CN202785795U - Internal recycle bio-filter reactor - Google Patents
Internal recycle bio-filter reactor Download PDFInfo
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- CN202785795U CN202785795U CN2012204966370U CN201220496637U CN202785795U CN 202785795 U CN202785795 U CN 202785795U CN 2012204966370 U CN2012204966370 U CN 2012204966370U CN 201220496637 U CN201220496637 U CN 201220496637U CN 202785795 U CN202785795 U CN 202785795U
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- pipe
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- filtrate
- water
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- 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
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Abstract
The utility model discloses an internal recycle bio-filter reactor which is characterized in that the inner side of a tank is filled with filter material, the upper portion of the tank is provided with a clean water outlet, and a center water inlet pipe is vertically arranged inside the tank. The lower portion of the center water inlet pipe is provided with a filter material equally-distributing machine. A center material-lifting pipe is arranged inside the center water inlet pipe. Two ends of the center lifting-material pipe respectively stretch out of two ends of the center water inlet pipe. The space between the upper end of the center water inlet pipe and the center lifting-material pipe is sealed. The side face of the center water inlet pipe is communicated with a waterhead height tube. The side face of the waterhead height tube is provided with a water inlet. The upper end of the center lifting-material pipe extends into a folded-plate-type washing-material machine. The folded-plate-type washing-material machine is connected with the tank and a discharge pipe. The discharge pipe is arranged below the clean water outlet. The lower part of the tank is provided with an aeration perforated pipe. A back-flushing gas inlet pipe extends into the tank through the top of the tank. The lower end of the back-flushing gas inlet pipe is arranged on the lower portion of the tank. The internal recycle bio-filter reactor is capable of processing produced water continuously, back-flushing the filter material and discharging pollution.
Description
Technical field
The utility model relates to technical field of sewage treatment equipment, specifically a kind of internal circulation biological filter reactor.
Background technology
BAF is called for short BAF, is a kind of New biological membrane method sewage water treatment method that grows up the America and Europe end of the eighties, and the method has removes SS, COD, BOD, nitrated, denitrogenation, dephosphorization, removal AOX(objectionable impurities) effect.Its advantage is as follows: 1. one-time investment is than traditional method low 1/4; 2. area occupied is 1/10～1/5 of common process, running cost low 1/5; 3. water inlet requires suspended substance 50～60mg/L, preferably processes combining with primary reinforcement, as adopting hydrolysis acidification pool; 4. filtrate adopts haydite more, diameter 5mm, floor height 1.5～2m; 5. water down, gas reverse flow up can not establish second pond.
BAF is compared with conventional activated sludge process, have organic loading height, floor space little (be conventional activated sludge process 1/3), less investment (saving 30%), can not produce the advantages such as sludge bulking, the oxygen transmission efficiency is high, effluent quality is good, but it requires tight (general requirement SS≤100mg/L to water inlet SS, best SS≤60mg/L), therefore need to carry out pre-treatment to water inlet.Simultaneously, its back flushing water yield, head loss are all larger.
In addition, BAF is as integrating bio-oxidation and the novel process of holding back suspended solids, saved post precipitation pond (second pond), have volumetric loading, hydraulic load is large, hydraulic detention time is short, required initial cost is few, and effluent quality is good: operation energy consumption is low, the characteristics that working cost is few.
But existing BAF need to regularly be carried out back flushing, the SS that wear out microbial film and filter tank are held back gets rid of, back flushing need to be carried out gas, water associating backwash, need to be equipped with backwash pond, independent backwash gas blower, backwash water pump and pipeline valve etc., the system operation process is complicated, supporting structures and equipment are numerous, observe from existing heavy construction practical application example, and the attached supporting structures of its backwashing function account for the 40-50% for the treatment of system total amount.Can not realize continuous back flushing and blowdown, when back flushing, BAF need stop production run.
