CN216273646U - New forms of energy villages and small towns sewage treatment system - Google Patents
New forms of energy villages and small towns sewage treatment system Download PDFInfo
- Publication number
- CN216273646U CN216273646U CN202123112027.4U CN202123112027U CN216273646U CN 216273646 U CN216273646 U CN 216273646U CN 202123112027 U CN202123112027 U CN 202123112027U CN 216273646 U CN216273646 U CN 216273646U
- Authority
- CN
- China
- Prior art keywords
- tank
- sludge
- grit chamber
- membrane
- advection
- Prior art date
- 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.)
- Active
Links
Images
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model provides a new energy village and town sewage treatment system which mainly comprises a collecting tank, an adjusting tank, an advection grit chamber, an anaerobic tank, an anoxic tank, an aerobic tank, a membrane tank, a clean water tank and a metering tank, wherein sewage flows in sequence, a thick grid channel is arranged in the collecting tank, a thin grid channel is arranged at the front end of the advection grit chamber, a membrane grid channel is arranged at the rear end of the advection grit chamber, the bottom of the advection grit chamber is butted with a separator, a sludge pump is further arranged for pumping sludge from the aerobic tank and the membrane tank to a sludge dewatering machine for dewatering, the sludge discharged by the sludge dewatering machine enters the sludge tank, the upper parts of the collecting tank and the sludge tank are sealed by a cover and are provided with air entraining pipes, and the air entraining pipes are connected with an ion deodorization machine through a fan. The utility model adaptively transforms part of mechanisms in the system, adopts new energy to supply power, leads pipelines of various mechanisms to be reasonably arranged, effectively treats separated wastes, can properly discharge the wastes, and has high efficiency and good treatment effect.
Description
The technical field is as follows:
the utility model relates to the technical field of sewage treatment, in particular to a new energy village and town sewage treatment system.
Background art:
at present, a sewage treatment system is an important configuration for treating water pollution, wherein the sewage treatment system comprises a grid channel, a grit chamber, an anoxic chamber, an aerobic chamber, an MBR membrane group and the like which are commonly used, and mainly separates impurities in sewage preferentially, heavy metals and particulate matters are separated, COD is removed through hydrolysis and acidification, and nitrate nitrogen, BOD and the like are removed through denitrification. At present, although the mechanisms are mostly applied to water treatment equipment, the mechanisms are simply used in series, and how to form a high-efficiency and optimized matched sewage treatment system through adaptive transformation of the mechanisms and reasonable discharge of sludge and gas is a problem to be solved at present.
The utility model content is as follows:
in view of the defects of the prior art, the utility model aims to provide a new energy village and town sewage treatment system, which is characterized in that various mechanisms are reasonably arranged, separated wastes are effectively treated, and the waste discharge reaches the standard while the sewage purification efficiency is improved.
In order to solve the technical problems, the utility model adopts the following technical scheme:
the utility model relates to a new energy village and town sewage treatment system which mainly comprises a collecting tank, an adjusting tank, an advection grit chamber, an anaerobic tank, an anoxic tank, an aerobic tank, a membrane tank, a clear water tank and a metering tank, wherein sewage flows in sequence, a thick grid channel is arranged in the collecting tank, a thin grid channel is arranged at the front end of the advection grit chamber, a membrane grid channel is arranged at the rear end of the advection grit chamber, the bottom of the advection grit chamber is butted with a separator, a sludge pump is further arranged for pumping sludge from the aerobic tank and the membrane tank to a sludge dewatering machine for dewatering, the sludge discharged by the sludge dewatering machine enters the sludge tank, the upper parts of the collecting tank and the sludge tank are sealed by a cover and are provided with air entraining pipes, and the air entraining pipes are connected with an ion deodorization machine through a fan.
According to the utility model, water at the bottom of the adjusting tank is pumped into the advection sand basin, and overflow liquid at the upper part of the adjusting tank is connected to the coarse grid channel through a pipeline.
The waste water separated by the separator is connected to a water collecting tank through a pipeline, and the separated sand is conveyed outwards through a lifting mechanism.
