CN200946119Y - A new biological aerated filter - Google Patents
A new biological aerated filter Download PDFInfo
- Publication number
- CN200946119Y CN200946119Y CNU2006200983761U CN200620098376U CN200946119Y CN 200946119 Y CN200946119 Y CN 200946119Y CN U2006200983761 U CNU2006200983761 U CN U2006200983761U CN 200620098376 U CN200620098376 U CN 200620098376U CN 200946119 Y CN200946119 Y CN 200946119Y
- Authority
- CN
- China
- Prior art keywords
- pipe
- water
- siphon
- draining
- feed
- 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.)
- Expired - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 90
- 239000000463 material Substances 0.000 claims abstract description 6
- 230000006378 damage Effects 0.000 claims abstract 4
- 238000005273 aeration Methods 0.000 claims description 5
- 102000010637 Aquaporins Human genes 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 23
- 230000000630 rising effect Effects 0.000 abstract description 14
- 238000011001 backwashing Methods 0.000 abstract description 11
- 238000012423 maintenance Methods 0.000 abstract description 3
- 238000010276 construction Methods 0.000 abstract 2
- 238000011010 flushing procedure Methods 0.000 description 12
- 238000000605 extraction Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 5
- 230000001066 destructive effect Effects 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000000813 microbial effect Effects 0.000 description 4
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000010525 oxidative degradation reaction Methods 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Filtration Of Liquid (AREA)
Abstract
A novel aerating biologic filtering pool is characterized in that: inside the pool are arranged a filtering pool, a feed-water canal, a waterexit weir and a timekeeping water tank, while the pool bottom is connected with a rising pipe; the rising pipe communicates a plurality of aerating biologic filtering pools and is connected with a waterexit trough; a draining siphon pipe is connected with a water-seal well and an aerating biologic filtering pool, while a feed-water siphon pipe with the feed-water canal and the waterexit weir; on the feed-water siphon pipe is connected a feed-water auxiliary siphon pipe, a feed-water suction pipe and a feed-water siphon destruction pipe, while on the draining siphon pipe is connected a draining auxiliary siphon pipe, a draining suction pipe and a draining siphon destruction pipe with the draining siphon destruction pipe connected with the timekeeping water tank; inside the filtering pool is filled with filtering material, while the bottom of the filtering pool is provided with a filtering head, an aerating pipe and a backwashing air tube. The utility model has the advantages of that: (1) it is of complete hydraulic automatic control, convenient operation, simplifying management and less maintenance workload; (2) no special clear water tank is needed, thereby saving construction cost; (3) backwash pump is not needed with less equipment investment and running cost; (4) no large-scale valve but siphon pipe is arranged on the filtering pool, thereby reducing construction cost; (5) lattice subdivision of filtering pool is realized, thereby being helpful to distribute water and gas evenly.
Description
Technical field
The utility model relates to a kind of novel BAF.
Background technology
BAF is the sewage treatment process that contact oxidation technology and suspended substance filtration process are combined, its technological principle is the less particulate filter of a certain amount of particle diameter of filling in the filter tank, the filter material surface microbial film of growing, the inner aeration in filter tank, effluent stream through the time, owing to adhere to high-concentration biological film amount on the filtrate, utilize the pollutent in the quick degrading waste water of its strong oxidative degradation ability, simultaneously, utilize particle diameter of filter medium features of smaller and biomembranous biological flocculation, hold back a large amount of suspended substances in the sewage, and guarantee that the microbial film that comes off can not drift out with water, reaches the purpose of purifying liquid waste thus.Carry out along with filtering, because microbial film progressive additive in the filter material layer, suspended solids constantly accumulates, water head loss by filtration progressively strengthens, under certain intake pressure, design discharge will can not get guaranteeing, should carry out back flushing regeneration this moment to remove excessive microbial film and suspended solids in the filter bed, recover the processing power in filter tank.The back-flushing method of BAF is to utilize backwashing pump to wash, and backwashing water derives from tank.The main drawback of this purging method is: (1) need be provided with special backwashing pump, because the back flushing water yield is bigger, the power of backwashing pump is bigger, has increased facility investment, maintenance of the equipment and the operation electricity charge; (2) the back flushing pond must be set and store backwashing water, because the back flushing water yield is bigger, often the backwashing water pool volume is bigger, increases civil engineering costs; Must stop into water during (3) owing to back flushing, therefore water intaking valve, outlet valve, back-washing valve and water discharge valve must be set controls water (flow) direction, has increased the expense of valve on the one hand, has increased the difficulty of operational administrative on the other hand.
Summary of the invention
The purpose of this utility model provides a kind of novel BAF, and it need not special clear water tank and backwashing pump, saves civil engineering and cost of equipment.
The utility model is achieved like this, it comprises into water siphon pipe, discharge siphon, water tank clocks, trapped well, inlet channel, effluent weir, effluent trough, drainage tray, it is characterized in that being provided with in the BAF filtering basin, inlet channel, effluent weir, timing tank, the BAF bottom is connected with rising pipe, rising pipe interconnects some lattice BAF, rising pipe connects effluent trough, discharge siphon connects trapped well and BAF, the water inlet siphon pipe connects inlet channel and effluent weir 10, on the water inlet siphon pipe, connect the auxiliary siphon pipe of water inlet, water inlet extraction pipe and water inlet siphon destructing tube, on discharge siphon, connect the auxiliary siphon pipe of draining, draining extraction pipe and draining siphon destructing tube, the draining siphon destructive pipe coupling water tank that clocks, filtrate is housed in the filtering basin, and filter is arranged in the filtering basin bottom, aeration tube and back flushing tracheae.