In view of problem and the defective that above-mentioned existing BAF in use exists, the inventor relies on for many years working experience and abundant expertise actively to be researched and developed, and finally develops a kind of internal circulation biological filter reactor.Can realize producing continuously water, continuously backwash filtrate and continuous blowdown.
The utility model content
In order to solve the above-mentioned problems in the prior art, the utility model provides a kind of internal circulation biological filter reactor.Can realize producing continuously water, continuously backwash filtrate and continuous blowdown.
In order to solve the problems of the technologies described above, the utility model has adopted following technical scheme:
The internal circulation biological filter reactor, comprise: tank body, be filled with filtrate in the tank body, tank body top is provided with the Graceful mouth of a river, vertically be provided with the center water inlet pipe in the tank body, the bottom of described center water inlet pipe is provided with the filtrate balancing distributing devices, be provided with the center extraction pipe in the water inlet pipe of center, the two ends of center water inlet pipe are stretched out respectively at the two ends of center extraction pipe, seal between the upper end of described center water inlet pipe and the center extraction pipe, the side of described center water inlet pipe is communicated with the head height pipe, the side of described head height pipe has water-in, the upper end of center extraction pipe is stretched in the folded plate type diffuser, and the folded plate type diffuser is connected with tank body, and the folded plate type diffuser connects blow-off pipe, described blow-off pipe is positioned at the below at the Graceful mouth of a river, the bottom is provided with the aeration perforated pipe in the tank body, and the backwash inlet pipe stretches in the tank body from the top of tank body, and the lower end of described backwash inlet pipe is positioned at tank body lower part.
Further, described backwash inlet pipe along between center water inlet pipe and the center extraction pipe to downward-extension, the lower end of center water inlet pipe is stretched out in the lower end of backwash inlet pipe.
Further, described folded plate type diffuser upper end is connected with tank body is airtight, and the end that blow-off pipe is positioned at the folded plate type diffuser is provided with the filtrate disrupter.
Further, the grid hole dividing plate of described filtrate disrupter for arranging around the center extraction pipe forms the filtrate isolated area between described grid hole dividing plate and the center extraction pipe, and described blow-off pipe stretches in the filtrate isolated area.
Further, described tank interior is provided with the clear water bucket, and the described Graceful mouth of a river is located in the clear water bucket.
Further, described backwash inlet pipe connects air compressor, and the backwash inlet pipe is provided with reducing valve, valve and under meter.
Further, described aeration perforated pipe connects gas blower by inlet pipe, and inlet pipe is provided with under meter.
Further, described water-in connects water equipment.
Further, be provided with coarse filter and under meter between described water-in and the water equipment.
Further, described inner tank wall is provided with the end vertebra support of supporting the filtrate balancing distributing devices.
Further, described filtrate is spherical haydite or column type active carbon particles.
Compared with prior art, the beneficial effects of the utility model are:
Internal circulation biological filter reactor of the present utility model can realize producing continuously water, continuously backwash filtrate and continuous blowdown.Determine whether to carry out backwash and backwash time length by the head in the observation water grease head highness pipe, be convenient to control, realize that product water and backwash filtrate carry out simultaneously.Can make simultaneously that bacterium, microbial biomass remain under relatively a large amount of, the stable state between the filtrate in the reactor, continue to carry out the biochemical treatment of sewage.By the aeration oxygen-supplying amount of accuracy-control system, with the specific bacteria group culture of certain water treatment in the more convenient realization response device.The backwash of internal circulation biological filter reactor of the present utility model and blowdown are convenient to realize automatic control by providing the backwash pressurized gas to realize.The utility model has been saved all supporting back flushing structures and equipment of common BAF, has saved processing cost and floor space.
Description of drawings
Fig. 1 is the structural representation of the internal circulation biological filter reactor of utility model.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model is described in further detail, but not as to restriction of the present utility model.
