CN202151549U - Membrane component with center pipe for MBR (membrane bioreactor) - Google Patents

Membrane component with center pipe for MBR (membrane bioreactor) Download PDF

Info

Publication number
CN202151549U
CN202151549U CN2011202252969U CN201120225296U CN202151549U CN 202151549 U CN202151549 U CN 202151549U CN 2011202252969 U CN2011202252969 U CN 2011202252969U CN 201120225296 U CN201120225296 U CN 201120225296U CN 202151549 U CN202151549 U CN 202151549U
Authority
CN
China
Prior art keywords
epoxy
membrane
tube
pipe
mbr
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011202252969U
Other languages
Chinese (zh)
Inventor
任冬伟
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.)
SUZHOU DINGYU WATER TECHNOLOGY CO LTD
Original Assignee
SUZHOU DINGYU WATER TECHNOLOGY 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 SUZHOU DINGYU WATER TECHNOLOGY CO LTD filed Critical SUZHOU DINGYU WATER TECHNOLOGY CO LTD
Priority to CN2011202252969U priority Critical patent/CN202151549U/en
Application granted granted Critical
Publication of CN202151549U publication Critical patent/CN202151549U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

A membrane component with a center pipe for an MBR (membrane bioreactor) comprises hollow fiber membrane wires (2), the center aerator pipe (3), an epoxy plugging pipe sheet (4), an epoxy plugging dead end (5) and a porous outer pipe (6). The hollow fiber membrane wires (2) are mounted in the porous outer pipe (6) through the epoxy plugging pipe sheet (4) at one end and the epoxy plugging dead end (5) at the other end, the center aerator pipe (3) is arranged between the two hollow fiber membrane wires (2), and pores are arranged on the porous outer pipe (6). The membrane component has the advantages that the membrane component is simple in installation, convenient in adjustment and durable in use, particularly, gas utilization rate is increased, dissolved oxygen in water is increased, biochemical reaction is benefited, harmful substances in the water can be removed effectively, the stain resistance of a membrane is improved, and flux is stable.

Description

The MBR of band central tube uses membrane module
Technical field
The utility model relates to the novel polysulfone hollow fiber ultrafiltration membrane system of a kind of MBR of being used for system, belongs to sewage treatment area.
Background technology
At present, hollow fiber ultrafiltration membrane is used for that the MBR system is many to be existed with curtain formula kit form, promptly is poured into the two ends of multi beam hollow fibre filament respectively with epoxy and forms so-called curtain formula assembly in two plastic tubes, then this assembly formation module that is together in parallel.There is following shortcoming in this form: film silk root is easily broken, influences effluent quality thereby when aeration, more be prone to fracture of wire; Mostly membrane material is the stronger materials of toughness such as PVDF and PP, and the material of PS or PES excellent performance is owing to easily broken being excluded of silk, material alternative little; Simultaneously, aeration is many to make aeration rate big by the peripheral aeration of aeration tube at the film silk, not enough to the strength of turbulence of water, thereby bad to the cleaning performance of film.
Summary of the invention
The utility model technical problem to be solved provide a kind of have install simply, easy to adjust, durable in use, be prone to the novel polysulfone hollow fiber ultrafiltration membrane system that is used for the MBR system that cleans.
The utility model adopts following technical scheme:
A kind of MBR with central tube uses membrane module; Comprise hollow-fibre membrane silk, center aeration tube, epoxy shutoff tube sheet, epoxy shutoff dead end, porous outer tube; The epoxy shutoff dead end of epoxy shutoff tube sheet and the other end of described hollow-fibre membrane silk through an end is installed in and comprises in the shell; Described center aeration tube is arranged between the two intrafascicular hollow fiber film silks, and described shell is provided with the hole.
The diameter of described center aeration tube is the 1-3 millimeter.
The advantage of the utility model is to have installs simply, easy to adjust, durable in use; Particularly the utilization rate of gas improves, and oxygen in water improves, and helps biochemical reaction; Removal effect for harmful substance in the water is obvious, and the stain resistance of film improves, flux stabilized.
Description of drawings
Fig. 1 is the overall structure sketch map of the utility model.
The specific embodiment
As shown in Figure 1; A kind of MBR with central tube uses membrane module; Comprise hollow-fibre membrane silk 2, center aeration tube 3, epoxy shutoff tube sheet 4, epoxy shutoff dead end 5, porous outer tube 6; Described hollow-fibre membrane silk 2 is installed in the porous outer tube 6 through the epoxy shutoff tube sheet 4 of an end and the epoxy shutoff dead end 5 of the other end, and center aeration tube 3 is arranged between the two intrafascicular hollow fiber film silks 2, and porous outer tube 6 is provided with the hole.The diameter of center aeration tube 3 select for use into the 1-3 millimeter for well.
The utility model is produced according to the manufacturing approach of hollow fiber film assembly; Just porous outer tube 6 is processed to porous, and each assembly middle part all is provided with center aeration tube 3 simultaneously, is hollow-fibre membrane silk 2 around the center aeration tube 3; Gas in the center aeration tube 3 can play stripping and cleaning action to the surface of any hollow-fibre membrane silk 2 like this; Increased the contact probability of gas and water simultaneously, made the dissolved oxygen in water amount increase, the utilization rate of gas improves.The diameter of center aeration tube 3 is advisable with the 1-3 millimeter, the hole size on the porous outer tube 6 with the intensity of not damaging shell for well; All hollow-fibre membrane silks 2 are cast in the porous outer tube 6 after being wrapped up by the plastics protecting wire net, during use, equally assemble the preparation method of these assemblies according to the ultrafiltration module, enter into biochemistry pool to them then and get final product.

Claims (2)

1. the MBR with central tube uses membrane module; It is characterized in that: comprise hollow-fibre membrane silk (2), center aeration tube (3), epoxy shutoff tube sheet (4), epoxy shutoff dead end (5), porous outer tube (6); Described hollow-fibre membrane silk (2) is installed in the porous outer tube (6) through the epoxy shutoff tube sheet (4) of an end and the epoxy shutoff dead end (5) of the other end; Described center aeration tube (3) is arranged between the two intrafascicular hollow fiber film silks (2), and described porous outer tube (6) is provided with the hole.
2. the MBR according to the said band central tube of claim 1 uses membrane module, it is characterized in that: the diameter of described center aeration tube (3) is the 1-3 millimeter.
CN2011202252969U 2011-06-29 2011-06-29 Membrane component with center pipe for MBR (membrane bioreactor) Expired - Fee Related CN202151549U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011202252969U CN202151549U (en) 2011-06-29 2011-06-29 Membrane component with center pipe for MBR (membrane bioreactor)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011202252969U CN202151549U (en) 2011-06-29 2011-06-29 Membrane component with center pipe for MBR (membrane bioreactor)

Publications (1)

Publication Number Publication Date
CN202151549U true CN202151549U (en) 2012-02-29

Family

ID=45692060

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011202252969U Expired - Fee Related CN202151549U (en) 2011-06-29 2011-06-29 Membrane component with center pipe for MBR (membrane bioreactor)

Country Status (1)

Country Link
CN (1) CN202151549U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102847438A (en) * 2011-06-29 2013-01-02 苏州顶裕水务科技有限公司 Membrane module for MBR having central tube

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102847438A (en) * 2011-06-29 2013-01-02 苏州顶裕水务科技有限公司 Membrane module for MBR having central tube

Similar Documents

Publication Publication Date Title
CN205241329U (en) Globular carbon fiber combined packing
CN105413472B (en) A kind of membrane for water treatment component
CN205653224U (en) Bubble -free oxygen aeration ware
CN204039124U (en) A kind of aeration film assembly
CN202151549U (en) Membrane component with center pipe for MBR (membrane bioreactor)
WO2012074222A3 (en) Preparation method of hollow fiber membrane for water treatment using cellulose-based resin
CN103214085A (en) Membrane bioreactor for combining flat membrane and hollow fibrous membrane
CN105129971A (en) Micro-pore aerator
CN202283454U (en) Columnar beam-splitting pulsation type hollow-fiber membrane element
CN202146720U (en) Membrane component used for MBR (membrane biological reactor) and provided with central tube
CN202921177U (en) Hollow fiber membrane module and membrane bioreactor comprising same
CN203123835U (en) Integrated combined aeration curtain membrane component
CN208990576U (en) A kind of novel reverse osmosis membrane end plate
CN205730913U (en) A kind of highly efficient durable hollow fiber film assembly
CN105036315B (en) A kind of aeration hollow fiber film assembly and its connection structure
CN109534496A (en) A kind of bionical aerator of activated sludge and aerating system
CN102847438A (en) Membrane module for MBR having central tube
CN201735337U (en) Hollow fiber ultrafiltration membrane component with improved central catheter structure
CN209778449U (en) Conical wetland tower
CN208265863U (en) A kind of efficient pure oxygen aeration device
CN102849843A (en) Novel membrane assembly with gas nozzle for MBR
CN201684546U (en) Immersed hollow filament membrane filtering device
CN204824325U (en) Aeration hollow fiber membrane subassembly and connection structure thereof
CN201817326U (en) Hollow filter ultrafiltration membrane component for integrated water treatment device
CN204111397U (en) A kind of tubular fibre MBR membrane module

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120229

Termination date: 20180629

CF01 Termination of patent right due to non-payment of annual fee