The utility model is also provided with a fan room for supplying air to the aerobic pool and the membrane pool, and is provided with a pharmacy for supplying medicine to the anaerobic pool, the anoxic pool, the aerobic pool 6, the clean water pool and the membrane group in the membrane pool.
The clean water tank is provided with a sodium hypochlorite disinfection channel.
The bottom of the middle section of the advection grit chamber is provided with two grit chambers, a first partition plate, a second partition plate and a third partition plate are sequentially arranged from front to back on the middle section, the first partition plate and the third partition plate are positioned on the upper parts of two sides of the middle section, and the second partition plate is positioned on the lower part of the middle section.
The first partition plate is correspondingly positioned above the first grit chamber, the second partition plate is correspondingly positioned at the joint between the two grit chambers, and the third partition plate is correspondingly positioned above the second grit chamber.
The first partition plate and the third partition plate are provided with corresponding air cylinders to be lifted.
The utility model has the advantages that: all kinds of mechanism's pipeline guide rational arrangement in the system adopts the new forms of energy to provide the power for equipment, purifies again and cleaning equipment each part through the backward flow, and the advection grit chamber carries out adaptability transformation, and particulate matter deposits with higher speed to and reduce advection pond area occupied, pile up after the waste mud rational processing of separating, and will contain odorous gas and derive and purify and discharge, waste water is flow back repeatedly and is purified, not only improves the efficiency that the system purifies, and treatment effect is good.
Description of the drawings:
FIG. 1 is a schematic structural diagram of the present invention;
FIG. 2 is a schematic structural diagram of the advection grit chamber of the present invention.
The specific implementation mode is as follows:
the utility model will be further described with reference to the accompanying drawings.
As shown in figure 1, the utility model relates to a new energy village and town sewage treatment system which mainly comprises a water collecting tank 1, an adjusting tank 2, an advection grit chamber 3, an anaerobic tank 4, an anoxic tank 5, an aerobic tank 6, a membrane tank 7, a clean water tank 8 and a metering tank 9, wherein sewage flows in sequence. Wherein, dispose thick grid canal 10 in the catch basin 1 for get rid of the thick suspended solid that probably blocks up water pump unit and pipeline valve, 3 front ends of advection grit chamber dispose thin grid canal 11, the rear end disposes membrane grid canal 12, thin grid canal 11 separates at 3 front ends of advection grit chamber to less solid debris, and then after the granule settlement in 3 middle sections of advection grit chamber, separate tiny solid suspended solid through membrane grid canal 12 at last, make sewage get into the biological reaction flow.
During the water pump-out entering advection grit chamber 3 of 2 bottoms in equalizing basin, 2 upper portion overflow liquids in equalizing basin pass through pipe connection to thick grid canal 10, extract the comparatively even sewage entering advection grit chamber 3 in 2 bottoms in equalizing basin, and the sewage of taking the suspended solid to overflow on adjusting basin 2 returns to thick grid canal 10 and separates debris once more, forms virtuous circle.
3 middle sections bottoms of advection grit chamber are equipped with two grit chambers 30, and lie in the middle section and be equipped with first baffle 31, second baffle 32 and third baffle 33 after to in the past in proper order, first baffle 31 and third baffle 33 are located middle section both sides upper portion, and second baffle 32 is located the middle section lower part. That is, sewage is during through 3 middle sections of advection grit chamber, be stopped by first baffle 31, the rivers can turn to down, be favorable to the solid particle to sink into first grit chamber 30 this moment, then rivers upwards and cross second baffle 32 downwards, a large amount of solid particles can be subsided by blockking of second baffle 32 in this in-process, be stopped by third baffle 33, rivers will have a decurrent turn after crossing second baffle 32, make the solid particle subside once more, so wavy rivers moving path, can make the solid particle subside fast, reduce the length of advection grit chamber 3.
Preferably, the first partition plate 31 is correspondingly positioned above the first grit chamber, the second partition plate 32 is correspondingly positioned at the joint between the two grit chambers, and the third partition plate 33 is correspondingly positioned above the second grit chamber, so that solid particles can be purposefully prevented from settling into the corresponding grit chamber. In addition, in order to adapt to different water flow depths and equipment depths, the first partition plate 31 and the third partition plate 33 are provided with corresponding air cylinders to be lifted, and the depth of the first partition plate 31 and the third partition plate 33 inserted into the advection grit chamber 3 is adjusted through the air cylinders, so that the first partition plate 31 and the third partition plate 33 can be matched with the fixed second partition plate 32 better, and the settling efficiency of solid particles is improved.
