CN101422698A - Hollow fiber ultrafiltration micro-filtration membrane module - Google Patents

Hollow fiber ultrafiltration micro-filtration membrane module Download PDF

Info

Publication number
CN101422698A
CN101422698A CNA2008101222687A CN200810122268A CN101422698A CN 101422698 A CN101422698 A CN 101422698A CN A2008101222687 A CNA2008101222687 A CN A2008101222687A CN 200810122268 A CN200810122268 A CN 200810122268A CN 101422698 A CN101422698 A CN 101422698A
Authority
CN
China
Prior art keywords
membrane
hollow
water distributor
putamina
yarns
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.)
Granted
Application number
CNA2008101222687A
Other languages
Chinese (zh)
Other versions
CN101422698B (en
Inventor
姚玉章
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN2008101222687A priority Critical patent/CN101422698B/en
Publication of CN101422698A publication Critical patent/CN101422698A/en
Application granted granted Critical
Publication of CN101422698B publication Critical patent/CN101422698B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses a hollow fiber ultra-filtration and micro-filtration membrane component which comprises a membrane shell, a central water distributor provided with a plurality of small orifices and a plurality of hollow fibrous membrane yarns on a lateral wall, the central water distributor is enveloped in the middle of the hollow fibrous membrane yarns, the central water distributor and the hollow fibrous membrane yarns are all fixed inside the membrane shell, material inlets are arranged at the positions of the two ends of the membrane shell that are corresponding to the central water distributor, liquid ports are arranged at the positions at the two ends of the membrane shell that are corresponding to the hollow fibrous membrane yarns, and a plurality of reflux ports are arranged on a lateral wall of the membrane shell. The material inlets and the liquid ports are all arranged at the two ends of the membrane shell, when working, water or material liquid are fed simultaneously at two ends through the central water distributor, water or material liquid can simultaneously penetrate two membrane end faces, thus leading the cross current speed on the membrane surfaces of the hollow fibrous membrane yarns to be capable of obtaining balance, maximization, largest effective filtering membrane area and ultra-easy discharge of intercepted impurities, reducing the resistance on flow paths of the penetrating liquid, and reaching the back washing impulse effect of 100 percent.

Description

The Hollow Fiber Ultrafiltration micro-filtration membrane module
[technical field]
The present invention relates to the membrane separation technique field, relate in particular to Hollow Fiber Ultrafiltration micro-filtration membrane module (group device).
[background technology]
The Hollow Fiber Ultrafiltration micro-filtration membrane module has been widely used in the isolation of purified, grading purification of water purification, sewage turbidity removal, the preliminary treatment of counter-infiltration front end, liquid (solution) and the field such as has concentrated.
Present external-compression type Hollow Fiber Ultrafiltration micro-filtration membrane module structure all is that another brings out through liquid from an endfeed as shown in Figure 1.There is following defective in this structure: one, the face cross flow effects is unbalanced, and operation and when cleaning the membrane module intimal surface exist and clean the dead angle.Two, flush efficiency is lower than 70% during the film backwash, and is easy to generate the doughnut film rupture.
[summary of the invention]
Purpose of the present invention solves the problems of the prior art exactly, proposes a kind of Hollow Fiber Ultrafiltration micro-filtration membrane module, can balanced cross flow effects, and improve backwash efficient, prolong effective service life.
For achieving the above object, the present invention proposes a kind of Hollow Fiber Ultrafiltration micro-filtration membrane module, comprise that putamina, sidewall are provided with center water distributor and some hollow-fibre membrane silks of some apertures, described center water distributor is rolled in the centre of some hollow-fibre membrane silks, described center water distributor and some hollow-fibre membrane silks all are fixed in the putamina, the position of corresponding center, the two ends of described putamina water distributor is equipped with charging aperture, the position of the corresponding hollow-fibre membrane silk in the two ends of described putamina is equipped with through the liquid mouth, and the sidewall of described putamina is provided with some refluxing openings.
As preferably, described charging aperture is arranged on the center of putamina end.
Adopt resin that hollow-fibre membrane silk and center water distributor are solidified together, and be fixed on the two ends of putamina.
As preferably, the quantity of described hollow-fibre membrane silk is 2000 or above/every assembly.
Beneficial effect of the present invention: the present invention all is provided with charging aperture and sees through the liquid mouth at the two ends of putamina, two ends intake or feed liquid simultaneously through the center water distributor during work, two film end faces are permeable or saturating liquid simultaneously, thereby make the film surface cross-flow flow velocity of hollow-fibre membrane silk can obtain equilibrium and maximization, effective membrane area maximum of filtering, the as easy as rolling off a log discharge of the impurity that is trapped reduces to see through the path resistance that liquid flows, and the impulse force effect of backwash simultaneously can reach 100%.
Feature of the present invention and advantage will be elaborated in conjunction with the accompanying drawings by embodiment.
[description of drawings]
Fig. 1 is the structural representation of Hollow Fiber Ultrafiltration micro-filtration membrane module in the prior art;
Fig. 2 is the structural representation of Hollow Fiber Ultrafiltration micro-filtration membrane module of the present invention.
[specific embodiment]
Consult Fig. 2, the Hollow Fiber Ultrafiltration micro-filtration membrane module, comprise putamina 1, sidewall is provided with center water distributor 2 and some hollow-fibre membrane silks 3 of some apertures, described center water distributor 2 is rolled in the centre of some hollow-fibre membrane silks 3, described center water distributor 2 and some hollow-fibre membrane silks 3 all are fixed on the two ends in the putamina 1, the position of corresponding center, the two ends of described putamina 1 water distributor 2 is equipped with charging aperture 4, the position of the corresponding hollow-fibre membrane silk 3 in the two ends of described putamina 1 is equipped with through liquid mouth 5, the sidewall of described putamina 1 is provided with some refluxing openings 6, is generally 1 or 2 refluxing openings 6.Described charging aperture 4 is arranged on the center of putamina 1 end.Adopt resin that hollow-fibre membrane silk 3 and center water distributor 2 are solidified together, and be fixed on the two ends of putamina 1.The quantity of described hollow-fibre membrane silk 3 is 2000 or above/every assembly.
Charging aperture 4 all is set at the two ends of putamina and sees through liquid mouth 5, two ends intake or feed liquid simultaneously through center water distributor 2 during work, and two film end faces can produce water simultaneously, and current or feed liquid flow resistance are little, face pressure reduction stable and consistent.Make the face cross-flow flow velocity of hollow-fibre membrane silk 3 obtain equilibrium, effective membrane area maximum of filtering, the as easy as rolling off a log discharge of the impurity that is trapped, the impulse force effect of backwash reaches 100%.Water that is not filtered or feed liquid two refluxing openings 6 on putamina 1 are discharged simultaneously or are refluxed.
The foregoing description is to explanation of the present invention, is not limitation of the invention, any structure after the simple transformation of the present invention is all belonged to protection scope of the present invention.

