CN202729953U - Intermission biological reactor (IBR) continuous-flow integration sewage processing device - Google Patents
Intermission biological reactor (IBR) continuous-flow integration sewage processing device Download PDFInfo
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- CN202729953U CN202729953U CN 201220372520 CN201220372520U CN202729953U CN 202729953 U CN202729953 U CN 202729953U CN 201220372520 CN201220372520 CN 201220372520 CN 201220372520 U CN201220372520 U CN 201220372520U CN 202729953 U CN202729953 U CN 202729953U
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- shock wave
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- 239000010865 sewage Substances 0.000 title abstract description 24
- 238000012545 processing Methods 0.000 title abstract description 8
- 230000010354 integration Effects 0.000 title abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000006243 chemical reaction Methods 0.000 claims abstract description 42
- 230000035939 shock Effects 0.000 claims abstract description 19
- 238000005192 partition Methods 0.000 claims abstract description 18
- 238000000746 purification Methods 0.000 claims abstract description 18
- 238000005276 aerator Methods 0.000 claims abstract description 17
- 239000002699 waste material Substances 0.000 claims description 16
- 238000012546 transfer Methods 0.000 claims description 15
- 238000012856 packing Methods 0.000 claims description 7
- 238000000034 method Methods 0.000 abstract description 18
- 230000000694 effects Effects 0.000 abstract description 9
- 206010021143 Hypoxia Diseases 0.000 abstract description 7
- 238000000926 separation method Methods 0.000 abstract description 4
- 230000001146 hypoxic effect Effects 0.000 abstract 1
- 239000013049 sediment Substances 0.000 abstract 1
- 239000010802 sludge Substances 0.000 abstract 1
- 238000010276 construction Methods 0.000 description 6
- 230000007954 hypoxia Effects 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000011499 joint compound Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- -1 organism Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- NHDHVHZZCFYRSB-UHFFFAOYSA-N pyriproxyfen Chemical compound C=1C=CC=NC=1OC(C)COC(C=C1)=CC=C1OC1=CC=CC=C1 NHDHVHZZCFYRSB-UHFFFAOYSA-N 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
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- 239000007921 spray Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Biological Treatment Of Waste Water (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The utility model discloses an intermission biological reactor (IBR) continuous-flow integration sewage processing device. The IBR continuous-flow integration sewage processing device comprises device outer walls which are provided with inner partition walls. The inner partition walls enable a pond body which is formed by surrounding of the device outer walls to be divided into a middle biological reaction area and a water purification separating area. Sinking pumps are arranged in the biological reaction area and connected with shock wave mass transferring jet aerators through connection pipes. Air inlet pipes of the shock wave mass transferring jet aerators are arranged on upper ends of the shock wave mass transferring jet aerators. The biological reaction area is further provided with stirrers. A sludge draining pipe is arranged at the bottom of the biological reaction area. The IBR continuous-flow integration sewage processing device is compact in structure, enables an aerobic reaction process, a hypoxic reaction process, a sediment process and a water purification separation effluent process of sewage treatment to be integrated in a pond body unit structure to be completed, simultaneously achieves continuous uninterrupted operation of water inflowing and outflowing, improves working efficiency, and has obvious effects of being small in occupation space, low in operational cost, and good in processing effect and saving investment.
Description
Technical field
The utility model relates to sewage disposal, relates in particular to IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence (Continuous-flow Intermi ssion Biological Reactor, abbreviation IBR).
Background technology
At sewage treatment area, biological method is the mode of the main flow of present sewage disposal.Technique and the device thereof of realizing the biological process sewage disposal have a lot, no matter it is building coagulation structure, steel construction or other type structure, mostly exist modular construction many, can not continuous flow, invest greatly, the defective such as efficient is low, working cost is high.
Therefore, need to provide IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence to address the above problem.
