CN200974792Y - Integral life sewage treating equipment - Google Patents
Integral life sewage treating equipment Download PDFInfo
- Publication number
- CN200974792Y CN200974792Y CN 200620120390 CN200620120390U CN200974792Y CN 200974792 Y CN200974792 Y CN 200974792Y CN 200620120390 CN200620120390 CN 200620120390 CN 200620120390 U CN200620120390 U CN 200620120390U CN 200974792 Y CN200974792 Y CN 200974792Y
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- CN
- China
- Prior art keywords
- slag bath
- tank
- sewage pump
- submersible sewage
- oil removal
- 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.)
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- Activated Sludge Processes (AREA)
Abstract
With under aerator for oxygen supply and mixing, an integrated domestic sewage treatment device consists of an oil and slag separating tank, an adjusting chamber and a SBR biological contact tank. The aerobic nitrification and hypoxic denitrification are realized with no machine room and no voice pollution. The air intake is arranged in the adjusting chamber to reduce the odor spillover. With submersible sewage pump for draining, the device has advantages of simple structure, and table and reliable property. The draining is not influenced by the deep bury of the equipment. The remained sludge is reserved and digested by the oil and slag separating tank, which makes the daily manual operating projects less. The drainage treatment of equipment is capable of achieving the first standard requires of State Standards for Comprehensive Discharge of Wastewater (GB8978-1996).
Description
Technical field
Utility model relates to integrated domestic sewage treatment device, be suitable for especially using, as the sanitary sewage in the less place of the water yields such as village, rural area, holiday village, hotel, Expressway Service or the processing of other kin organic waste waters away from the place of municipal drainage pipeline.
Background technology
At present, known integrated domestic sewage treatment device all adopts the catalytic oxidation treatment process, because the sedimentation effect of second pond is bad, excess sludge is not effectively addressed, cause treatment effect bad, be difficult to the stable requirement that reaches " waste water comprehensive discharge standard " secondary standard (GB8978-1996).And it is pretty troublesome to change filler, can not denitrogenation, and the scope of application is limited to.
Summary of the invention
Utility model is to provide a kind of processing efficiency height, energy denitrogenation, strong to water quality and quantity variation adaptability, operational management is simple, need not to dispose the concrete management personnel, the requirement of " waste water comprehensive discharge standard " primary standard (GB8978-1996) be can stable reach, the sanitary sewage of the less water yield and the treatment facility of kin organic waste water adapted to.
Utility model is established in one with 3 oil removals every slag bath, 1 equalizing tank and 1 SBR biological treatment tank, both can be embedded in undergroundly, also can place vault.
Utility model adopts unique oil removal every slag bath, can effectively block except that foreign material, oil slick and sediment, can store and digest excess sludge again.Select aerator under water for use, can realize aerobic nitrification by aeration, can serve as stirrer again and realize the anoxic denitrification denitrogenation, without machine room, sound pollution useless is arranged at equalizing tank with inlet mouth, and it is excessive also can to reduce stink.Adopt unique water mode of straining, simple structure, stable and reliable for performance, draining is not subjected to the influence of equipment buried depth.Automatically finish biological cultivation process, can be for a long time automatically continuously or intermittent operation, running maintenance is simple.An oil removal of cleaning does not have other artificial operation items every the body refuse of slag bath about half a year.Except that electrical control cubicles, equipment places underground, can afforest or harden in ground.
Description of drawings
Describe the structure and the technical process of equipment in detail below in conjunction with accompanying drawing (equipment sectional view).Constitute housing by glass reinforced plastic or the metal sheet that scribbles impregnating material, impregnating material can adopt resin, epoxy coal asphalt paint or other analogous materials.In housing, be separated out 3 oil removals every slag bath, 1 equalizing tank and 1 SBR biological treatment tank with above-mentioned materials.
