CN109574406A - A kind of MBR integration biochemical treatment equipment - Google Patents
A kind of MBR integration biochemical treatment equipment Download PDFInfo
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- CN109574406A CN109574406A CN201811645143.2A CN201811645143A CN109574406A CN 109574406 A CN109574406 A CN 109574406A CN 201811645143 A CN201811645143 A CN 201811645143A CN 109574406 A CN109574406 A CN 109574406A
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- zone
- anaerobic
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- anaerobic zone
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/301—Aerobic and anaerobic treatment in the same reactor
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/308—Biological phosphorus removal
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- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The invention discloses a kind of MBR integration biochemical treatment equipments, are used for field of waste water treatment, including anaerobic zone, and anaerobic zone is equipped with intake tunnel；Anoxic zone, anoxic zone are located at the top of anaerobic zone, and anoxic zone is connected with anaerobic zone by the first water passage；Aerobic zone, aerobic zone are located at the top of anaerobic zone, and aerobic zone is connected with anaerobic zone by the second water passage, and aerator is equipped in aerobic zone；MBR membrane module, MBR membrane module are located in aerobic zone, and MBR membrane module is connect by water producing pipe with water pump is produced；Anaerobic zone, anoxic zone and aerobic zone set gradually to form vertical structure from bottom to top.This equipment sets gradually to form vertical structure from bottom to top, have occupied area it is small, integrated height, can modularization, equipmentization, commercialization, improve reaction speed, solution low efficiency and raising Nitrogen/Phosphorus Removal the advantages that.
Description
Technical field
The present invention is used for field of waste water treatment, equips more particularly to a kind of MBR integration biochemical treatment.
Background technique
Traditional biochemical treatment system is this setup tool in such a way that anaerobism, aerobic and precipitating are independently separated
It takes up a large area, pipeline linking is more, the disadvantages for the treatment of effeciency is not high.
Summary of the invention
It is an object of the invention at least solve one of the technical problems existing in the prior art, a kind of MBR one is provided
Metaplasia processing equipment, integrated height small with occupied area, can modularization, equipmentization, commercialization, improve reaction speed,
The advantages that solving low efficiency and improving Nitrogen/Phosphorus Removal.
The technical solution adopted by the present invention to solve the technical problems is: a kind of MBR integration biochemical treatment equipment, including
Anaerobic zone, anaerobic zone are equipped with intake tunnel；
Anoxic zone, anoxic zone are located at the top of anaerobic zone, and anoxic zone is connected with anaerobic zone by the first water passage；
Aerobic zone, aerobic zone are located at the top of anaerobic zone, and aerobic zone is connected with anaerobic zone by the second water passage, aerobic zone
In be equipped with aerator；
MBR membrane module, MBR membrane module are located in aerobic zone, and MBR membrane module is connect by water producing pipe with water pump is produced；
Anaerobic zone, anoxic zone and aerobic zone set gradually to form vertical structure from bottom to top.
It is further used as the improvement of technical solution of the present invention, further includes Impulsive tank, and Impulsive tank connects water inlet pipe, and Impulsive tank is logical
Extra pulse pipe accesses anaerobic zone bottom, and pulse tube forms intake tunnel.
It is further used as the improvement of technical solution of the present invention, and anaerobic zone and anoxic zone are separated by first partition, first every
Plate is equipped with the first water hole and forms the first water passage, and anaerobic zone bottom is equipped with evacuation port.
It is further used as the improvement of technical solution of the present invention, and three phase separation inclined plate is equipped at the top of anaerobic zone, and three phase separation is oblique
Anaerobism gas collecting tube is connected at the top of plate, anaerobism gas collecting tube connects anaerobism exhaust pipe.
It is further used as the improvement of technical solution of the present invention, and anoxic zone bottom is equipped with boring aeration pipe, aerobic zone and anoxic
Area is separated by second partition, and second partition is equipped with the second water hole and forms the second water passage.
It is further used as the improvement of technical solution of the present invention, and aerobic zone is equipped with sludge pipe.
It is further used as the improvement of technical solution of the present invention, and water producing pipe is equipped with negative pressure gauge and produces water ga(u)ge.
It is further used as the improvement of technical solution of the present invention, and anaerobic zone bottom is equipped with evacuation port.
It is further used as the improvement of technical solution of the present invention, and anaerobic zone and anoxic zone are equipped with inspection hole.
A technical solution in above-mentioned technical proposal at least has the following advantages that or one of beneficial effect: water treatment procedure
In, sewage through intake tunnel enter MBR integration biochemical treatment equip, then from bottom to top successively by anaerobic zone, anoxic zone,
Aerobic zone, using water pump is produced, the mode of negative pressure is by the water outlet in aerobic zone by the filtering water outlet of MBR membrane module, and wherein anaerobism, lacks
The functions and effects of removal organic cod, BOD etc. are played in oxygen, the combination of aerobic MBR, have the characteristics of effect is high, excellent in efficiency；
This equipment sets gradually to form vertical structure from bottom to top, have occupied area it is small, integrated height, can modularization, equipmentization, production
Product, the advantages that improving reaction speed, solve low efficiency and improve Nitrogen/Phosphorus Removal.
Detailed description of the invention
The present invention will be further explained below with reference to the attached drawings:
Fig. 1 is one embodiment of the invention structural schematic diagram.
Specific embodiment
This part will be described in specific embodiments of the present invention, and the preferred embodiments of the invention is shown in the accompanying drawings, attached
The effect of figure be with figure remark additionally book word segment description, enable a person to intuitively, visually understand of the invention
Each technical characteristic and overall technical architecture, but it should not be understood as limiting the scope of the invention.
In the present invention, when if there is being described to direction (upper and lower, left and right, before and after), be merely for convenience of description this
The technical solution of invention, rather than the technical characteristic of indication or suggestion meaning must have a particular orientation, with specific orientation
Construction and operation, therefore be not considered as limiting the invention.
In the present invention, " several " are meant that one or more, " being greater than ", " small the meaning of " plurality " is two or more
In ", " being more than " etc. be interpreted as not including this number；" more than ", " following ", " within " etc. be interpreted as including this number.Of the invention
In description, if there is being described to " first ", " second " be only used for for the purpose of distinguishing technical characteristic, and should not be understood as instruction or dark
Show relative importance or implicitly indicates the quantity of indicated technical characteristic or implicitly indicate indicated technical characteristic
Precedence relationship.
In the present invention, unless otherwise restricted clearly, the words such as " setting ", " installation ", " connection " be shall be understood in a broad sense, example
Such as, it can be directly connected, it can also be indirectly connected through an intermediary；It may be a fixed connection, be also possible to detachably connect
It connects, can also be integrated molding；It can be mechanical connection, be also possible to be electrically connected or can communicate with each other；It can be two members
The interaction relationship of connection or two elements inside part.Skilled artisan can be with the tool of combination technology scheme
Hold in vivo and rationally determines the concrete meaning of above-mentioned word in the present invention.
Referring to Fig. 1, the embodiment provides a kind of MBR integration biochemical treatment equipments, including
Anaerobic zone 1, anaerobic zone 1 are equipped with intake tunnel；
Anoxic zone 2, anoxic zone 2 are located at 1 top of anaerobic zone, and anoxic zone 2 is connected with anaerobic zone 1 by the first water passage；
Aerobic zone 3, aerobic zone 3 are located at 1 top of anaerobic zone, and aerobic zone 3 is connected with anaerobic zone 1 by the second water passage,
Aerator 31 is equipped in aerobic zone 3；
MBR membrane module 41, MBR membrane module 41 are located in aerobic zone 3, and MBR membrane module 41 is by water producing pipe 42 and produces water pump
43 connections；
Anaerobic zone 1, anoxic zone 2 and aerobic zone 3 set gradually to form vertical structure from bottom to top.
Wherein, MBR is also known as membrane bioreactor (Membrane Bio-Reactor), in water treatment procedure, sewage pass through into
Aquaporin enters MBR integration biochemical treatment equipment, then from bottom to top successively by anaerobic zone 1, anoxic zone 2, aerobic zone 3,
Using water pump 43 is produced, the mode of negative pressure is by the water outlet in aerobic zone 3 by the filtering water outlet of MBR membrane module 41, and wherein anaerobism, lacks
The functions and effects of removal organic cod, BOD etc. are played in oxygen, the combination of aerobic MBR, have the characteristics of effect is high, excellent in efficiency；
Moreover, the water outlet in aerobic zone 3 can be directly discharged by MBR membrane module 41, it is possible to reduce settling zone improves treatment effeciency,
The advantages that reducing height limitation.This equipment sets gradually to form vertical structure from bottom to top, has occupied area small, integrated
Height, can modularization, equipmentization, commercialization, improve reaction speed, solve low efficiency and improve Nitrogen/Phosphorus Removal the advantages that.MBR
Membrane module 41 has the microorganism fungus kind in retention reactor, improves microbial degradation efficiency, has and leads applied to advanced treating
The technology in domain.
