CN205258121U - A aeration equipment that is used for high concentration suspended solid submergence formula membrane module - Google Patents

A aeration equipment that is used for high concentration suspended solid submergence formula membrane module Download PDF

Info

Publication number
CN205258121U
CN205258121U CN201521006342.0U CN201521006342U CN205258121U CN 205258121 U CN205258121 U CN 205258121U CN 201521006342 U CN201521006342 U CN 201521006342U CN 205258121 U CN205258121 U CN 205258121U
Authority
CN
China
Prior art keywords
membrane module
membrane
high concentration
film
aerator
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.)
Active
Application number
CN201521006342.0U
Other languages
Chinese (zh)
Inventor
董俊
刘鲁建
覃将伟
刘卫勇
熊蔚
方潇
张双峰
陈亮
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Junji Environmental Technology Co.,Ltd.
Original Assignee
Hubei Junji Water Treatment Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hubei Junji Water Treatment Co Ltd filed Critical Hubei Junji Water Treatment Co Ltd
Priority to CN201521006342.0U priority Critical patent/CN205258121U/en
Application granted granted Critical
Publication of CN205258121U publication Critical patent/CN205258121U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

The utility model discloses an aeration equipment that is used for high concentration suspended solid submergence formula membrane module, including membrane module, membrane curtain, membrane silk, membrane mounting system, membrane product water pipe and aeration pipeline, the membrane curtain is formed by a plurality of membrane silk parallel arrangement, and the membrane module comprises the membrane curtain of multiunit parallel arrangement on membrane mounting system, it produces water pipe and aeration pipeline to be provided with the membrane in the membrane module, the aeration pipeline comprises membrane module air supply header, membrane module air feed branch pipe, perforated aeration tube, and blast main and external blower connection, the other end and membrane module air feed branch connection are passed through to membrane module air supply header one end, membrane module air feed branch pipe is a reversion siphunculus, and even parallel expert has met a plurality of perforated aeration tube among them, perforated aeration tube and membrane module air feed branch pipe are fixed to be set up on membrane support membrane mounting system. The utility model discloses simple structure easily makes, and low in manufacturing cost can be applied to the hollow fiber membrane water separation system of high concentration suspended solid.