Sewage enters oil removal every slag bath (2) by water-in (1), blocks through grid (3) earlier and removes thick foreign material, and oil removal can effectively be blocked except that oil slick and sediment every slag bath (2), and stores and digest the excess sludge of SBR biological treatment tank (14) generation; Water outlet enters equalizing tank (5) through thrust-augmenting nozzle (4) gravity flow, and water inlet submersible sewage pump (8) lifting sewage enters SBR biological treatment tank (14); After SBR biological treatment tank (14) reaches high liquid level, starting under water, aerator (12) carries out aerobic aeration and anoxic stirring, inlet pipe (11) import of aerator (12) under water is located at equalizing tank (5), on inlet pipe (11) pipeline electrically operated valve (9) is housed, when electrically operated valve (9) is opened under water aerator (12) carry out aerobic aeration, electrically operated valve (9) when closing under water aerator (12) carry out anoxic and stir; Aerator (12) carries out stopping after aerobic aeration and anoxic are stirred for some time under water, and SBR biological treatment tank (14) is in the precipitation state; About about 1 hour of SBR biological treatment tank (14) precipitation, pollutants in sewage is fully degraded at SBR biological treatment tank (14), suspended substance is precipitated to be held back, start the draining submersible sewage pump (15) that is arranged on about 1 meter high support (17) at the bottom of SBR biological treatment tank (11) pond, the supernatant liquor of SBR biological treatment tank (14) is through rising pipe (18) standard discharge; After SBR biological treatment tank (14) reached low liquid level, draining submersible sewage pump (15) stopped, and started spoil disposal submersible sewage pump (10), extracted the part excess sludge out and entered oil removal every slag bath (2) storage and digestion through shore pipe (6).
Oil removal is equipped with access opening (16) every slag bath (2), equalizing tank (5) and SBR biological treatment tank (14).Water inlet submersible sewage pump (8), aerator (12), draining submersible sewage pump (15) and spoil disposal submersible sewage pump (10) are equipped with self coupling device (7) under water, are convenient to take out to keep in repair.
Equipment is arranged to automatic cycle when operation, starts or stops periodic duty by the equalizing tank liquid level, all electromechanical equipments according to the program of setting in the automatic control cabinet with limit in relevant liquid level under automatic operation.When equalizing tank reached high liquid level, cycle (phase can be made as 8 hours weekly) starting point timing began, and water inlet submersible sewage pump (8) starts, and moved 1 hour or SBR biological treatment tank (14) stops intake pump when reaching high liquid level; Timing 1 hour aerator (12) under water starts, and moves to stop after 5 hours; Timing 7 hours, draining submersible sewage pump (15) start, and moves 1 hour or SBR biological treatment tank (14) reaches when hanging down liquid level and stops; Timing 1 hour, the electrically operated valve (9) of aerator (12) inlet pipe is opened under water, closes after 4 hours; After the timing 7.9 hours, spoil disposal submersible sewage pump (10) starts, and spoil disposal stopped after 5 minutes.After the timing 8 hours, the cycle timing is made zero, and enters the next cycle of operation (cycle duration and in the cycle each time in stage can shorten or prolong according to practical situation).
The operation condition and SBR biological treatment tank (14) the periodic duty technology of each electromechanical equipment match (referring to SBR biological treatment tank Running Status Table) in cycle, and SBR biological treatment tank (14) is realized the loop cycle of water inlet, aerobic nitrification, anoxic denitrification, precipitation, drainage procedure successively.Equipment moves one or more all after dates, and the equalizing tank liquid level is reduced to low liquid level, and then equipment enters lay-up period, rises to high liquid level until the equalizing tank liquid level, and equipment is the restore cycle operation again.Between lay-up period, aerator (12) started aeration oxygen supply 1 hour every 6 hours under water, to guarantee the activity of active sludge.