The bottom of the advection grit chamber 3 is butted with a separator 13, the separator 13 is a solid-liquid separator, and can separate solid particles and wastewater released from the grit chamber, which is applied in the prior art and is not described herein again. Waste water that separator 13 separated passes through pipe connection to catch basin 1, can form the circulation through backward flow waste water, avoids waste water to arrange outward, and the sand of separation is transported outward through hoist mechanism.
Further, still have sludge pump 14 and draw mud from aerobic tank 6 and membrane cisterna 7 and dewater in sludge dewaterer 15, sludge that sludge dewaterer 15 discharged gets into sludge impoundment 16, pile up contaminated mud, so that centralized processing, and pile up the in-process and can produce gaseous pollutants, the sewage that flows in the catch basin 1 also can disperse the excessive foul smell, consequently catch basin 1 and sludge impoundment 16 upper portion cover sealed and be equipped with bleed pipe 17, bleed pipe 17 passes through the fan and connects ion deodorizer 18, the unified guide has gaseous smell of stink to get into and discharge into the air after ion deodorizer 18 handles.
Furthermore, a fan room 19 is also arranged for supplying air to the aerobic tank 6 and the membrane tank 7, necessary conditions are provided for microbial propagation for the air supply of the aerobic tank 6, the membrane can be flushed for the air supply of the membrane tank 7, the air supply and oxygenation system adopts a multi-path oxygenation matching, and the real-time control of a multi-path dissolved oxygen controller is adopted, so that the dissolved oxygen of the sewage is effectively controlled, and the sustainable time and the survival rate of the sludge are increased; dispose with add drugstore 20 toward anaerobism pond 4, oxygen deficiency pond 5, good oxygen pond 6, clean water basin 8, supply medicine in the membrane group of membrane pond 7, add the carbon source specifically toward anaerobism pond 4 and oxygen deficiency pond 5, add PAC toward good oxygen pond 6, extract the clear water through membrane washing water pump toward clean water basin 8, combine citric acid and sodium hypochlorite to send to and wash the membrane in membrane pond 7, extract the membrane grid in the clear water toward membrane grid canal 12 through membrane grid scavenging pump and wash.
The clear water tank 8 is provided with a sodium hypochlorite disinfection channel 81, and sodium hypochlorite is provided to the sodium hypochlorite disinfection channel 81 by the pharmacy 20, so that the purified clear water can be discharged after being further disinfected and can reach the standard.
It is to be understood that the technical scope of the present invention is not limited to the content of the specification, and that modifications or changes may be made by those skilled in the art based on the above description, and all such modifications and changes are intended to fall within the scope of the appended claims.
Claims (8)
1. The utility model provides a new forms of energy villages and small towns sewage treatment system which characterized in that: mainly comprises a collecting tank (1), an adjusting tank (2), an advection grit chamber (3), an anaerobic tank (4), an anoxic tank (5), an aerobic tank (6), a membrane tank (7), a clean water tank (8) and a metering tank (9) which are used for sewage to flow in sequence, a thick grating channel (10) is arranged in the water collecting tank (1), a thin grating channel (11) is arranged at the front end of the advection grit chamber (3), a membrane grating channel (12) is arranged at the rear end of the advection grit chamber (3), a separator (13) is butted at the bottom of the advection grit chamber (3), a sludge pump (14) is further arranged to pump sludge from the aerobic tank (6) and the membrane tank (7) to a sludge dewatering machine (15) for dewatering, the sludge discharged by the sludge dewatering machine (15) enters a sludge tank (16), the upper parts of the water collecting tank (1) and the sludge tank (16) are sealed by a cover and are provided with air guide pipes (17), and the air guide pipes (17) are connected with an ion deodorizer (18) through a fan.
2. The system of claim 1, wherein the system comprises: and water at the bottom of the adjusting tank (2) is pumped into the advection sand basin (3), and overflow liquid at the upper part of the adjusting tank (2) is connected to the coarse grid channel (10) through a pipeline.