The utility model content
In order to address this problem, the utility model discloses IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence, described waste disposal plant comprises the device outer wall, in described device outer wall, be provided with internal partition wall, the pond body that described internal partition wall surrounds described device outer wall is separated into bio-reaction zone and the water purification disengaging zone at middle part, be provided with submersible pump on the described internal partition wall in the described bio-reaction zone, the mass transfer by shock wave jet aerator is connected with described submersible pump by pipe connecting, be provided with mass transfer by shock wave jet aerator inlet pipe in the upper end of described mass transfer by shock wave jet aerator, in described bio-reaction zone, also be provided with agitator, also be provided with the mud water shoot in the bottom of described bio-reaction zone.
Preferably, be provided with slip swash plate, air guide plate washer, inclined tube filter packing, water shoot and overflow weir notch in the described water purification disengaging zone, the position that links to each other with described internal partition wall at described slip swash plate offers the long strip type lower mud slot, the position that links to each other with described internal partition wall at described air guide plate washer offers the long strip type air drain, described inclined tube filter packing is arranged on the top of described slip swash plate and described air guide plate washer, offer described water shoot at described device outer wall, described water shoot is connected with described overflow weir notch.
Continuous Flow of the present utility model biological respinse waste disposal plant at integrated intermittence, compact construction, aerobic reaction process, hypoxia response process, precipitation process, the water purification separation exiting water process of sewage disposal are concentrated in the pond body unit structure and finish, realize that simultaneously Inlet and outlet water runs without interruption continuously, improved working efficiency, have occupation of land less, reduced investment, working cost is low, treatment effect is good unusual effect.
Introduced the concept of a series of reduced forms in the utility model content part, this will further describe in the embodiment part.The utility model content part does not also mean that key feature and the essential features that will attempt to limit technical scheme required for protection, does not more mean that the protection domain of attempting to determine technical scheme required for protection.
Below in conjunction with accompanying drawing, describe advantage of the present utility model and feature in detail.
Description of drawings
Fig. 1 is the synoptic diagram according to the Continuous Flow biological respinse waste disposal plant at integrated intermittence of an embodiment of the utility model.
Embodiment
In the following description, having provided a large amount of concrete details understands the utility model more thoroughly in order to provide.Yet, it will be apparent to one skilled in the art that the utility model can need not one or more these details and implemented.In other example, for fear of obscuring with the utility model, be not described for technical characterictics more well known in the art.
In order thoroughly to understand the utility model, detailed structure will be proposed in following description.Obviously, execution of the present utility model is not limited to the specific details that those skilled in the art has the knack of.Preferred embodiment of the present utility model is described in detail as follows, yet except these were described in detail, the utility model can also have other embodiments.
Below in conjunction with accompanying drawing embodiment of the present utility model is described in detail.
With reference to figure 1, it is the synoptic diagram according to the Continuous Flow biological respinse waste disposal plant at integrated intermittence of an embodiment of the utility model.Waste disposal plant of the present utility model can be concrete structure, steel construction or other material and combination construction thereof.Its mounting means can be ground type, and is buried or partly buried.
This waste disposal plant comprises device outer wall 1, and this device outer wall 1 surrounds the main body of waste disposal plant, wherein is used for holding sewage and purifying waste water of processing, and installation is within it equally for required miscellaneous equipment.Be provided with internal partition wall 2 at device in the outer wall 1, it will install bio-reaction zone and water purification disengaging zone (water, mud, gas three-phase separation area) that pond body that outer wall 1 surrounds is separated into the middle part, this water purification disengaging zone be arranged in reaction zone around or both sides or one side.
In bio-reaction zone, be provided with sewage water inlet pipe 11, need sewage to be processed to enter in the bio-reaction zone by this sewage water inlet pipe 11.There is shown sewage level 14.Also be provided with submersible pump 8 on the internal partition wall 2 in this bio-reaction zone, the quantity of submersible pump 8 can arrange as required.Mass transfer by shock wave jet aerator 10 is connected with submersible pump 8 by pipe connecting 9.Also be provided with mass transfer by shock wave jet aerator inlet pipe in the upper end of mass transfer by shock wave jet aerator 10.Also be provided with agitator 12 in bio-reaction zone, its quantity can arrange equally as required.The sewage that agitator 12 stirs in the reaction zone evenly rolls.Its effect will be discussed in more detail below.Also be provided with mud water shoot 13 in order to get rid of mud in the bottom of bio-reaction zone.