Description

A kind of aerator for high concentration suspended matter immersion type membrane component
Technical field
The utility model belongs to technical field of sewage, particularly relates to a kind of aerator for high concentration suspended matter immersion type membrane component.
Background technology
In the submerged membrane system of disposing of sewage, sewage is provided to many employings perforated pipe of disturbance and aeration oxygen replenishing, the membrane module bottom adopting in tradition MBR membrane bioreactor generally also adopts perforated pipe aerating regulation, and most of gas stirs for muddy water, and small part is for increasing oxygen in water.
Because flco in activated sludge is little, when stirring, easily to break up, density is light, and sludge concentration is below 20000mg/L, and suitable approximately 8000mg/L, has exceeded 30000mg/L, and mud is dense thick without the concentrated property of precipitation, is difficult to improve and realizes in submerged membrane treatment system. So the design aeration mode of existing membrane module is applicable to biochemical process, tolerance with gas-water ratio 12:1 compared with core, the about 6h of hydraulic detention time.
The range of application of submerged ultrafiltration has had further expansion at present, conventional membrane bioreactor and water treatment field are not limited to, processing water and suspension characteristic for immersion type membrane component are necessary specific aim optimization aeration mode, meet the requirement of membrane module under different operating condition. Penetration hole diameter 5 ~ the 7mm of tradition aeration perforated pipe, spacing 100mm, arrange from film curtain away from, mainly utilize gas duck in drink rise form backwater effect, drive current rise, utilize between ascending current and film silk and rub, reach the wiping of suspension of film silk surface adhesion, realize the effect that film silk superficial layer upgrades. In the time processing low concentration suspension, because concentration of suspension is low, density is light, the water velocity that air pocket drives just can meet the demands, and also can slow down film silk two ends and middle fixed position and assemble bulk suspension;
But under new condition, immersion type membrane component more than high concentration suspended matter 30g/L, the concentration of suspension is higher, between suspension, there is self-adhesive, density is larger, settling rate is fast, in separation muddy water process, film silk outer surface concentration of suspension is higher, more easily between film silk outer surface and film silk, form high concentration region, time one is long, in situation that disturbance is not enough, between film silk, high concentration suspended matter district concentration of suspension can be more long-pending higher, and moisture content is more and more lower, assembles bulk mud and the middle bad phenomenon that forms bulk mud pie of film silk thereby formed film silk two ends. This phenomenon is mainly because the disturbance deficiency of air-flow and current causes, there is no the feature for concentration of suspension raises between film silk in mud-water separation process, therefore need to be for high concentration suspended matter submerged membrane separation assembly, strengthen targetedly disturbance and the scouring intensity of film, prevent two ends and film silk staging bulk mud pie.
Utility model content
Task of the present utility model is the aerator of the hollow-fibre membrane water separating system that a kind of high concentration suspended matter is provided, mainly solve in high concentration suspended matter the fixing film silk surface erosion disturbance of film curtain on membrane module bad, the concentrated piece that is easily bonded to of film silk two ends and middle suspension, reduce the flux of membrane filtration system, to solve on traditional aeration tube the number of openings, aperture, arrangement and the unmatched phenomenon of Process operating parameters.
The technical scheme that the utility model adopts is: a kind of aerator for high concentration suspended matter immersion type membrane component, comprises membrane module, film curtain, film silk, membrane module support, film water producing pipe and aerating pipelines; Described film curtain is be arranged in parallel and is formed by some film silks, and described membrane module is made up of the many groups of film curtains that are set in parallel on membrane module support; In described membrane module, be provided with film water producing pipe and aerating pipelines;
It is characterized in that: described aerating pipelines is made up of membrane module air supply header, membrane module gas manifold, boring aeration pipe, described membrane module air supply header one end is connected with extraneous air blast by blast main, and the other end is connected with described membrane module gas manifold; Described membrane module gas manifold is a reversion siphunculus, even parallel some boring aeration pipes that connected in the middle of it; Described boring aeration pipe and membrane module gas manifold are fixedly installed on described membrane module support.
As preferably, described boring aeration pipe is the foraminate pipeline of distribution that adopts duroplasts pvc material to make, and it is by the even gas distribution of membrane module gas manifold.
As preferably, described membrane module support adopts rigidity hard wire rod to make.
As preferably, described aerating pipelines is arranged on aeration tube support, and described aeration tube support is connected with four pin of membrane module support, squarely circle.
As preferably, described boring aeration pipe opening diameter is 2.5mm, pitch of holes 50mm, and angle is downward 45 ° of level.
As preferably, between described boring aeration pipe and film curtain, level interval is 15 ~ 40mm, is 100mm ~ 150mm from spacing at the bottom of pond.
As preferably, the single aperture of described boring aeration pipe aeration speed is 10 ~ 15m/s.
As preferably, on described membrane module air supply header, dispose valve, for adjusting aeration tolerance size.
Aerator of the present utility model, has advantage simple in structure, with low cost, convenient to use, and has improved membrane module inner membrance silk surface disturbance, has avoided the problem of film curtain two ends and middle suspension caking; Can be applicable to the Middle hollow fiber membrane water system of high concentration suspended matter.
Brief description of the drawings
The structural representation of Fig. 1 the utility model embodiment
The aerating pipelines structural representation of Fig. 2 the utility model embodiment;
The aerating pipelines upward view of Fig. 3 the utility model embodiment;
The boring aeration pipe upward view of Fig. 4 the utility model embodiment;
The boring aeration pipe side view of Fig. 5 the utility model embodiment.
Detailed description of the invention
Understand and enforcement the utility model for the ease of those of ordinary skill in the art, below in conjunction with drawings and Examples, the utility model is described in further detail, should be appreciated that exemplifying embodiment described herein is only for description and interpretation the utility model, and be not used in restriction the utility model.
Ask for an interview Fig. 1, Fig. 2, Fig. 3, Fig. 4 and Fig. 5, a kind of aerator for high concentration suspended matter immersion type membrane component that the utility model provides, comprises membrane module 1, film curtain 2, film silk 3, membrane module support 7, film water producing pipe and aerating pipelines; Film curtain 2 is be arranged in parallel and is formed by some film silks 3, and membrane module 1 is made up of the many groups of film curtains 2 that are set in parallel on membrane module support 7; In membrane module 1, be provided with film water producing pipe and aerating pipelines; Aerating pipelines is made up of membrane module air supply header 4, membrane module gas manifold 5, boring aeration pipe 6, and membrane module air supply header 4 one end are connected (low-pressure air of sending here) with extraneous air blast by blast main 9, and the other end is connected with membrane module gas manifold 5; Membrane module gas manifold 5 is a reversion siphunculus, even parallel some boring aeration pipes 6 that connected in the middle of it.
Air supply header 4 is provided with opening/shutting valve 8 and is connected with blast main 9 with fast joint, so that membrane module 1 sling after off-line tracheae and water pipe in easy disassembly pipeline while rinsing, air supply header 4 connects membrane module gas manifold 5 vertically downward, membrane module gas manifold 5 is that polyvinyl chloride material is with horizontal annular configuration, maintain membrane module gas manifold 5 internal gas pressures identical, membrane module gas manifold 5 connects boring aeration pipe 6 by threeway again, boring aeration pipe 6 can adopt polyvinyl chloride material equally, stick with glue agent gluing fixing, boring aeration pipe 6 is the rear electric drill perforation of spacing and aperture line on request first, opening diameter is 2.5mm, pitch of holes 50mm, angle is downward 45 ° of level, afterwards according to the position of film curtain 2 in membrane module 1, determine the horizontal range 25mm of boring aeration pipe 6 and film curtain 2, 2 boring aeration pipes 6 of every a line film curtain configuration, membrane module gas manifold 5 is the combination of order autotype with boring aeration pipe 6 and arranges. again boring aeration pipe 6 and membrane module gas manifold 5 are fixed on membrane module support 7. boring aeration pipe 6 is from 150mm at the bottom of pond.
Although this description has more used the terms such as membrane module 1, film curtain 2, film silk 3, membrane module air supply header 4, membrane module gas manifold 5, boring aeration pipe 6, membrane module support 7, valve 8, blast main 9, film water producing pipe, aerating pipelines, do not get rid of the possibility that uses other terms. Use these terms to be only used to describe more easily essence of the present utility model, they are construed to any additional restriction is all contrary with the utility model spirit.
Should be understood that, the part that this description does not elaborate all belongs to prior art.
Should be understood that; the above-mentioned description for preferred embodiment is comparatively detailed; can not therefore think the restriction to the utility model scope of patent protection; those of ordinary skill in the art is under enlightenment of the present utility model; do not departing from the scope situation that the utility model claim protects; can also make and replacing or distortion, within all falling into protection domain of the present utility model, request protection domain of the present utility model should be as the criterion with claims.