In certain embodiments, water hole, excessively water pipe etc. can be used in the first water passage, the second water passage.
It in certain embodiments, further include Impulsive tank 51, Impulsive tank 51 connects water inlet pipe 52, and Impulsive tank 51 passes through pulse tube
53 access 1 bottoms of anaerobic zone, pulse tube 53 form intake tunnel, and pulse tube 53 forms intake tunnel, and Impulsive tank 51 plays picking-up
The disadvantages of effect of 1 sludge blanket of anaerobic zone solves traditional anaerobic pond sludge and is easy to sink to the bottom, inefficient.
In certain embodiments, anaerobic zone 1 and anoxic zone 2 are separated by first partition 61, and first partition 61 is equipped with the
One water hole 62 forms the first water passage, the first water hole 62 uniform or non-uniform Distribution in first partition 61, as excellent
Choosing, the first water hole 62 first partition 61 periphery be uniformly distributed in a ring, wherein the water outlet of anaerobic zone 1 by first every
The first water hole 62 being arranged in plate 61 rises to anoxic zone 2.1 bottom of anaerobic zone is equipped with evacuation port 11, and evacuation port 11 can be arranged
Water in empty whole equipment.
In certain embodiments, at the top of anaerobic zone 1 be equipped with three phase separation inclined plate 12, separation anaerobic sludge, anaerobic effluent and
Gas, after three phase separation inclined plate 12 separates, the water outlet of anaerobic zone 1 rises by the first water hole 62 being arranged in first partition 61
To anoxic zone 2, anaerobism gas collecting tube 13 is connected at the top of three phase separation inclined plate 12, anaerobism gas collecting tube 13 connects anaerobism exhaust pipe 14, point
Gas from generation passes through anaerobism gas collecting tube 13,14 device for transferring of anaerobism exhaust pipe.
In certain embodiments, 2 bottom of anoxic zone is equipped with boring aeration pipe 21, and in 2 lower end of anoxic zone, anoxic zone 2 is passed through
After 21 aeration aerating of boring aeration pipe, into aerobic zone 3, the micro-hole aerator high using oxygen-transfer efficiency of aerobic zone 3 is improved aerobic
Growth efficiency improves degradation rate.
In certain embodiments, aerobic zone 3 and anoxic zone 2 are separated by second partition 63, and second partition 63 is equipped with the
Two water holes 64 form the second water passage.Second water hole 64 uniform or non-uniform Distribution on second partition 63, as excellent
Choosing, the second water hole 64 are uniformly distributed in a ring in the periphery of second partition 63.Aerobic zone 3 is in 2 upper end of anoxic zone, anoxic zone 2
After perforated pipe aerating regulation is oxygenated, the water outlet of anoxic zone 2 rises to by the second water hole 64 being arranged in second partition 63
Oxygen area 3, the micro-hole aerator high using oxygen-transfer efficiency of aerobic zone 3, improves aerobic growth efficiency, improves degradation rate.
In certain embodiments, aerobic zone 3 is equipped with sludge pipe 32, for the sludge generated in water treatment procedure to be discharged.
In certain embodiments, water producing pipe 42 is equipped with negative pressure gauge 44 and produces water ga(u)ge 45, produces water for detecting
The negative pressure pressure and water yield of pipe 42.
In certain embodiments, anaerobic zone 1 and anoxic zone 2 are equipped with inspection hole 65.
Certainly, the invention is not limited to above embodiment, and those skilled in the art are without prejudice to originally
Equivalent deformation or replacement can be also made under the premise of spirit, these equivalent variation or replacement are all contained in the application right
It is required that in limited range.
Claims (8)
1. a kind of MBR integration biochemical treatment equipment, it is characterised in that: including
Anaerobic zone, anaerobic zone are equipped with intake tunnel；
Anoxic zone, anoxic zone are located at the top of anaerobic zone, and anoxic zone is connected with anaerobic zone by the first water passage；
Aerobic zone, aerobic zone are located at the top of anaerobic zone, and aerobic zone is connected by the second water passage with anaerobic zone, set in aerobic zone
There is aerator；
MBR membrane module, MBR membrane module are located in aerobic zone, and MBR membrane module is connect by water producing pipe with water pump is produced；
Anaerobic zone, anoxic zone and aerobic zone set gradually to form vertical structure from bottom to top.
2. MBR integration biochemical treatment equipment according to claim 1, it is characterised in that: further include Impulsive tank, Impulsive tank
Water inlet pipe is connected, Impulsive tank accesses anaerobic zone bottom by pulse tube, and pulse tube forms intake tunnel.