In the water purification disengaging zone, be provided with slip swash plate 3, air guide plate washer 4, inclined tube filter packing 5, water shoot 6 and overflow weir notch 7.The position that links to each other with internal partition wall 2 at slip swash plate 3 offers long strip type lower mud slot 22, and the position that links to each other with internal partition wall 2 at air guide plate washer 4 offers long strip type air drain 21.Inclined tube filter packing 5 is arranged on the top of slip swash plate 3 and air guide plate washer 4.Offer water shoot 6 at device outer wall 1, water shoot 6 is connected with overflow weir notch 7.
The working process of waste disposal plant of the present utility model below is described.
Bio-reaction zone is inner to be formed and working process:
The sewage that needs to process enters in the bio-reaction zone from sewage water inlet pipe 11 continually continuously, make the whole liquid level in the device keep stable, thereby and make the processing of water purification disengaging zone by hydraulic pressure after water purification liquid level 15 just overflow across the purpose that overflow weir notch 7 reaches continuous effluent.
The alternately continuously operation of three workflow stages is arranged in the bio-reaction zone:
The aerobic reaction stage: the submersible pump 8 that is installed on the internal partition wall is sucked at a high speed mass transfer by shock wave jet aerator 10 and from top to bottom fast injection with sewage by pipe connecting 9.Because suction function, the air that contains oxygen passes through mass transfer by shock wave jet aerator inlet pipe 101 and sucks, and the cutting of the turbulent flow of the fluid shock in mass transfer by shock wave jet aerator 10 and fusion, thereby reaches the purpose that chops up mud and biological floe and accelerated oxidation.The fluid that contains oxygen sprays at a high speed from mass transfer by shock wave ejector 10 lower ends, wash and drive mud and biological floe constantly rolling in reaction zone of body bottom, pond open, make oxygen, organism, sewage evenly mix, react, mixture is repeated above process continuously by submersible pump 8 continuous suctions again, and this process can reach COD degraded, Ammonia Nitrification, aerobic suction phosphorus texts by biology and chemical reaction.
The hypoxia response stage: according to the program of prior setting, the aerobic reaction stage stops behind the certain hour, and the hypoxia response stage begins.All quit work at this stage submersible pump 8 and mass transfer by shock wave jet aerator 10.The sewage that is installed in the agitator 12 stirring reaction zones in the reaction zone evenly rolls, and this stage mainly reaches COD degraded and the denitrifying purpose of ammonia nitrogen.
The anaerobic reaction stage: the hypoxia response stage enters this stage after stopping by the time of setting, this stage except sewage water inlet pipe 11 still water inlet, miscellaneous equipment such as submersible pump, mass transfer by shock wave jet aerator, agitator etc. all quit work.Sewage in the reaction zone is by gravitational settling, and mud sinks at the bottom of the pond.Still there are COD degraded and phosphor-removing effect in this stage.According to practical situation, unnecessary mud is discharged by mud vent pipe 12.
Aerobic reaction stage, hypoxia response stage, anaerobic reaction stage are in alternately continuously operation of reaction zone.
Water purification disengaging zone (water, mud, gas three-phase separation area) is inner to be formed and working process:
The mixed solution of crossing through biological respinse of bio-reaction zone flows into the water purification disengaging zone by the long strip type air drain 21 on the device internal partition wall 2 and long strip type lower mud slot 22, under the natural sedimentation effect, the bubble of light specific gravity rises, and rises along air guide plate washer 4 times along face and dissolves in the bio-reaction zone by long strip type air drain 21; Mud in the mixed solution is because of than great, and precipitation glides and flows into the bottom of bio-reaction zones by long strip type lower mud slot 22 along slip swash plate 3 downwards; Under Water Pressure, pass through the narrow orifice of slip swash plate 3 and air guide plate washer 4 to the upper reaches through what gas mud separated than clean water, and process inclined tube filter packing 5 further cement filtering separation, at this moment water purification up to standard overflows into overflow weir notch 7 and passes through water shoot 6 discharges after rising to the water purification liquid level through processing layer by layer also.