Claims (4)

1. Hollow Fiber Ultrafiltration micro-filtration membrane module, comprise putamina (1), sidewall is provided with center water distributor (2) and some hollow-fibre membrane silks (3) of some apertures, described center water distributor (2) is rolled in the centre of some hollow-fibre membrane silks (3), described center water distributor (2) and some hollow-fibre membrane silks (3) all are fixed in the putamina (1), it is characterized in that: the position of the corresponding center water distributors in the two ends of described putamina (1) (2) is equipped with charging aperture (4), the position of the corresponding hollow-fibre membrane silks in the two ends of described putamina (1) (3) is equipped with through liquid mouth (5), and the sidewall of described putamina (1) is provided with some refluxing openings (6).
2. Hollow Fiber Ultrafiltration micro-filtration membrane module as claimed in claim 1 is characterized in that: described charging aperture (4) is arranged on the center of putamina (1) end.
3. Hollow Fiber Ultrafiltration micro-filtration membrane module as claimed in claim 1 or 2 is characterized in that: adopt resin that hollow-fibre membrane silk (3) and center water distributor (2) are solidified together, and be fixed on the two ends of putamina (1).
4. Hollow Fiber Ultrafiltration micro-filtration membrane module as claimed in claim 1 or 2 is characterized in that: the quantity of described hollow-fibre membrane silk (3) be 2000 or more than.
CN2008101222687A 2008-11-06 2008-11-06 Hollow fiber ultrafiltration micro-filtration membrane module Expired - Fee Related CN101422698B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2008101222687A CN101422698B (en) 2008-11-06 2008-11-06 Hollow fiber ultrafiltration micro-filtration membrane module

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2008101222687A CN101422698B (en) 2008-11-06 2008-11-06 Hollow fiber ultrafiltration micro-filtration membrane module

Publications (2)

Publication Number Publication Date
CN101422698A true CN101422698A (en) 2009-05-06
CN101422698B CN101422698B (en) 2011-11-09

Family

ID=40613718

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2008101222687A Expired - Fee Related CN101422698B (en) 2008-11-06 2008-11-06 Hollow fiber ultrafiltration micro-filtration membrane module

Country Status (1)

Country Link
CN (1) CN101422698B (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101862598A (en) * 2010-06-25 2010-10-20 苏州顶裕节能设备有限公司 Hollow fiber ultra-filtration membrane assembly having improved shell structure
CN102489166A (en) * 2011-12-06 2012-06-13 深圳恒通源水处理科技有限公司 Ultrafiltration membrane processing system and processing technology thereof
CN103055700A (en) * 2013-01-30 2013-04-24 高然 Ultrafiltration membrane assembly
CN103446886A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446887A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446891A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446890A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly, and flushing method and water purifier thereof
CN103663624A (en) * 2012-09-14 2014-03-26 浙江中凯瑞普环境工程股份有限公司 Purification method for oilfield reinjection water
CN105129920A (en) * 2015-09-16 2015-12-09 湖州恒鑫过滤科技有限公司 Runner plate of cross-flow membrane module
WO2017059568A1 (en) * 2015-10-08 2017-04-13 Dow Global Technologies Llc Hollow fiber membrane module including concentrate distributor
CN106621819A (en) * 2016-12-21 2017-05-10 天津膜天膜科技股份有限公司 Hollow fiber desalination membrane assembly and equipment
CN108786473A (en) * 2018-08-29 2018-11-13 郑州恒博环境科技股份有限公司 A kind of polysulfone hollow fiber ultrafiltration membrane system
CN109459283A (en) * 2018-10-31 2019-03-12 国家海洋局天津海水淡化与综合利用研究所 A kind of preparation method of single external pressure hollow-fibre membrane cross-current type component

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101862598A (en) * 2010-06-25 2010-10-20 苏州顶裕节能设备有限公司 Hollow fiber ultra-filtration membrane assembly having improved shell structure
CN102489166A (en) * 2011-12-06 2012-06-13 深圳恒通源水处理科技有限公司 Ultrafiltration membrane processing system and processing technology thereof
CN103446891B (en) * 2012-06-01 2015-11-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446887B (en) * 2012-06-01 2016-04-13 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446887A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446891A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446890A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly, and flushing method and water purifier thereof
CN103446890B (en) * 2012-06-01 2015-11-04 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly, its purging method and water purifier
CN103446886A (en) * 2012-06-01 2013-12-18 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103446886B (en) * 2012-06-01 2016-01-20 珠海格力电器股份有限公司 Flushable external pressure type ultrafiltration filter core assembly and water purifier
CN103663624A (en) * 2012-09-14 2014-03-26 浙江中凯瑞普环境工程股份有限公司 Purification method for oilfield reinjection water
CN103663624B (en) * 2012-09-14 2015-12-16 浙江中凯瑞普环境工程股份有限公司 A kind of process for purification of oil field reinjection water
CN103055700B (en) * 2013-01-30 2015-05-27 高然 Ultrafiltration membrane assembly
CN103055700A (en) * 2013-01-30 2013-04-24 高然 Ultrafiltration membrane assembly
CN105129920A (en) * 2015-09-16 2015-12-09 湖州恒鑫过滤科技有限公司 Runner plate of cross-flow membrane module
WO2017059568A1 (en) * 2015-10-08 2017-04-13 Dow Global Technologies Llc Hollow fiber membrane module including concentrate distributor
CN108136291A (en) * 2015-10-08 2018-06-08 陶氏环球技术有限责任公司 Include the hollow fiber membrane module of concentrate distributor
CN106621819A (en) * 2016-12-21 2017-05-10 天津膜天膜科技股份有限公司 Hollow fiber desalination membrane assembly and equipment
CN108786473A (en) * 2018-08-29 2018-11-13 郑州恒博环境科技股份有限公司 A kind of polysulfone hollow fiber ultrafiltration membrane system
CN108786473B (en) * 2018-08-29 2023-10-03 郑州恒博环境科技股份有限公司 Hollow fiber ultrafiltration membrane component
CN109459283A (en) * 2018-10-31 2019-03-12 国家海洋局天津海水淡化与综合利用研究所 A kind of preparation method of single external pressure hollow-fibre membrane cross-current type component

Also Published As

Publication number Publication date
CN101422698B (en) 2011-11-09

Similar Documents

Publication Publication Date Title
CN101422698B (en) Hollow fiber ultrafiltration micro-filtration membrane module
CN104014246B (en) A kind of double diaphragm cross-flow filtration plate film assembly
CN110652879A (en) External pressure type hollow fiber membrane component and filtering device
CN110339720A (en) A kind of vertical cross-flow filtration integrating device based on hollow-fibre membrane
CN212236746U (en) Ceramic membrane device for washing and purifying superfine powder
CN201423250Y (en) Ultrafiltration membrane self-cleaning device
CN212504128U (en) Ultrafiltration device in reclaimed water recycling system
CN104399373A (en) Multi-channel double-layer type flat membrane combined apparatus
CN112237846A (en) Cross-flow filtering flat membrane component
CN211198738U (en) MBR flat plate filtering membrane middle-mounted aeration scouring device
CN207313223U (en) A kind of New bag MBR plate membrane groups
CN214437987U (en) Cross-flow filtering flat membrane component
CN102068911A (en) Device for rinsing membrane yarns of hollow fiber membranes
CN214880401U (en) Water treatment device and water purifier
CN204017678U (en) A kind of two diaphragm cross-flow filtration plate film assembly
CN202569969U (en) External pressure type hollow fiber membrane module
CN103130349B (en) Water purifier
CN214764555U (en) Grouping reverse osmosis filter element subassembly and water purifier
CN213446370U (en) Alternative reverse flushing type filter element device and water purifier
CN214880278U (en) Water filtering device and water purifier with same
CN212999362U (en) Vitamin B12 draws purification device
CN209778485U (en) Marine sewage water purification unit filter
CN204073864U (en) The dull and stereotyped film group device of multichannel two-layer equation
CN210356709U (en) Cross-flow type ceramic membrane filter
CN211216192U (en) External pressure type hollow fiber membrane component and filtering device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20111109

Termination date: 20161106