Fig. 1 is the structural representation of the internal circulation biological filter reactor of utility model.As shown in Figure 1, the internal circulation biological filter reactor comprises: tank body 1, be filled with filtrate 2 in the tank body 1, and filtrate 2 is spherical haydite or column type active carbon particles, or other spherical filtrate and granule filter materials that are fit to.Tank body 1 top is provided with the Graceful mouth of a river 3, the tank body 1 interior center water inlet pipe 4 that vertically is provided with.The bottom of center water inlet pipe 4 is provided with filtrate balancing distributing devices 5, and tank body 1 inwall is provided with the end vertebra that supports filtrate balancing distributing devices 5 and supports 18.Be provided with center extraction pipe 6 in the center water inlet pipe 4, the two ends of center water inlet pipe 4 are stretched out respectively at the two ends of center extraction pipe 6.Sealing between the upper end of center water inlet pipe 4 and the center extraction pipe 6.The side of center water inlet pipe 4 is communicated with head height pipe 7.The side of head height pipe 7 has water-in 8, and the upper end of center extraction pipe 6 is stretched in the folded plate type diffuser 9, and the folded plate type diffuser is connected with tank body.Folded plate type diffuser 9 connects blow-off pipe 10, and blow-off pipe 10 is positioned at the below at the Graceful mouth of a river, and tank body 1 interior bottom is provided with aeration perforated pipe 11.Aeration perforated pipe 11 is arranged on the carriage 12 of fixing with tank body 1 inwall.Backwash inlet pipe 25 is in tank body 1 is stretched on the top of tank body 1, and the lower end of backwash inlet pipe 25 is positioned at tank body lower part.
Tank interior is provided with clear water bucket 27, and the Graceful mouth of a river 3 is located in the clear water bucket 27.Guaranteed the stable of the clear water water surface.Backwash inlet pipe 25 connects air compressor 21, and the backwash inlet pipe is provided with reducing valve 28, valve 22 and under meter 23.Valve 22 can adopt magnetic valve, is convenient to control.Air compressor 21 is standby for often offering, and when air compressor air storage tank reaches setting pressure, air compressor 21 is stopped transport automatically.The end that blow-off pipe 10 is positioned at tank body 1 outside is communicated with sump 29, and blow-off pipe 10 is upwards bending in sump 29, highly is lower than the clear water water level, carries out blowdown by liquid level difference.The sewage draining exit of sump 29 is provided with valve 24.Valve 24 can adopt electric butterfly valve, or Pneumatic butterfly valve, or the valve that adopts as required other to be fit to.
Aeration perforated pipe 11 connects gas blower 13.Be provided with the spinner-type flowmeter 14 of metering air demand between gas blower 13 and the aeration perforated pipe 11.Water-in 8 connects water equipment 15.Water equipment 15 adopts two water pumps, and two water pumps use in the mode of the using and the reserved.Be provided with between water-in 8 and the water equipment 15 for the coarse filter 16 that filters hair etc. and the spinner-type flowmeter 17 of quantative water supply amount.Tank body 1 bottom is tapered.The bottom of tank body 1 is communicated with establishes valvular blow-down pipe 19.The side of tank body 1 conical lower portion is provided with discharge opening 20.
Tank body 1 in the utility model can be metal tank body, also can be the structures such as civil engineering Chi Ti.Folded plate type diffuser 9 upper ends and 1 airtight connection of tank body, sewage and clear water are effectively isolated like this, guarantee the clear water water quality when product water and backwash filtrate carry out simultaneously.