Three processes of the working process of water purification disengaging zone and bio-reaction zone are carried out simultaneously, so realized the purpose of continuous effluent.
The integrated biological respinse waste disposal plant of having a rest of asking of Continuous Flow of the present utility model, compact construction, aerobic reaction process, hypoxia response process, precipitation process, the water purification separation exiting water process of sewage disposal are concentrated in the pond body unit structure and finish, realize that simultaneously Inlet and outlet water runs without interruption continuously, improved working efficiency, have occupation of land less, reduced investment, working cost is low, treatment effect is good unusual effect.
The utility model is illustrated by above-described embodiment, but should be understood that, above-described embodiment just is used for for example and the purpose of explanation, but not is intended to the utility model is limited in the described scope of embodiments.It will be understood by those skilled in the art that in addition; the utility model is not limited to above-described embodiment; can also make more kinds of variants and modifications according to instruction of the present utility model, these variants and modifications all drop in the utility model scope required for protection.Protection domain of the present utility model is defined by the appended claims and equivalent scope thereof.
Claims (2)
1.IBR Continuous Flow biological respinse waste disposal plant at integrated intermittence, it is characterized in that, described waste disposal plant comprises the device outer wall, in described device outer wall, be provided with internal partition wall, the pond body that described internal partition wall surrounds described device outer wall is separated into bio-reaction zone and the water purification disengaging zone at middle part, be provided with submersible pump on the described internal partition wall in the described bio-reaction zone, the mass transfer by shock wave jet aerator is connected with described submersible pump by pipe connecting, be provided with mass transfer by shock wave jet aerator inlet pipe in the upper end of described mass transfer by shock wave jet aerator, in described bio-reaction zone, also be provided with agitator, also be provided with the mud water shoot in the bottom of described bio-reaction zone.
2. according to Continuous Flow claimed in claim 1 biological respinse waste disposal plant at integrated intermittence, it is characterized in that, described water purification is provided with the slip swash plate in the disengaging zone, the air guide plate washer, the inclined tube filter packing, water shoot and overflow weir notch, the position that links to each other with described internal partition wall at described slip swash plate offers the long strip type lower mud slot, the position that links to each other with described internal partition wall at described air guide plate washer offers the long strip type air drain, described inclined tube filter packing is arranged on the top of described slip swash plate and described air guide plate washer, offer described water shoot at described device outer wall, described water shoot is connected with described overflow weir notch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220372520 CN202729953U (en) | 2012-07-31 | 2012-07-31 | Intermission biological reactor (IBR) continuous-flow integration sewage processing device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220372520 CN202729953U (en) | 2012-07-31 | 2012-07-31 | Intermission biological reactor (IBR) continuous-flow integration sewage processing device |
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| CN202729953U true CN202729953U (en) | 2013-02-13 |
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| CN 201220372520 Expired - Lifetime CN202729953U (en) | 2012-07-31 | 2012-07-31 | Intermission biological reactor (IBR) continuous-flow integration sewage processing device |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150594A (en) * | 2014-07-28 | 2014-11-19 | 武汉芳笛环保股份有限公司 | Floating island precipitation type IBR bioreactor |