The utility model has the advantages that: (1) waterpower is fully controlled automatically, and operation is convenient, and management is simple, and maintenance workload is little; (2) do not need special clear water tank, save civil engineering costs; (3) backwashing pump need be set, save facility investment and working cost; (4) do not need large-scale valve on the filter tank, utilize siphon pipe to replace valve, cost is low; (5) filter tank segmentation lattice be can accomplish, uniform water distribution, distribution helped.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
In the drawings 1, the auxiliary siphon pipe 2 of water inlet, water inlet extraction pipe 3, water inlet siphon destructing tube 4, BAF 5, water inlet siphon pipe 6, discharge siphon 7, water tank 8 clocks, trapped well 9, inlet channel 10, effluent weir 11, filter 12 aeration tubes 13, recoil Xian tracheae 14, rising pipe 15, total rising pipe 16, effluent trough 17, filtrate 18, top water-level 19, filtering basin 20, effluent trough top water-level 21, siphon pipe 22 is assisted in draining, draining extraction pipe 23, the draining siphon destructing tube
Embodiment
As shown in Figure 1, the utility model comprises into water siphon pipe 5, discharge siphon 6, water tank 7 clocks, trapped well 8, inlet channel 9, effluent weir 10, effluent trough 16, rising pipe 14, it is characterized in that being provided with in the BAF 4 filtering basin 19, inlet channel 9, effluent weir 10, timing tank 7, BAF 4 bottoms are connected with rising pipe 14, rising pipe interconnects some lattice BAF, rising pipe connects effluent trough 16, the BAF 4 outer trapped wells 8 that connect, discharge siphon 6 connects trapped well 8 and BAF 4, water inlet siphon pipe 5 connects inlet channel 9 and effluent weir 10, on the water inlet siphon pipe, connect the auxiliary siphon pipe 1 of water inlet, water inlet extraction pipe 2 and water inlet siphon destructing tube 3, connect the auxiliary siphon pipe 21 of draining in discharge siphon, draining extraction pipe 22 and draining siphon destructing tube 23, the draining siphon destructive pipe coupling water tank 7 that clocks, filtrate 17 is housed in the filtering basin 19, filter 11, aeration tube 12 and back flushing tracheae 13 are arranged in the filtering basin bottom.During use, former water enters inlet channel 9, because the effect of auxiliary siphon pipe 1 of water inlet and water inlet extraction pipe 2, making into, water siphon pipe 5 forms vacuum, water inlet siphon pipe 5 produces syphonic effect, former water enters filtering basin 19 by syphonic effect to begin to filter, and the water after the filtration is discharged through rising pipe 14, total rising pipe 15 and effluent trough 16.Carry out along with filtering, the water level in the filter tank rises gradually, and when water level rose to top water-level 18, the current overflow entered the auxiliary siphon pipe 21 of draining.Under the effect of auxiliary siphon pipe 21 of draining and draining extraction pipe 22, constantly take the air in the discharge siphon 6 away, discharge siphon 6 forms siphon.Because discharge siphon 6 forms siphons, the water level in the filter tank descends rapidly, and when the water level in the filter tank is lower than the mouth of pipe of water siphon destructing tube 3 into when following, water inlet siphon pipe 5 is communicated with atmosphere, and the siphon destructive of intaking stops into water; When the water level in the filter tank was lower than the water level 20 of effluent trough, current began reversed flow, were flowed to filter material layer 17 by effluent trough, and current carry out back flushing to filter material layer, and flushing waste water is discharged the filter tank by discharge siphon 6.Backwashing time determines that by timing tank 7 in the time of discharge siphon 6 drainings, draining siphon destructing tube 23 is taken the water in the timing tank away, when the water of timing tank is drained, draining siphon destructing tube 23 in the timing tank is communicated with atmosphere, the draining siphon destructive, and back flushing finishes.After back flushing finishes, the filter tank median water level rises gradually, when water level rises to the mouth of pipe of water siphon destructing tube 3 into when above, water inlet siphon pipe 5 cuts off with air, under the effect of auxiliary siphon pipe 1 of water inlet and water inlet extraction pipe 2, the air in the water inlet siphon pipe 5 is constantly taken away, and water inlet siphon pipe 5 forms vacuum, siphon forms, and water inlet is filtered again.The water of whole backwash process is provided by other filter grid filtered water, the clear water tank need be set, and all filter grids are interconnected by rising pipe.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200983761U CN200946119Y (en) | 2006-08-12 | 2006-08-12 | A new biological aerated filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006200983761U CN200946119Y (en) | 2006-08-12 | 2006-08-12 | A new biological aerated filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200946119Y true CN200946119Y (en) | 2007-09-12 |
Family
ID=38733182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006200983761U Expired - Fee Related CN200946119Y (en) | 2006-08-12 | 2006-08-12 | A new biological aerated filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200946119Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102267758A (en) * | 2011-07-27 | 2011-12-07 | 新疆博能环保工程有限公司 | Layered automatic air reoxygenation ecological pool |
-
2006
- 2006-08-12 CN CNU2006200983761U patent/CN200946119Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102267758A (en) * | 2011-07-27 | 2011-12-07 | 新疆博能环保工程有限公司 | Layered automatic air reoxygenation ecological pool |
| CN102267758B (en) * | 2011-07-27 | 2012-11-28 | 新疆博能环保工程有限公司 | Layered atmospheric automatic reoxygenation ecological pool |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070912 Termination date: 20100812 |