Claims (8)

1. for an aerator for high concentration suspended matter immersion type membrane component, comprise membrane module (1), film curtain (2), film silk (3), membrane module support (7), film water producing pipe and aerating pipelines; Described film curtain (2) is be arranged in parallel and is formed by some film silks (3), and described membrane module (1) is made up of the many groups of film curtains (2) that are set in parallel on membrane module support (7); Described membrane module is provided with film water producing pipe and aerating pipelines in (1);
It is characterized in that: described aerating pipelines is made up of membrane module air supply header (4), membrane module gas manifold (5), boring aeration pipe (6), described membrane module air supply header (4) one end is connected with extraneous air blast by blast main (9), and the other end is connected with described membrane module gas manifold (5); Described membrane module gas manifold (5) is a reversion siphunculus, the even parallel some boring aeration pipes (6) that connected in the middle of it; Described boring aeration pipe (6) and membrane module gas manifold (5) are fixedly installed on described membrane module support (7).
2. the aerator for high concentration suspended matter immersion type membrane component according to claim 1, it is characterized in that: the distribution foraminate pipeline of described boring aeration pipe (6) for adopting duroplasts pvc material to make, it is by evenly gas distribution of membrane module gas manifold (5).
3. the aerator for high concentration suspended matter immersion type membrane component according to claim 1, is characterized in that: described membrane module support (7) adopts rigidity hard wire rod to make.
4. the aerator for high concentration suspended matter immersion type membrane component according to claim 1, is characterized in that: described aerating pipelines is arranged on aeration tube support, and described aeration tube support is connected with four pin of membrane module support (7), squarely circle.
5. the aerator for high concentration suspended matter immersion type membrane component according to claim 1, is characterized in that: described boring aeration pipe (6) opening diameter is 2.5mm, pitch of holes 50mm, and angle is downward 45 ° of level.
6. the aerator for high concentration suspended matter immersion type membrane component according to claim 1, is characterized in that: between described boring aeration pipe (6) and film curtain (2), level interval is 15 ~ 40mm, is 100mm ~ 150mm from spacing at the bottom of pond.
7. according to the aerator for high concentration suspended matter immersion type membrane component described in claim 1-6 any one, it is characterized in that: the single aperture of described boring aeration pipe (6) aeration speed is 10 ~ 15m/s.
8. according to the aerator for high concentration suspended matter immersion type membrane component described in claim 1-6 any one, it is characterized in that: on described membrane module air supply header (4), dispose valve (8), for adjusting aeration tolerance size.
CN201521006342.0U 2015-11-27 2015-11-27 A aeration equipment that is used for high concentration suspended solid submergence formula membrane module Active CN205258121U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201521006342.0U CN205258121U (en) 2015-11-27 2015-11-27 A aeration equipment that is used for high concentration suspended solid submergence formula membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201521006342.0U CN205258121U (en) 2015-11-27 2015-11-27 A aeration equipment that is used for high concentration suspended solid submergence formula membrane module

Publications (1)

Publication Number Publication Date
CN205258121U true CN205258121U (en) 2016-05-25

Family

ID=55999660

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201521006342.0U Active CN205258121U (en) 2015-11-27 2015-11-27 A aeration equipment that is used for high concentration suspended solid submergence formula membrane module

Country Status (1)

Country Link
CN (1) CN205258121U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105293687A (en) * 2015-11-27 2016-02-03 湖北君集水处理有限公司 Aeration device for high-concentration suspended matter submerged membrane component

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105293687A (en) * 2015-11-27 2016-02-03 湖北君集水处理有限公司 Aeration device for high-concentration suspended matter submerged membrane component

Similar Documents

Publication Publication Date Title
CN106277324B (en) Water treatment device for removing total nitrogen
CN109928488B (en) River aeration membrane assembly, aeration membrane system and method
CN104474912B (en) Hollow fiber tube and aeration oxygenation device formed by hollow fiber tube
CN207121467U (en) Spliced curtain type film assembly
CN205258121U (en) A aeration equipment that is used for high concentration suspended solid submergence formula membrane module
CN206396002U (en) A kind of biological film sewage treatment system
CN105293687A (en) Aeration device for high-concentration suspended matter submerged membrane component
CN204022559U (en) Island sewage integrated treatment device
CN202246234U (en) Cylindrical biological contact oxidation reactor for hollow porous fiber packing
CN101830607B (en) Alternate two-stage aerobic membrane bioreactor
CN207259229U (en) A kind of automatic aeration system for membrane bioreactor
CN207537304U (en) A kind of biology sewage treatment equipment
CN106976972B (en) Bioreactor
CN105884131A (en) Double-membrane integrated intelligent biological sewage treatment system
CN105344251A (en) Double-layer flat membrane module
CN105289060B (en) Horizontal type filter device for sea water desalination
CN205313204U (en) Multistage compound moving bed biofilm reactor MC -MBBR's aeration systems
CN203683213U (en) Fixed tube micropore aerator
CN212068362U (en) Plug-in curtain type membrane device and plug-in curtain type membrane equipment
CN204824377U (en) Mounting structure of aerator
CN210367126U (en) Algae-like biomembrane processing device
CN203990321U (en) A kind of high filling density hollow fiber film assembly and film unit
CN205023940U (en) Hang chain micropore aeration device
CN205569851U (en) Seawater desalination uses horizontal filter for installation
CN201684546U (en) Immersed hollow filament membrane filtering device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CP01 Change in the name or title of a patent holder

Address after: 430000, No.3, Huangjiahu University Town, Hongshan District, Wuhan City, Hubei Province

Patentee after: Junji Environmental Technology Co.,Ltd.

Address before: 430000, No.3, Huangjiahu University Town, Hongshan District, Wuhan City, Hubei Province

Patentee before: HUBEI JUNJI WATER TREATMENT Co.,Ltd.

CP01 Change in the name or title of a patent holder