| CN104891657A (en) * | 2015-06-08 | 2015-09-09 | 新乡市蓝海环境工程有限公司 | CBR sewage biological treatment device and operating method thereof |
| CN105293701A (en) * | 2015-11-06 | 2016-02-03 | 武汉芳笛环保股份有限公司 | Carbon source reserve type immobilized bioreactor (IBR) |
| CN106186289A (en) * | 2016-08-22 | 2016-12-07 | 上海同济建设科技股份有限公司 | Integration high load capacity aerobic reactor |
| CN112551810A (en) * | 2020-11-19 | 2021-03-26 | 武汉芳笛环保股份有限公司 | Denitrification IBR denitrification and dephosphorization integrated reactor and reaction process thereof |
| CN117164096A (en) * | 2023-10-11 | 2023-12-05 | 武汉芳笛环保股份有限公司 | Sewage advanced treatment contact biochemical reactor |
-
2012
- 2012-07-31 CN CN 201220372520 patent/CN202729953U/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104150594A (en) * | 2014-07-28 | 2014-11-19 | 武汉芳笛环保股份有限公司 | Floating island precipitation type IBR bioreactor |
| CN104150594B (en) * | 2014-07-28 | 2016-09-21 | 武汉芳笛环保股份有限公司 | A kind of chinampa precipitating type IBR bioreactor |
| CN104891657A (en) * | 2015-06-08 | 2015-09-09 | 新乡市蓝海环境工程有限公司 | CBR sewage biological treatment device and operating method thereof |
| CN105293701A (en) * | 2015-11-06 | 2016-02-03 | 武汉芳笛环保股份有限公司 | Carbon source reserve type immobilized bioreactor (IBR) |
| CN105293701B (en) * | 2015-11-06 | 2022-11-01 | 武汉芳笛环保股份有限公司 | Carbon source reserve type IBR bioreactor |
| CN106186289A (en) * | 2016-08-22 | 2016-12-07 | 上海同济建设科技股份有限公司 | Integration high load capacity aerobic reactor |
| CN112551810A (en) * | 2020-11-19 | 2021-03-26 | 武汉芳笛环保股份有限公司 | Denitrification IBR denitrification and dephosphorization integrated reactor and reaction process thereof |
| CN117164096A (en) * | 2023-10-11 | 2023-12-05 | 武汉芳笛环保股份有限公司 | Sewage advanced treatment contact biochemical reactor |
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Denomination of utility model: Intermission biological reactor (IBR) continuous-flow integration sewage processing device Effective date of registration: 20130619 Granted publication date: 20130213 Pledgee: Guanggu Branch of Wuhan Rural Commercial Bank Co.,Ltd. Pledgor: WUHAN FUND ENVIRONMENT PROT ENGINEERING Co.,Ltd. Registration number: 2013990000384 |
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Owner name: WUHAN FUND ENVIRONMENTAL PROTECTION CO., LTD. Free format text: FORMER NAME: WUHAN FUND ENVIRONMENTAL PROTECTION ENGINEERING CO., LTD. |
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Address after: 430000 A2103, Pioneer Street, East Lake Development Zone, Hubei, Wuhan Patentee after: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Address before: 430000 A2103, Pioneer Street, East Lake Development Zone, Hubei, Wuhan Patentee before: WUHAN FUND ENVIRONMENT PROT ENGINEERING Co.,Ltd. |
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Date of cancellation: 20140701 Granted publication date: 20130213 Pledgee: Guanggu Branch of Wuhan Rural Commercial Bank Co.,Ltd. Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2013990000384 |
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Denomination of utility model: Intermission biological reactor (IBR) continuous-flow integration sewage processing device Effective date of registration: 20140928 Granted publication date: 20130213 Pledgee: Bank of Hankou Limited by Share Ltd. Wuchang branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2014980000086 |
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Date of cancellation: 20151023 Granted publication date: 20130213 Pledgee: Bank of Hankou Limited by Share Ltd. Wuchang branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2014980000086 |
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Denomination of utility model: Intermission biological reactor (IBR) continuous-flow integration sewage processing device Effective date of registration: 20180817 Granted publication date: 20130213 Pledgee: Pudong Shanghai Development Bank Limited by Share Ltd. Wuhan branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2018990000703 |
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Date of cancellation: 20231129 Granted publication date: 20130213 Pledgee: Pudong Shanghai Development Bank Limited by Share Ltd. Wuhan branch Pledgor: WUHAN FUND ENVIRONMENT PROTECTION Co.,Ltd. Registration number: 2018990000703 |
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