3. MBR integration biochemical treatment equipment according to claim 1 or 2, it is characterised in that: anaerobic zone and anoxic zone are logical
It crosses first partition to separate, first partition is equipped with the first water hole and forms the first water passage, and anaerobic zone bottom is equipped with evacuation port.
4. MBR integration biochemical treatment equipment according to claim 3, it is characterised in that: be equipped with three-phase at the top of anaerobic zone
Separating inclined plate, three phase separation inclined plate top connect anaerobism gas collecting tube, and anaerobism gas collecting tube connects anaerobism exhaust pipe.
5. MBR integration biochemical treatment equipment according to claim 1, it is characterised in that: anoxic zone bottom is equipped with perforation
Aeration tube, aerobic zone and anoxic zone are separated by second partition, and second partition is crossed water equipped with the second water hole formation second and led to
Road.
6. MBR integration biochemical treatment equipment according to claim 1, it is characterised in that: aerobic zone is equipped with sludge pipe.
7. MBR integration biochemical treatment equipment according to claim 1, it is characterised in that: water producing pipe is equipped with negative pressure pressure
Power table and production water ga(u)ge.
8. MBR integration biochemical treatment equipment according to claim 1, it is characterised in that: set on anaerobic zone and anoxic zone
There is inspection hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811645143.2A CN109574406A (en) | 2018-12-30 | 2018-12-30 | A kind of MBR integration biochemical treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811645143.2A CN109574406A (en) | 2018-12-30 | 2018-12-30 | A kind of MBR integration biochemical treatment equipment |
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| Publication Number | Publication Date |
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| CN109574406A true CN109574406A (en) | 2019-04-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201811645143.2A Pending CN109574406A (en) | 2018-12-30 | 2018-12-30 | A kind of MBR integration biochemical treatment equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112919629A (en) * | 2021-01-21 | 2021-06-08 | 广东酌希生态环境科技有限公司 | Domestic sewage integration treatment facility |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203187461U (en) * | 2013-04-08 | 2013-09-11 | 中国水电顾问集团贵阳勘测设计研究院 | Integrated denitrification membrane bioreactor |
| CN105948258A (en) * | 2016-07-06 | 2016-09-21 | 苏州苏科环保科技有限公司 | High-tower-type A2/O(Anaerobic-Anoxic-Oxic)-MBR (Membrane Bioreactor) |
| CN106242050A (en) * | 2016-07-27 | 2016-12-21 | 广州鹏凯环境科技股份有限公司 | Circular integration sewage disposal device in a kind of vertical low energy consumption |
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2018
- 2018-12-30 CN CN201811645143.2A patent/CN109574406A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203187461U (en) * | 2013-04-08 | 2013-09-11 | 中国水电顾问集团贵阳勘测设计研究院 | Integrated denitrification membrane bioreactor |
| CN105948258A (en) * | 2016-07-06 | 2016-09-21 | 苏州苏科环保科技有限公司 | High-tower-type A2/O(Anaerobic-Anoxic-Oxic)-MBR (Membrane Bioreactor) |
| CN106242050A (en) * | 2016-07-27 | 2016-12-21 | 广州鹏凯环境科技股份有限公司 | Circular integration sewage disposal device in a kind of vertical low energy consumption |
Non-Patent Citations (1)
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112919629A (en) * | 2021-01-21 | 2021-06-08 | 广东酌希生态环境科技有限公司 | Domestic sewage integration treatment facility |
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Address after: 510663 room 602, 601, building 3, No.232 Kezhu Road, Science City, Guangzhou hi tech Industrial Development Zone, Guangdong Province Applicant after: Guangdong Guangshen Environmental Protection Technology Co.,Ltd. Address before: The science city of Guangzhou high tech Development Zone in Guangdong province 510663 Yimin Science Park 3 building 602, 606 Applicant before: GUANGZHOU GUANGSHEN ENVIRONMENTAL SCI-TECH Co.,Ltd. |
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Address after: 510663 room 602, Room 601, building 3, No. 232 Kezhu Road, Science City, Guangzhou high tech Industrial Development Zone, Guangdong Province Applicant after: Guangdong Guangshen Environmental Protection Technology Co.,Ltd. Address before: 510663 room 602, Room 601, building 3, No. 232 Kezhu Road, Science City, Guangzhou high tech Industrial Development Zone, Guangdong Province Applicant before: Guangdong Guangshen Environmental Protection Technology Co.,Ltd. |
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Application publication date: 20190405 |