The process that internal circulation biological filter reactor of the present utility model carries out sewage disposal is as follows:
A. by water equipment sewage is sent into the center water inlet pipe via water-in and head height pipe, sewage is discharged from the lower end of center water inlet pipe, and is upward through filtrate, is discharged by the Graceful mouth of a river through the microbially decontaminate gained clear water in filtrate and the filtrate; Simultaneously, the aeration perforated pipe carries out aeration and is beneficial in filter material layer breeding and generates a large amount of bacteriums, microorganism;
B. by head height pipe observation water inlet head, when head reaches predetermined height, in tank body, pass into the backwash pressurized gas, the backwash pressurized gas drives the filtrate extracting that makes progress from extraction pipe lower end, center, and by entering the folded plate type diffuser on the extraction pipe of center, the flow of control of sewage disposal pipe is greater than the flow of the water of center extraction pipe extracting, make clear water upwards clean filtrate from the lower end of folded plate type diffuser, filtrate after the cleaning is from upper strata that the folded plate type diffuser is fallen filtrate in the tank body, clean filtrate gained sewage and discharge from blow-off pipe, the air input of control backwash pressurized gas and control water inlet working time head height are in pre-determined range.Predetermined height is between pre-determined range (1.5～2.5 meters).Generally reach 1.5 meters and can carry out backwash.
The utility model is by arranging liquidometer at the head height pipe, when the water inlet head reaches predetermined height, automatically open air-supplying valve 22, in tank body 1, pass into the backwash pressurized gas, the backwash pressurized gas drives the filtrate extracting that makes progress from center extraction pipe 6 lower ends, and entering the folded plate type diffuser by center extraction pipe 6 upper ends, ceramic grain filter falls into filter material layer upper end by flap because its proportion overweights water in the folded plate type diffuser.Set the blowdown water level and be lower than clear water water outlet water level (clear water water outlet water level is constant), water amount of blowdown and the Graceful water yield equal the flooding quantity total amount, and water amount of blowdown guarantees that greater than the water yield of carrying on the center extraction pipe 6 clear water upwards cleans filtrate.At this moment, open the valve 24(electric butterfly valve on the sewage draining exit), filtrate and water in the folded plate type diffuser move following mode:
At first filtrate is in the material pipe is washed at the center, because the violent stirring of mixing wastewater with air, the microbial film of growing on the filtrate is come off fully, separate with filtrate, as previously mentioned, filtrate drops down onto filter material layer upper end next time in action of gravity, the wastewater suspended substance of holding back between the microbial film that comes off and filtrate since its proportion close to water, will be effluxed this moment by blow-off pipe;
Because designated water level is poor, flooding quantity is greater than water amount of blowdown in addition, water purification after this moment, processed the reactor upper end will be by in the bottom-up inflow folded plate type diffuser of flap position, water purification upwards, filtrate is downward, water purification will carry out reverse elutriation to filtrate, and flap arranges and further disperses being conducive to filtrate, improve and eluriate effect.The suspended substance that cleans out in microbial film and the water body can only efflux with the sewage current because its proportion, can't overcome the clean water area that upwards flows near water, thus continuous backwash, the continuous blowdown of the system of realization; Water purification effluxes at reactor upper end Heng Shuiweichu after the unnecessary processing.
Air inlet switch and the single of control backwash pressurized gas are delayed time working time, can select the thickness of each backwash filter material layer, biomass in the filter material layer is remained in the controlled range, satisfy and stablize the condition of possessing biomass system in, but stable system treatment effect namely.
Above embodiment is exemplary embodiment of the present utility model only, is not used in restriction the utility model, and protection domain of the present utility model is defined by the claims.Those skilled in the art can make various modifications or be equal to replacement the utility model in essence of the present utility model and protection domain, this modification or be equal to replacement and also should be considered as dropping in the protection domain of the present utility model.