SBR biological treatment tank Running Status Table
Embodiment
Embodiment of the present utility model: the equipment that the processing power that housing employing glass reinforced plastic is made is 60 tons/day, 3000 millimeters * 12000 millimeters of physical dimension φ, wherein, oil removal is 4000 millimeters every the total length of slag bath, equalizing tank and SBR biological treatment tank, and oil removal is every each long 1000 millimeters of slag baths.Water inlet submersible sewage pump, draining submersible sewage pump and under water the power of aerator be 1.5 kilowatts, the power of spoil disposal submersible sewage pump is 0.75 kilowatt.The diameter of water-in is 200 millimeters, and the diameter of the adapter of water inlet submersible sewage pump, draining submersible sewage pump is 65 millimeters, shore pipe and under water the diameter of aerator inlet pipe be 50 millimeters.The equipment cycle of operation is 8 hours, and water inlet COD concentration is 300 mg/litre, and ammonia nitrogen concentration is 25 mg/litre.Through using, the every water-quality guideline of draining all can reach the requirement of " waste water comprehensive discharge standard " primary standard (GB8978-1996).
Claims (5)
1, a kind of integrated domestic sewage treatment device, comprise that 3 grades of oil removals are every slag bath, equalizing tank, SBR biological treatment tank, it is characterized in that: equipment pond body is divided into 3 grades of oil removals every slag bath, equalizing tank, SBR biological treatment tank, the 1st grade of oil removal communicates every slag bath with the 2nd grade of oil removal through grid every the slag bath outlet, the 2nd grade of oil removal communicates every slag bath with the 3rd level oil removal through thrust-augmenting nozzle every the slag bath outlet, the 3rd level oil removal communicates with equalizing tank through thrust-augmenting nozzle every the slag bath outlet, and the equalizing tank outlet communicates with the SBR biological treatment tank through submersible sewage pump and pipeline.
By the described integrated domestic sewage treatment device of claim 1, it is characterized in that 2, the equalizing tank upper end is provided with access opening, and submersible sewage pump is housed in the pond, submersible sewage pump has the self coupling device.
3, by the described integrated domestic sewage treatment device of claim 1, it is characterized in that aerator under water is housed in the SBR biological treatment tank, and draining submersible sewage pump and spoil disposal submersible sewage pump all have the self coupling device, the top, pond is provided with access opening.
By the described integrated domestic sewage treatment device of claim 3, it is characterized in that 4, aerator inlet pipe inlet is located at equalizing tank top, and electrically operated valve is housed under water on pipeline.
By the described integrated domestic sewage treatment device of claim 3, it is characterized in that 5, the outlet of spoil disposal submersible sewage pump is located at the 1st grade of oil removal every slag bath top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620120390 CN200974792Y (en) | 2006-06-21 | 2006-06-21 | Integral life sewage treating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620120390 CN200974792Y (en) | 2006-06-21 | 2006-06-21 | Integral life sewage treating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200974792Y true CN200974792Y (en) | 2007-11-14 |
Family
ID=38901082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620120390 Expired - Fee Related CN200974792Y (en) | 2006-06-21 | 2006-06-21 | Integral life sewage treating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200974792Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101648767B (en) * | 2009-07-06 | 2011-04-13 | 西南铝业（集团）有限责任公司 | Method and system for processing hot-rolling and emulsifying wastewater for aluminum plate |
| CN101792212B (en) * | 2010-01-28 | 2011-09-14 | 同济大学 | Integrated air lift SBR reactor |
-
2006
- 2006-06-21 CN CN 200620120390 patent/CN200974792Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101648767B (en) * | 2009-07-06 | 2011-04-13 | 西南铝业（集团）有限责任公司 | Method and system for processing hot-rolling and emulsifying wastewater for aluminum plate |
| CN101792212B (en) * | 2010-01-28 | 2011-09-14 | 同济大学 | Integrated air lift SBR reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C57 | Notification of unclear or unknown address | ||
| DD01 | Delivery of document by public notice |
Addressee: Yang Shuibin Document name: Notification of Termination of Patent Right |
|
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |