CN106040005A - Long-acting spiral-wound membrane module - Google Patents
Long-acting spiral-wound membrane module Download PDFInfo
- Publication number
- CN106040005A CN106040005A CN201610546127.2A CN201610546127A CN106040005A CN 106040005 A CN106040005 A CN 106040005A CN 201610546127 A CN201610546127 A CN 201610546127A CN 106040005 A CN106040005 A CN 106040005A
- Authority
- CN
- China
- Prior art keywords
- central canal
- shell
- hydrophobic cloth
- conductive contact
- electrode
- 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
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 65
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 56
- 239000004744 fabric Substances 0.000 claims abstract description 44
- 230000002209 hydrophobic effect Effects 0.000 claims abstract description 43
- 229920000049 Carbon (fiber) Polymers 0.000 claims abstract description 13
- 239000004917 carbon fiber Substances 0.000 claims abstract description 13
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000007789 sealing Methods 0.000 claims description 23
- 125000006850 spacer group Chemical group 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 6
- 239000000284 extract Substances 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 abstract description 7
- 239000002253 acid Substances 0.000 abstract description 3
- 239000003513 alkali Substances 0.000 abstract description 3
- 230000003203 everyday effect Effects 0.000 abstract description 3
- 238000011010 flushing procedure Methods 0.000 abstract 1
- 238000000746 purification Methods 0.000 description 9
- 239000002351 wastewater Substances 0.000 description 7
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000000605 extraction Methods 0.000 description 4
- 230000004907 flux Effects 0.000 description 4
- 239000000385 dialysis solution Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000005684 electric field Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 150000001450 anions Chemical class 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 241000083547 Columella Species 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- -1 and so Substances 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/10—Spiral-wound membrane modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/22—Electrical effects
- B01D2321/223—Polarity reversal
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a long-acting spiral-wound membrane module which comprises a plurality of spiral-wound membrane elements, a center pipe and a shell. The problems that once membranes are polluted, halt is needed for cleaning, pure water is used every day for cleaning the membrane elements in a back flushing mode, and the membrane elements need to be cleaned with acid and alkali regularly are solved. A hydrophobic cloth (9) is used as a carbon fiber hydrophobic cloth, a flat conductive contact is pulled out of the carbon fiber hydrophobic cloth, all conductive contacts are named according to arranging sequence numbers, the conductive contacts with odd sequence numbers are connected in parallel to form an electrode A, the conductive contacts with even sequence numbers are connected in parallel to form an electrode B, and the electrode A and the electrode B are led out of the shell (7) through the center pipe (6) to be connected with a polarity-adjustable power source.
Description
Technical field:
The present invention is relevant with rolled membrane module.
Background technology:
Rolled membrane module is that existing market uses the most widest film application form, and it is big that it is mainly characterized by loading density, makes
With easy and simple to handle.In great majority film occasion, film is all to occur with the form of rolled film.Rolled membrane module mainly uses Flat Membrane
Sheet rolls and forms.Include the assemblies such as flat board diaphragm, runner spacer web, dialysis solution collecting pipe, putamina.
Wound membrane element is one hydrophobic cloth of folder between two permeable membranes, and the long letter forming a rectangle is closed in three limit heat seals
The flat board diaphragm of envelope shape, unclosed opening edge just hole to central canal, the dialysis solution through film just can be collected into central canal
In.Wound membrane element is wound by a flat board diaphragm and runner spacer web and forms, and is referred to as " single leaf ".Commercialization rolled membrane module is big
Many employing " leafy " structures.In the case of membrane area is substantially the same, the runner of the permeate of leafy more single leaf is short, reduces back pressure
Lose, improve flux, also make runner flowing everywhere more uniform.Leafy wound membrane element is to open unclosed for flat board diaphragm
Just hole to central canal, mouthful limit is cohered on central canal, is re-lining with a runner spacer web, until cohering multi-disc flat board diaphragm also
One-tenth spiral wound it is wound on central canal every lining multi-disc runner spacer web.
The former water of wound membrane element introduces from membrane component end, and the direction flowing parallel along film surface, be separated is saturating
Analysis liquid is then perpendicular to film surface and enters hydrophobic cloth, and so, dialysis solution and former water form the vertically and laterally two kinds of flow directions that intersect.
Zwitterion, salinity and colloid in water is left in former water (forming dense water step by step), and is taken away by lateral current, if film
The water flux of element is excessive, or the response rate too high (referring to exceed maker directive/guide regulation), and salinity and colloid are detained on the surface of the film
Probability the biggest.Excessive concentration can form concentration polarization, and zwitterion, salinity and colloidal solid can polluted membrane surfaces.