Claims (10)
1. internal circulation biological filter reactor, comprise: tank body, be filled with filtrate in the tank body, tank body top is provided with the Graceful mouth of a river, vertically be provided with the center water inlet pipe in the tank body, the bottom of described center water inlet pipe is provided with the filtrate balancing distributing devices, be provided with the center extraction pipe in the water inlet pipe of center, it is characterized in that, the two ends of center water inlet pipe are stretched out respectively at the two ends of center extraction pipe, seal between the upper end of described center water inlet pipe and the center extraction pipe, the side of described center water inlet pipe is communicated with the head height pipe, and the side of described head height pipe has water-in, and the upper end of center extraction pipe is stretched in the folded plate type diffuser, the folded plate type diffuser is connected with tank body, the folded plate type diffuser connects blow-off pipe, and described blow-off pipe is positioned at the below at the Graceful mouth of a river, and the bottom is provided with the aeration perforated pipe in the tank body, the backwash inlet pipe stretches in the tank body from the top of tank body, and the lower end of described backwash inlet pipe is positioned at tank body lower part.
2. internal circulation biological filter reactor according to claim 1 is characterized in that, described backwash inlet pipe along between center water inlet pipe and the center extraction pipe to downward-extension, the lower end of center water inlet pipe is stretched out in the lower end of backwash inlet pipe.
3. internal circulation biological filter reactor according to claim 1 is characterized in that, described folded plate type diffuser upper end is connected with tank body is airtight, and the end that blow-off pipe is positioned at the folded plate type diffuser is provided with the filtrate disrupter.
4. internal circulation biological filter reactor according to claim 3, it is characterized in that, the grid hole dividing plate of described filtrate disrupter for arranging around the center extraction pipe forms the filtrate isolated area between described grid hole dividing plate and the center extraction pipe, described blow-off pipe stretches in the filtrate isolated area.
5. internal circulation biological filter reactor according to claim 1 is characterized in that, described tank interior is provided with the clear water bucket, and the described Graceful mouth of a river is located in the clear water bucket.
6. internal circulation biological filter reactor according to claim 1 is characterized in that, described backwash inlet pipe connects air compressor, and the backwash inlet pipe is provided with reducing valve, valve and under meter.
7. internal circulation biological filter reactor according to claim 1 is characterized in that, described aeration perforated pipe connects gas blower by inlet pipe, and inlet pipe is provided with under meter.
8. internal circulation biological filter reactor according to claim 1 is characterized in that, described water-in connects water equipment, is provided with coarse filter and under meter between described water-in and the water equipment.
9. internal circulation biological filter reactor according to claim 1 is characterized in that, described inner tank wall is provided with the end vertebra that supports the filtrate balancing distributing devices and supports.
10. internal circulation biological filter reactor according to claim 1 is characterized in that, described filtrate is spherical haydite or column type active carbon particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204966370U CN202785795U (en) | 2012-09-26 | 2012-09-26 | Internal recycle bio-filter reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012204966370U CN202785795U (en) | 2012-09-26 | 2012-09-26 | Internal recycle bio-filter reactor |
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| Publication Number | Publication Date |
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| CN202785795U true CN202785795U (en) | 2013-03-13 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012204966370U Withdrawn - After Issue CN202785795U (en) | 2012-09-26 | 2012-09-26 | Internal recycle bio-filter reactor |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102849848A (en) * | 2012-09-26 | 2013-01-02 | 北京市环境保护科学研究院 | Inner circulation bio-filter reactor and sewage treatment method |
-
2012
- 2012-09-26 CN CN2012204966370U patent/CN202785795U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102849848A (en) * | 2012-09-26 | 2013-01-02 | 北京市环境保护科学研究院 | Inner circulation bio-filter reactor and sewage treatment method |
| CN102849848B (en) * | 2012-09-26 | 2014-03-05 | 北京市环境保护科学研究院 | Inner circulation bio-filter reactor and sewage treatment method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Yang Zheng Inventor after: Pan Tao Inventor after: Du Yipeng Inventor after: Nie Yongshan Inventor before: Yang Zheng |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: YANG ZHENG TO: YANG ZHENG PAN TAO DU YIPENG NIE YONGSHAN |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20130313 Effective date of abandoning: 20140305 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20130313 Effective date of abandoning: 20140305 |
|
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |