant emission
Standard " (GB18918-2002) level-one A standard requirement, processing and maintenance process are easy, high treating effect, and device operation can
It leans on, economical rationality.The town sewage treatment system of the utility model has not only widened the Processing tecchnics of this kind of sewage, but also right
The improvement of other trade effluents also has certain reference value.
Detailed description of the invention
Fig. 1 is the process for town sewage treatment flow diagram of the utility model.
Specific embodiment
The utility model is further described below combined with specific embodiments below.
Embodiment
A kind of urban wastewater treatment device, including grid, setting pot, anaerobic pond, anoxic pond, aerobic tank, secondary settling tank, V-type
Filter tank, sterilization pool, sludge concentration tank, sludge dewatering equipment；As shown in Figure 1, town sewage passes sequentially through grid, setting pot, anaerobism
Pond, anoxic pond, aerobic tank, secondary settling tank, V-type filter tank and sterilization pool；Aerobic tank is connected with anoxic pond；Secondary settling tank and anaerobic pond phase
Even；Secondary settling tank is also connected with sludge concentration tank；Sludge concentration tank is connected with setting pot；Sludge concentration tank also with sludge dewatering equipment phase
Even, sludge dewatering equipment is connect with setting pot.
Wherein:
Grid is twice grid, coarse rack and fine fack, and the grizzly bar gap of coarse rack is 30mm, the grizzly bar gap of fine fack
For 8mm, the scarfing cinder mode of grid is mechanical scarfing cinder；Inlet pumping station is arranged in coarse rack and fine fack.
Setting pot is aerated grit chamber, is aerated using boring aeration pipe, main purpose be in order to remove specific gravity compared with
Big inorganic particle.
Aerobic tank uses SBR activated sludge process, and anaerobic pond, anoxic pond, the volumetric ratio of aerobic tank are 1:1:3.
Secondary settling tank is radical sedimentation basin, and scraping and sucking machine is arranged in pond；
V-type filter tank use micro- resistance water distribution system, filtrate be single layer quartz sand homogeneous filtering material, 1.2 meters of quartz sand thickness, stone
The effective grain size of sand is 0.90~1.20mm, and the backwashing manner combined with surface sweep washing is backwashed using three step of air water.
Chlorine dioxide generator is equipped in sterilization pool, chlorine dioxide generator is placed in chlorination house.
Sludge dewatering equipment is belt filter press.
Certain town sewage, water 8000m are handled using above-mentioned apparatus3/ d, including following steps as shown in Figure 1:
Step 1, aerated grit chamber is passed through after town sewage being removed floating material and suspended matter by grid；
Step 2, sewage removes most inorganic grit by aerated grit chamber；
Step 3, setting pot water outlet passes sequentially through anaerobic pond, anoxic pond and aerobic tank to remove most organic pollutants
(including ammonia nitrogen, total phosphorus etc.), 1/3 effluent recycling of aerobic tank to anoxic pond (i.e. nitrification liquid reflux) is to remove ammonia nitrogen, remaining water outlet
Into Radial Flow Secondary Sedimentation Tank, hydraulic detention time of the sewage in anaerobic pond is 1.5h, and the residence time in anoxic pond is
1.5h, the residence time in aerobic tank are 4.5h；
Step 4, sewage further removes oil removal in Radial Flow Secondary Sedimentation Tank, and the partial sludge of secondary settling tank is back to anaerobism
Pond is to guarantee the amount of useful microorganism, return sludge ratio 1:3；
It step 5, is the treatment effect for further increasing sewage, secondary clarifier effluent enters V-type filter tank, passes through the mistake of quartz sand
The further purification sewage of filter, sewage carries out disinfection pond later, is discharged after being carried out disinfection using chlorine dioxide；
Step 6, the excess sludge of secondary settling tank is discharged into sludge concentration tank and carries out gravity concentration, and gained supernatant is back to sand setting
Pond；Sludge after concentration enters sludge dewatering equipment and is dehydrated, and gained percolate is back to setting pot, is dehydrated outside gained mud cake
Fortune.
The correlation water index of sewage is shown in Table 1 after treatment, illustrates final outflow water water quality better than " urban wastewater treatment firm
Pollutant emission standard " (GB18918-2002) level-one A standard requirement.
The water quality indicator of the sewage before and after the processing of table 1
Claims (7)
1. a kind of town sewage treatment system, which is characterized in that including sequentially connected grid, setting pot, biological processing unit,
Secondary settling tank, filtering ponds and sterilization pool, the biological processing unit are used to remove most organic pollutants using biochemical treatment,
The mud discharging mouth of the secondary settling tank is connect with sludge concentration tank, the sludge concentration tank respectively with sludge dewatering equipment and described heavy
The connection of sand pond, the sludge dewatering equipment are connect with the setting pot.
2. town sewage treatment system according to claim 1, which is characterized in that the main body biological processing unit includes
Sequentially connected anaerobic pond, anoxic pond and aerobic tank, the aerobic tank are connected with the anoxic pond, the sludge row of the secondary settling tank
Mouth is put to be connected with the anaerobic pond.
3. town sewage treatment system according to claim 1, which is characterized in that the filtering ponds are V-type filter tank, described
V-type filter tank uses micro- resistance water distribution system, and filtrate is single layer quartz sand homogeneous filtering material, and 1.2 meters of quartz sand thickness, quartz sand has
Effect partial size is 0.90~1.20mm.
4. town sewage treatment system according to claim 1, which is characterized in that the grid includes coarse rack and thin lattice
Grid, the grizzly bar gap of the coarse rack are 30mm, and the grizzly bar gap of the fine fack is 8mm.
5. town sewage treatment system according to claim 1, which is characterized in that the setting pot is aerated grit chamber.
6. town sewage treatment system according to claim 1, which is characterized in that the secondary settling tank is radial-flow type sedimentation
Scraping and sucking machine is arranged in pond in pond.
7. town sewage treatment system according to claim 1, which is characterized in that anaerobic pond, anoxic pond, the appearance of aerobic tank
Product is than being 1:1:3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822052829.2U CN209210593U (en) | 2018-12-07 | 2018-12-07 | A kind of town sewage treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822052829.2U CN209210593U (en) | 2018-12-07 | 2018-12-07 | A kind of town sewage treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209210593U true CN209210593U (en) | 2019-08-06 |
Family
ID=67463453
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822052829.2U Expired - Fee Related CN209210593U (en) | 2018-12-07 | 2018-12-07 | A kind of town sewage treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209210593U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109368941A (en) * | 2018-12-07 | 2019-02-22 | 江苏开放大学（江苏城市职业学院） | A kind of urban wastewater treatment device and its application |
| CN111039505A (en) * | 2019-12-25 | 2020-04-21 | 水净缘环境科技股份有限公司 | Sewage treatment process and system using air source as power |
| CN115286176A (en) * | 2022-07-22 | 2022-11-04 | 安徽润岳科技有限责任公司 | Wastewater treatment process and device for wastewater station |
-
2018
- 2018-12-07 CN CN201822052829.2U patent/CN209210593U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109368941A (en) * | 2018-12-07 | 2019-02-22 | 江苏开放大学（江苏城市职业学院） | A kind of urban wastewater treatment device and its application |
| CN111039505A (en) * | 2019-12-25 | 2020-04-21 | 水净缘环境科技股份有限公司 | Sewage treatment process and system using air source as power |
| CN115286176A (en) * | 2022-07-22 | 2022-11-04 | 安徽润岳科技有限责任公司 | Wastewater treatment process and device for wastewater station |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190806 Termination date: 20211207 |