Wound membrane element major advantage:
1. compact conformation, in unit volume, effective film area is bigger.
2. processing technology is relatively easy.
3. install, operate more convenient.
But its shortcoming is in use, film is once contaminated, and needs stop cleaning, and every day is clear with water purification recoil
Wash membrane component, periodically to clean membrane component with acid, alkali respectively.The infringement that membrane component is caused by traditional cleaning way, adds
The discharge of waste water, reduces the service life of membrane component, improves the operating cost of device.
Summary of the invention:
It is an object of the invention to provide a kind of membrane module while filtering can self-cleaning, the service life of membrane component
Long, that the operational efficiency of device is high rolled membrane module.
The present invention is achieved in that
The present invention includes that wound membrane element 5, central canal 6, shell 7, wound membrane element 5 are to press from both sides at least one between two permeable membranes 10
Opening the first hydrophobic cloth 9, three limit heat seals are closed the flat board diaphragm of the long envelope shape forming rectangles, are opened unclosed for flat board diaphragm
Just hole to central canal, mouthful limit is cohered on central canal, and one runner spacer web 11 of lining between two wound membrane element 5, multi-disc is put down
Plate diaphragm and runner spacer web 11 are wound on central canal composition helical coil, and helical coil is positioned at shell 7, outside central canal 6 is positioned at
Columella line, its upper and lower end is connected with sealing flange 4, permeable pad 8 between helical coil and sealing flange 4, shell 7 times
Intake antrum between end and sealing flange 4 has original water inlet 1, the water chamber between shell 7 upper end and sealing flange 4 to have dense
Water outlet 3 connects permeable pad 8, and pure water inlet 2 is positioned at external part on central canal 6, and the first hydrophobic cloth 9 is the hydrophobic cloth of carbon fiber,
A flat conductive contact is extracted out, by the conductive contact of all of first hydrophobic cloth 9 according to arrangement in the hydrophobic cloth of carbon fiber
Serial number is named, and is connected in parallel by odd number conductive contact as A electrode, is connected in parallel by even number conductive contact as B electricity
Pole, two electrodes of A, B are connected with adjustable polarity power from shell 7 extraction by central canal 6.
Including some wound membrane element 5, central canal 6, shell 7, wound membrane element 5 is to press from both sides one between two permeable membranes 10
First hydrophobic cloth 9, the flat board diaphragm of the long envelope shape forming a rectangle is closed in three limit heat seals, by unclosed for flat board diaphragm opening
Just hole to central canal, limit is cohered on central canal, and multi-disc flat board diaphragm and runner spacer web 11 are wound on central canal composition spiral shell
Circumvolution, helical coil is positioned at shell 7, and central canal 6 is positioned at housing axis, and its upper and lower end is connected with sealing flange 4, permeable pad 8
Between helical coil and sealing flange 4, the intake antrum between shell 7 lower end and sealing flange 4 has original water inlet 1, outward
Water chamber between shell 7 upper end and sealing flange 4 has condensed water outlet 3 to be connected permeable pad 8, and pure water inlet 2 is positioned at central canal 6
Upper external part, two runner spacer webs 11 of lining between two wound membrane element 5, one second, the folder of two runner spacer webs 11 is dredged
Water cloth 9, the second hydrophobic cloth is the hydrophobic cloth of carbon fiber, extracts a flat conductive contact out, by second in the hydrophobic cloth of carbon fiber
The hydrophobic all of conductive contact of cloth 9 is named according to the number of putting in order, and is connected in parallel by odd number conductive contact as A electrode, general
Even number conductive contact is connected in parallel as B electrode, and two electrodes of A, B are drawn and adjustable polarity electricity from shell 7 by central canal 6
Source connects.
Hydrophobic cloth is extracted out flat thickness 0.2mm, width 8mm, a conductive contact for length 36mm.
The present invention is made the material of the hydrophobic cloth 9 in flat board diaphragm into same specification, electric conductivity with size by nylon material
The hydrophobic cloth of carbon fiber that energy is good, has drawn two electrodes of A, B respectively at two symmetrical ports.Connect adjustable polarity power,
Electric field is formed in wound membrane element.Partly deposit anion on diaphragm, another part diaphragm deposits cation.By certain week
Phase converting power source polarity, due to gravitation and the repulsion effect of electric field, the anions and canons on diaphragm starts to exchange, thus departs from film
Sheet, is carried over diaphragm with the flowing of former water.
The polarity of conversion electric field has just reached to clean the function of diaphragm, makes the membrane element that original every day cleans with water purification recoil
Part and the membrane component periodically cleaned with acid, alkali respectively almost no longer clean.Owing to not using excessive pressure and excessive temperature
Solution carries out positive and negative cleaning to diaphragm, and therefore the life-span of element is greatly prolonged.Improve the operational efficiency of device.
Accompanying drawing illustrates:
Fig. 1 is present configuration figure.
Fig. 2 is the partial enlarged drawing of Fig. 1.
Detailed description of the invention:
Embodiment 1:
The present invention includes that wound membrane element 5, central canal 6, shell 7, wound membrane element 5 are to press from both sides one the between two permeable membranes 10
One hydrophobic cloth 9, the flat board diaphragm of the long envelope shape forming a rectangle is closed in three limit heat seals, by unclosed for flat board diaphragm opening edge
The just hole to central canal is cohered on central canal, one runner spacer web 11 of lining, multi-disc Flat Membrane between two wound membrane element 5
Sheet and runner spacer web 11 are wound on central canal composition helical coil, and helical coil is positioned at shell 7, and central canal 6 is positioned at enclosure axis
Line, its upper and lower end is connected with sealing flange 4, permeable pad 8 between helical coil and sealing flange 4, shell 7 lower end with
Intake antrum between sealing flange 4 has original water inlet 1, the water chamber between shell 7 upper end and sealing flange 4 to have condensed water
The outlet 3 permeable pad 8 of connection, pure water inlet 2 is positioned at external part on central canal 6, and the first hydrophobic cloth 9 is the hydrophobic cloth of carbon fiber, at carbon
The hydrophobic cloth of fiber is extracted a flat conductive contact, by all of first hydrophobic cloth 9 conductive contact according to the number of putting in order out
Name, is connected in parallel odd number conductive contact as A electrode, is connected in parallel even number conductive contact into B electrode, A, B
Two electrodes are connected with adjustable polarity power from shell 7 extraction by central canal 6.
Hydrophobic cloth is extracted out flat thickness 0.2mm, width 8mm, a conductive contact for length 36mm.
Embodiment 2:
Including some wound membrane element 5, central canal 6, shell 7, wound membrane element 5 is to press from both sides one first between two permeable membranes 10
Hydrophobic cloth 9, three limit heat seals close the flat board diaphragm of the long envelope shape forming a rectangle, by unclosed for flat board diaphragm opening edge just
The hole of central canal is cohered on central canal, at least one runner spacer web 11 of lining, multi-disc flat board between two wound membrane element 5
Diaphragm and runner spacer web 11 are wound on central canal composition helical coil, and helical coil is positioned at shell 7, and central canal 6 is positioned at shell
Axis, its upper and lower end is connected with sealing flange 4, permeable pad 8 between helical coil and sealing flange 4, shell 7 lower end
And the intake antrum between sealing flange 4 has original water inlet 1, the water chamber between shell 7 upper end and sealing flange 4 to have concentration
Water out 3 connects permeable pad 8, and pure water inlet 2 is positioned at external part on central canal 6, two runners of lining between two wound membrane element 5
Spacer web 11, second hydrophobic cloth 9 of the folder of two runner spacer webs 11, the second hydrophobic cloth is the hydrophobic cloth of carbon fiber, fine at carbon
Tie up one flat conductive contact of extraction in hydrophobic cloth, the second hydrophobic all of conductive contact of cloth 9 is ordered according to the number of putting in order
Name, is connected in parallel odd number conductive contact as A electrode, is connected in parallel by even number conductive contact as B electrode, A, B two
Individual electrode is connected with adjustable polarity power from shell 7 extraction by central canal 6.
Experimental example:
From the former water of original water inlet 1 through the periphery of ring flange 4 and permeable pad 8, enter in rustless steel putamina 7, at pressure
Under effect, former water enters hydrophobic cloth 9 through permeable membrane 10, and entering collector pipe 6 under pressure becomes water purification, pure water inlet 2
Outflow is collected；A part of former water along film post through permeable pad 8 along the periphery of ring flange 4 and permeable pad 8 through going out to concentrate the mouth of a river 3
Discharge condensed water.
A, B are electrode, when film post works, the unidirectional current on A, B electrode, every 5-10 minute conversion polarity, A just, B
Negative, after 5-10 minute, become that A is negative, B just, so every 5-10 minute circulation primary, test voltage is 12V-36V.
Rolled film post with two kinds of different area of NF is explained for experimental example below:
Experimental example 1:
Long-acting rolled membrane module structure is the structure of embodiment 1.
Being rolled into the NF film post similar to Fig. 1 structure with flat board diaphragm, the area of film is 1, when temperature is 20 DEG C～28
DEG C, use tap water to make former water, be that 4L/min pumps into former water to NF film post with the water pump that pressure is 1.6MPa by flux, be not added with
On the premise of reversal power supply, can stream time at about 3 days, As time goes on, water yield reduces per hour
About 2%, after 72 hours, film is blocked, substantially can not be then exhausted from water purification, and wastewater flow rate increases to about 4L/min.
When on A, B electrode plus the power supply of adjustable polarity, voltage is V2, and electric current is 0.3A.When polarity conversion in every 8 minutes
A when time, the water purification output of NF film post is about 3.4L/min, and wastewater effluent amount is about 0.6L/min, ensuing 30 days
In, the output of water purification successively decreases 1% for every 3 days, and waste water output is incremented by 1% for every 3 days, continuously after work 60 days, and rolling NF film post
Still can work on.
Experimental example 2:
Long-acting rolled membrane module structure is the structure of embodiment 2.
Being rolled into the NF film post similar to Fig. 1 structure with flat board diaphragm, membrane area is 9, when temperature is 20 DEG C～28 DEG C,
Use tap water to make former water, be that 60L/min pumps into former water to film post, in not additive polarity with the water pump that pressure is 1.6MPa by flux
On the premise of converting power source, can stream time at about 3 days, As time goes on, it is left that water yield reduces 2% per hour
The right side, after 72 hours, film is blocked, substantially can not be then exhausted from water purification, and wastewater flow rate increases to about 60L/min.
When on A, B electrode plus the power supply of adjustable polarity, voltage is V1, and electric current is 3A.When polarity conversion one in every 8 minutes
Time secondary, water purification average output is 52 L/min, and waste water output is 8 L/min, As time goes on, and every 3 days water purification
Output will successively decrease about 1%, and waste water output will be incremented by about 1% for every 3 days, the most continuously after work 60 days, and rolling
Film post still can work on.
Above-mentioned test is done with tri-kinds of flat board diaphragms of RO, UF, MF, under suitable DC voltage, regular reverse, have
The same effect extending the cleaning frequency.
Claims (3)
- The most long-acting rolled membrane module, including some wound membrane element (5), central canal (6), shell (7), wound membrane element is two Pressing from both sides a first hydrophobic cloth (9) between permeable membrane (10), the Flat Membrane of the long envelope shape forming a rectangle is closed in three limit heat seals Sheet, by unclosed for flat board diaphragm opening edge, just hole to central canal is cohered on central canal, and between two wound membrane element, lining is extremely A few runner spacer web (11), multi-disc flat board diaphragm and runner spacer web are wound on central canal composition helical coil, helical coil Being positioned at shell, central canal is positioned at housing axis, and its upper and lower end is connected with sealing flange (4), and permeable pad (8) is positioned at spiral Between volume and sealing flange, the intake antrum between shell lower end and sealing flange has original water inlet (1), and shell upper end is with close Water chamber between envelope ring flange has condensed water outlet (3) to connect permeable pad, and pure water inlet (2) is positioned at external part on central canal, It is characterized in that the first hydrophobic cloth (9) is the hydrophobic cloth of carbon fiber, the hydrophobic cloth of carbon fiber extracted out a flat conductive contact, The conductive contact of all of first hydrophobic cloth is named according to the number of putting in order, odd number conductive contact is connected in parallel as A Electrode, is connected in parallel as B electrode by even number conductive contact, and two electrodes of A, B are drawn with adjustable from shell by central canal Polarity power connects.
- The most long-acting rolled membrane module, it is characterised in that include some wound membrane element (5), central canal (6), shell (7), rolled film Element is one the first hydrophobic cloth (9) of folder between two permeable membranes (10), and the long envelope forming a rectangle is closed in three limit heat seals The flat board diaphragm of shape, by unclosed for flat board diaphragm opening edge, just hole to central canal is cohered on central canal, two wound membrane element Between at least one runner spacer web (11) of lining, multi-disc flat board diaphragm and runner spacer web be wound on central canal composition spiral Volume, helical coil is positioned at shell, and central canal is positioned at housing axis, and its upper and lower end is connected with sealing flange (4), permeable pad (8) Between helical coil and sealing flange, the intake antrum between shell lower end and sealing flange has original water inlet (1), shell Water chamber between upper end with sealing flange has condensed water outlet (3) to be connected permeable pad, and pure water inlet (2) is positioned on central canal External part, it is characterised in that two runner spacer webs (11) of lining between two wound membrane element (5), between two runner spacer webs Pressing from both sides a second hydrophobic cloth, the second hydrophobic cloth is the hydrophobic cloth of carbon fiber, extracts a flat conduction in the hydrophobic cloth of carbon fiber out Joint, names the second all of conductive contact of hydrophobic cloth according to the number of putting in order, is connected in parallel by odd number conductive contact For A electrode, even number conductive contact is connected in parallel into B electrode, two electrodes of A, B by central canal from shell draw with can Tune polarity power connects.
- Long-acting rolled membrane module the most according to claim 1 and 2, it is characterised in that extracting conductive contact in hydrophobic cloth out is one Individual flat thickness 0.2mm, width 8mm, the conductive contact of length 36mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610546127.2A CN106040005B (en) | 2016-07-13 | 2016-07-13 | Rolled membrane module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610546127.2A CN106040005B (en) | 2016-07-13 | 2016-07-13 | Rolled membrane module |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106040005A true CN106040005A (en) | 2016-10-26 |
| CN106040005B CN106040005B (en) | 2018-03-27 |
Family
ID=57185343
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610546127.2A Expired - Fee Related CN106040005B (en) | 2016-07-13 | 2016-07-13 | Rolled membrane module |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106040005B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002530A (en) * | 2019-05-06 | 2019-07-12 | 中国科学院生态环境研究中心 | Film absorbent module, renewable membrane adsorptive reactor, liquid handling device and method |
| CN113456914A (en) * | 2021-07-06 | 2021-10-01 | 广州市恩德氏医疗制品实业有限公司 | Flat-plate rolling type dialyzer |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4624760A (en) * | 1984-06-21 | 1986-11-25 | United Kingdom Atomic Energy Authority | Filter cleaning |
| CN1045232A (en) * | 1989-01-25 | 1990-09-12 | 艾尔坎国际有限公司 | Filter cleaning |
| JPH0398621A (en) * | 1989-09-08 | 1991-04-24 | Shinko Pantec Co Ltd | Electric film filter device and its operation |
| JPH10165772A (en) * | 1996-12-05 | 1998-06-23 | Nitto Denko Corp | Reverse osmosis membrane module and liquid separation method |
| JPH11216343A (en) * | 1998-02-02 | 1999-08-10 | Toshiba Plant Kensetsu Co Ltd | Drainage treatment device |
| CN101415646A (en) * | 2006-03-31 | 2009-04-22 | 三井造船株式会社 | Method for treating ballast water by membrane usin membrane module, and membrane treatment apparatus |
| CN101721915A (en) * | 2008-10-28 | 2010-06-09 | 财团法人工业技术研究院 | Method and apparatus for cleaning thin film |
| CN102781558A (en) * | 2009-11-25 | 2012-11-14 | 悉尼大学 | Membrane and membrane separation system |
-
2016
- 2016-07-13 CN CN201610546127.2A patent/CN106040005B/en not_active Expired - Fee Related
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4624760A (en) * | 1984-06-21 | 1986-11-25 | United Kingdom Atomic Energy Authority | Filter cleaning |
| CN1045232A (en) * | 1989-01-25 | 1990-09-12 | 艾尔坎国际有限公司 | Filter cleaning |
| JPH0398621A (en) * | 1989-09-08 | 1991-04-24 | Shinko Pantec Co Ltd | Electric film filter device and its operation |
| JPH10165772A (en) * | 1996-12-05 | 1998-06-23 | Nitto Denko Corp | Reverse osmosis membrane module and liquid separation method |
| JPH11216343A (en) * | 1998-02-02 | 1999-08-10 | Toshiba Plant Kensetsu Co Ltd | Drainage treatment device |
| CN101415646A (en) * | 2006-03-31 | 2009-04-22 | 三井造船株式会社 | Method for treating ballast water by membrane usin membrane module, and membrane treatment apparatus |
| CN101721915A (en) * | 2008-10-28 | 2010-06-09 | 财团法人工业技术研究院 | Method and apparatus for cleaning thin film |
| CN102781558A (en) * | 2009-11-25 | 2012-11-14 | 悉尼大学 | Membrane and membrane separation system |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002530A (en) * | 2019-05-06 | 2019-07-12 | 中国科学院生态环境研究中心 | Film absorbent module, renewable membrane adsorptive reactor, liquid handling device and method |
| CN113456914A (en) * | 2021-07-06 | 2021-10-01 | 广州市恩德氏医疗制品实业有限公司 | Flat-plate rolling type dialyzer |
| CN113456914B (en) * | 2021-07-06 | 2023-11-07 | 广州市恩德氏医疗制品实业有限公司 | Flat plate winding type dialyzer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106040005B (en) | 2018-03-27 |
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