3. The system of claim 1 or 2, wherein the system comprises: the waste water separated by the separator (13) is connected to the water collecting tank (1) through a pipeline, and the separated sand is conveyed outwards through the lifting mechanism.
4. The system of claim 1, wherein the system comprises: a fan room (19) is also arranged to supply air to the aerobic pool (6) and the membrane pool (7), and a pharmacy (20) is arranged to supply medicine to the membrane group in the anaerobic pool (4), the anoxic pool (5), the aerobic pool (6), the clean water pool (8) and the membrane pool (7).
5. The system of claim 4, wherein the system comprises: and a sodium hypochlorite disinfection channel (81) is arranged in the clean water tank (8).
6. The system of claim 1 or 2, wherein the system comprises: advection grit chamber (3) middle section bottom is equipped with two grit chambers (30), and is located the middle section and is equipped with first baffle (31), second baffle (32) and third baffle (33) after to in the past in proper order, first baffle (31) and third baffle (33) are located middle section both sides upper portion, and second baffle (32) are located the middle section lower part.
7. The system of claim 6, wherein the system comprises: the first partition plate (31) is correspondingly positioned above the first grit chamber, the second partition plate (32) is correspondingly positioned at the joint between the two grit chambers, and the third partition plate (33) is correspondingly positioned above the second grit chamber.
8. The system of claim 7, wherein the system comprises: the first partition plate (31) and the third partition plate (33) are provided with corresponding cylinders and can lift.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202123112027.4U CN216273646U (en) | 2021-12-13 | 2021-12-13 | New forms of energy villages and small towns sewage treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202123112027.4U CN216273646U (en) | 2021-12-13 | 2021-12-13 | New forms of energy villages and small towns sewage treatment system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN216273646U true CN216273646U (en) | 2022-04-12 |
Family
ID=81057482
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202123112027.4U Active CN216273646U (en) | 2021-12-13 | 2021-12-13 | New forms of energy villages and small towns sewage treatment system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN216273646U (en) |
-
2021
- 2021-12-13 CN CN202123112027.4U patent/CN216273646U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN209872690U (en) | Leachate treatment process device for garbage transfer station | |
CN102225803B (en) | Biomembrane reactor, waste water treating system and method for treating waste water | |
CN205821109U (en) | Integrated domestic sewage treatment system | |
CN201538734U (en) | Sewage treatment device | |
CN102363537A (en) | Sludge backflow treatment system for secondary biochemical system | |
RU81721U1 (en) | WASTE WATER TREATMENT PLANT | |
CN209161794U (en) | It is a kind of for handling the integrated high-efficiency sewage treatment device of city domestic sewage | |
CN216273646U (en) | New forms of energy villages and small towns sewage treatment system | |
CN207713606U (en) | A kind of processing system with excrement medical waste water | |
CN201268647Y (en) | Small-sized domestic sewage processing system | |
CN210974307U (en) | Ecological rural sewage treatment plant | |
CN103936157B (en) | Integration degree of depth domestic sewage treatment device and sewage water treatment method thereof | |
CN1736907A (en) | Deep cleaning treatment process for city effluent | |
CN210176666U (en) | Domestic waste filtration liquid high efficiency treatment all-in-one | |
CN208218511U (en) | The processing unit of high-concentration sewage | |
CN1162360C (en) | Process for treating sewage of oil recovery | |
CN201268648Y (en) | Multifunctional universal sewage treatment system | |
CN206089326U (en) | MBR bio -membrane process integration sewage treatment device | |
CN218951168U (en) | Septic tank processor | |
CN212293207U (en) | Semi-fixed bed normal position purifies domestic sewage device | |
CN214457489U (en) | Domestic sewage treatment device | |
CN109264934A (en) | It is a kind of for handling the integrated high-efficiency sewage treatment device of city domestic sewage | |
CN220223874U (en) | Micro-power sewage treatment integrated device | |
CN220788201U (en) | Reclaimed water recycling treatment system for petrochemical wastewater | |
CN219314752U (en) | Compound enhanced sewage treatment system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |