CN107890781A - A kind of Hollow Fiber Ultrafiltration counter-infiltration integrates membrane module and its preparation technology - Google Patents
A kind of Hollow Fiber Ultrafiltration counter-infiltration integrates membrane module and its preparation technology Download PDFInfo
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- CN107890781A CN107890781A CN201711083380.XA CN201711083380A CN107890781A CN 107890781 A CN107890781 A CN 107890781A CN 201711083380 A CN201711083380 A CN 201711083380A CN 107890781 A CN107890781 A CN 107890781A
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- membrane
- reverse osmosis
- hollow fiber
- water
- bag
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- 239000012528 membrane Substances 0.000 title claims abstract description 111
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 31
- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 27
- 238000001764 infiltration Methods 0.000 title claims abstract description 14
- 238000005516 engineering process Methods 0.000 title claims abstract description 11
- 238000002360 preparation method Methods 0.000 title claims abstract description 7
- 238000001223 reverse osmosis Methods 0.000 claims abstract description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 239000000835 fiber Substances 0.000 claims abstract description 12
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 238000007789 sealing Methods 0.000 claims abstract 2
- 239000003292 glue Substances 0.000 claims description 7
- 238000005266 casting Methods 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 4
- 238000003780 insertion Methods 0.000 claims description 3
- 230000037431 insertion Effects 0.000 claims description 3
- 239000003822 epoxy resin Substances 0.000 claims description 2
- 229920000647 polyepoxide Polymers 0.000 claims description 2
- 238000000465 moulding Methods 0.000 claims 1
- 238000005096 rolling process Methods 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 7
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 210000004379 membrane Anatomy 0.000 description 35
- 238000000034 method Methods 0.000 description 11
- 238000000926 separation method Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- 238000012695 Interfacial polymerization Methods 0.000 description 2
- 210000002469 basement membrane Anatomy 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 238000001471 micro-filtration Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 241000219146 Gossypium Species 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- -1 boiler feedwater Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000009292 forward osmosis Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 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
- B01D63/02—Hollow fibre modules
- B01D63/021—Manufacturing thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/58—Multistep processes
-
- 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
- B01D63/02—Hollow fibre modules
- B01D63/021—Manufacturing thereof
- B01D63/022—Encapsulating hollow fibres
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention discloses a kind of Hollow Fiber Ultrafiltration counter-infiltration and integrates membrane module and its preparation technology, and the integrated membrane module includes：Central tube, ultra-low-pressure reverse osmosis film, production water flow passage net, hollow fiber ultrafiltration membrane and membrane module shell.There is the mouth of a river on the central tube tube wall, one end sealing, another end opening is as pure water delivery port.The ultra-low-pressure reverse osmosis film highest operating pressure is no more than 0.4MPa, and ultra-low-pressure reverse osmosis film is welded as into reverse osmosis membrane bag；The hollow-fibre membrane ultrafiltration is inner pressed ultra filtration hollow fiber membrane, is uniformly filled between two neighboring reverse osmosis membrane bag.Membrane module is integrated according to the Hollow Fiber Ultrafiltration counter-infiltration of the present invention, overall structure is more simplified, and can dispense the multistage pretreatment unit of existing purifier, therefore can play the effect for saving material and environmental protection.Ultra filtration hollow fiber membrane part reversely rushes cleaning film inwall by periodically changing Inlet and outlet water direction simultaneously, can extend the overall service life of membrane component with several times.
Description
Technical field
The present invention relates to water treatment facilities manufacturing technology field, more particularly to a kind of Hollow Fiber Ultrafiltration-counter-infiltration integrates
Membrane module and its preparation technology.
Background technology
Membrane separation technique is the new and high technology of an emerging a variety of subject crossings, and it is most important to be acknowledged as 21st century
One of new technology.Seperation film can be divided into microfiltration membranes, milipore filter, NF membrane, forward osmosis membrane and reverse osmosis by the size in its aperture
Permeable membrane etc., wherein ultrafiltration are the water technologies between micro-filtration and nanofiltration, and milipore filter pore diameter range is 0.001-0.02 μ
M, molecular cut off are generally 500-1000000 Da, and trapped substance is usually macromolecular particle and colloidal particle, operating pressure one
As be 0.2-0.4 MPa.Hollow fiber ultrafiltration membrane due to its good pressure-resistant performance, packed density is big, specific surface area is high the advantages that quilt
It is widely used in water treatment process.
Reverse osmosis membrane pore diameter range is 0.1-1 nm, separation object be dissolved in ion in water and molecular weight hundreds of with
On organic matter.With resident's issuing to the raising that is recognized with water quality and national environmental protection policy, reverse osmosis membrane is being lived
It is more and more wider with industrial application field, including drinking water, boiler feedwater, medicine, food, bitter desalination and work
The multiple fields such as industry wastewater treatment, particularly spiral wound reverse-osmosis membrane element, designed because its is compact, cheap price makes
It occupies most of market share.
Existing reverse-osmosis membrane element uses concentrated water filter to provide intake tunnel for reverse osmosis membrane, and concentrated water filter quality is hard,
Easily reverse osmosis membrane is caused to scratch, also easy contaminant deposition, and then influence separating property and the use of reverse-osmosis membrane element
Life-span.
Reverse osmosis membrane has higher requirement, the too poor pollution that can cause reverse osmosis membrane of water quality, shadow to the water quality of raw water simultaneously
Counter-infiltration membrane separation efficiency is rung, reduces the service life of reverse osmosis membrane, existing solution method is when using reverse osmosis membrane
Some preposition pretreatment units, such as activated carbon, PP cottons etc. are equipped with, so make that whole filtration system is cumbersome, space-consuming is big, simultaneously
These materials are easy to long bacterium and cause secondary pollution, it is necessary to regularly replace, and cause the waste of material and the pollution of environment.
The content of the invention
In order to overcome above-mentioned technical problem, the main object of the present invention is to provide a kind of Hollow Fiber Ultrafiltration-counter-infiltration collection
Into membrane module and its preparation technology, it is intended to solve the deficiencies in the prior art, i.e., disposable preposition pretreatment material in water treatment procedure
The waste of material is short with the service life of overall membrane component greatly.
To achieve the above object, a kind of Hollow Fiber Ultrafiltration-counter-infiltration proposed by the present invention integrates membrane module, and it prepares work
Skill includes：
1. preparing reverse osmosis membrane bag, from ultra-low-pressure reverse osmosis diaphragm, specific method is along the back side by reverse osmosis membrane（Non-woven fabrics
Face）Two sides of diaphragm rolled well will be sealed, make a reverse osmosis membrane bag by doubling, centre insertion water guide net using AB glue.
2. the reverse osmosis membrane bag is welded on central tube with glue successively, film bag opening crosses water towards on central tube
Mouthful.The film bag being welded is rolled up into a circle by specific direction on central tube, increases the fastness of film bag.
3. between inner pressed hollow fiber ultrafiltration membrane is uniformly filled into described two film bags, and the Hollow Fiber Ultrafiltration
Film length is longer than film bag parallel with it, reserves casting, the distance of cut end（At Fig. 2 dotted lines）.
4. by hollow-fibre membrane, reverse osmosis membrane bag and central tube overall package to membrane module shell, epoxy resin is used
Hollow-fibre membrane both ends and membrane module shell are cast, cut end.The shell（Such as Fig. 2）For cylinder, both ends are respectively
The water inlet and delivery port of raw water, and it is furnished with corresponding screw cap, there is a reverse osmosis concentrated shrink delivery port shell side.Center
Pipe one end is pure water delivery port, and the other end seals.
Compared with prior art, a kind of Hollow Fiber Ultrafiltration-counter-infiltration of the present invention integrates membrane module and its preparation
Technique has the characteristics that：
1. the form of membrane module being integrated using Hollow Fiber Ultrafiltration-counter-infiltration so that whole water purification structure is more simplified, is compact,
Save space, material and running cost；
2. hollow-fibre membrane is evenly distributed between reverse osmosis membrane bag, concentrated water filter can be played a part of, improve whole component
Interior streamflow regime, more uniform water stream channel is provided for reverse osmosis membrane bag；
3. compared with the concentrated water filter used in existing reverse-osmosis membrane element, hollow fiber ultrafiltration membrane profile is carefully round and soft, will not
Reverse osmosis membrane surface is caused to scratch, ensures membrane separation efficiency and stability；
4. the form of membrane module is integrated using Hollow Fiber Ultrafiltration-counter-infiltration, it is convenient to omit before the multistage for falling existing purifier
Pretreatment unit is put, the effect for saving material and environmental protection can be played.Hollow fiber ultrafiltration membrane is by periodically changing disengaging simultaneously
Water direction reversely rushes cleaning film inwall, can count the service life for extending overall membrane module.
Brief description of the drawings
Fig. 1 is the Structure of cross section schematic diagram of the embodiment of the present invention.
Fig. 2 is the structural representation of the embodiment of the present invention.
In figure, 1 is reverse osmosis membrane, and 2 be the production network of rivers, and 3 be central tube, and 4 be hollow-fibre membrane, and 5 be membrane module shell, and 6 are
The water inlet of membrane module, 7 be hollow fiber ultrafiltration membrane condensed water delivery port, and 8 be reverse osmosis concentrated shrink delivery port, and 9 be that pure water goes out
The mouth of a river, 10 be seal.
Embodiment
Below in conjunction with the technical scheme in 1,2 pairs of embodiment of the present invention of accompanying drawing in the embodiment of the present invention carry out it is clear,
It is fully described by, the scope that the present invention is protected includes but is not limited to embodiment described below.
Process for using：As shown in Figure 1, 2, raw water is intake from the water inlet 6 of the integral membrane module using membrane pump, adjusted
Appropriate pressure is saved, raw water is after the filtering of inner pressed hollow fiber ultrafiltration membrane 4, and condensed water is discharged by delivery port 7, filter water
The surface of reverse osmosis membrane 1 is flowed to along the outer wall of hollow-fibre membrane 4.Water after reverse osmosis membrane filtration flows to center along the production network of rivers 2
Pipe 3, mouth of a river outflow is crossed through central tube.Pure water is obtained by delivery port 9 of the above filter process can in integrated membrane module.
Embodiment 1
First, reverse osmosis membrane bag is made, concrete operation method is：Pass through the method system of the interfacial polymerization on flat plate ultrafiltration basement membrane
Standby polysulfones-polyamide ultra-low-pressure reverse osmosis diaphragm, by reverse osmosis membrane 1 along the back side（Nonwoven cloth cover）Doubling, centre insertion water guide
Net 2, two sides of diaphragm rolled well will be sealed with water guide net using AB glue, make the reverse osmosis membrane bag of an one end open.
Secondly, the reverse osmosis membrane bag is welded on central tube 3 with glue successively, film bag opening is towards the mistake on central tube
The mouth of a river.The film bag being welded is rolled up into a circle by specific direction on central tube, increases the fastness of film bag.
Then, between polysulfones inner pressed hollow fiber ultrafiltration membrane 4 being uniformly filled into above-mentioned two neighboring film bag, and it is described
Ultra filtration hollow fiber membrane length is longer than film bag parallel with it, reserves casting, the distance of cut end（At Fig. 2 dotted lines）.
Finally, by hollow-fibre membrane, reverse osmosis membrane bag and central tube overall package to membrane module shell 5, epoxy is used
Resin is cast hollow-fibre membrane both ends and membrane module shell, cut end.The shell is cylinder, and both ends are respectively raw water
Water inlet 6 and delivery port 7, and be furnished with corresponding screw cap, there is a reverse osmosis concentrated shrink delivery port 8 shell side.Center
Pipe one end is pure water delivery port 9, and the other end 10 seals.
Embodiment 2
First, reverse osmosis membrane bag is made, concrete operation method is：Pass through the method system of the interfacial polymerization on flat plate ultrafiltration basement membrane
Standby polyether sulfone-poly aromatic acid amides ultra-low-pressure reverse osmosis diaphragm, by reverse osmosis membrane 1 along the back side（Nonwoven cloth cover）Doubling, in interleave
Enter water guide net 2, two sides of diaphragm rolled well will be sealed with water guide net using AB glue, make the counter-infiltration of an one end open
Film bag.
Secondly, the reverse osmosis membrane bag is welded on central tube 3 with glue successively, film bag opening is towards the mistake on central tube
The mouth of a river.The film bag being welded is rolled up into a circle by specific direction on central tube, increases the fastness of film bag.
Then, between Kynoar inner pressed hollow fiber ultrafiltration membrane 4 being uniformly filled into above-mentioned two neighboring film bag,
And the ultra filtration hollow fiber membrane length is longer than film bag parallel with it, casting, the distance of cut end are reserved（Such as Fig. 2 dotted lines
Place）.
Finally, by hollow-fibre membrane, reverse osmosis membrane bag and central tube overall package to membrane module shell 5, epoxy is used
Resin is cast hollow-fibre membrane both ends and membrane module shell, cut end.The shell is cylinder, and both ends are respectively raw water
Water inlet 6 and delivery port 7, and be furnished with corresponding screw cap, there is a reverse osmosis concentrated shrink delivery port 8 shell side.Center
Pipe one end is pure water delivery port 9, and the other end 10 seals.
Above is embodiments of the present invention.It should be pointed out that to those of ordinary skill in the art, do not departing from
On the premise of base its general principles, some improvements and modifications can also be made, these improvements and modifications are also considered as the present invention
Protection domain.
Claims (6)
1. a kind of Hollow Fiber Ultrafiltration-counter-infiltration integrates membrane module and its preparation technology, it is characterised in that including：Central tube, make
For the water output duct of pure water；Ultra-low-pressure reverse osmosis film, reverse osmosis membrane is along the back side（Nonwoven cloth cover）Doubling, centre insertion water guide
Net, by two side welded seals of diaphragm to rolling well, make a reverse osmosis membrane bag；Water flow passage net is produced, inserts above-mentioned doubling
In good diaphragm, two side welded seals, a reverse osmosis membrane bag is made；Hollow fiber ultrafiltration membrane, it is the hollow fibre of inner pressed
Milipore filter is tieed up, is uniformly filled between two reverse osmosis membrane bags；Membrane module shell, for by hollow fiber ultrafiltration membrane and counter-infiltration
Film bag cast molding.
2. central tube according to claim 1, it is characterised in that had the mouth of a river, central tube one on the central tube tube wall
End sealing, delivery port of another end opening as pure water.
3. ultra-low-pressure reverse osmosis film according to claim 1, it is characterised in that highest operating pressure is no more than 0.4MPa,
Ultra-low-pressure reverse osmosis film is welded as reverse osmosis membrane bag, concrete operations are：Reverse osmosis membrane is along the back side（Nonwoven cloth cover）Doubling, in
Between insert water guide net, two sides of diaphragm rolled well will be sealed using AB glue, make a reverse osmosis membrane bag.
4. production water flow passage net according to claim 1, it is characterised in that it is wide runner net, it is pure for film bag to be filtered
The rapid water conservancy diversion of water, slow down the resistance of water.
5. hollow fiber ultrafiltration membrane according to claim 1, it is characterized in that inner pressed ultra filtration hollow fiber membrane, uniformly filling
To between two neighboring reverse osmosis membrane bag, and the ultra filtration hollow fiber membrane length is longer than reverse osmosis membrane bag parallel with it,
Reserve casting, the distance of cut end.
6. membrane module shell according to claim 1, it is characterised in that seal hollow fiber ultrafiltration membrane and reverse osmosis membrane bag
It is attached in membrane module shell, hollow-fibre membrane both ends and membrane module shell is cast using epoxy resin, cut end, the shell is
Cylinder, both ends are open respectively, and there is a reverse osmosis concentrated shrink delivery port side, and water outlet is provided with valve and can adjust water outlet
Amount.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711083380.XA CN107890781A (en) | 2017-11-07 | 2017-11-07 | A kind of Hollow Fiber Ultrafiltration counter-infiltration integrates membrane module and its preparation technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711083380.XA CN107890781A (en) | 2017-11-07 | 2017-11-07 | A kind of Hollow Fiber Ultrafiltration counter-infiltration integrates membrane module and its preparation technology |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107890781A true CN107890781A (en) | 2018-04-10 |
Family
ID=61804164
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711083380.XA Pending CN107890781A (en) | 2017-11-07 | 2017-11-07 | A kind of Hollow Fiber Ultrafiltration counter-infiltration integrates membrane module and its preparation technology |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336224A (en) * | 2018-11-30 | 2019-02-15 | 佛山市云米电器科技有限公司 | Collect the filter core and water purifier of ultrafiltration and reverse osmosis integrated design |
| CN116726709A (en) * | 2023-07-15 | 2023-09-12 | 广东永聚河科技有限公司 | Hollow fiber ultrafiltration membrane component for water treatment |
| CN117699917A (en) * | 2023-12-29 | 2024-03-15 | 江西国膜环保科技有限公司 | Radial multi-membrane bag reverse osmosis membrane |
| CN120817652A (en) * | 2025-09-12 | 2025-10-21 | 深圳市鹏翔汇星水处理技术有限公司 | A high-flux stainless steel reverse osmosis membrane group and its dynamic pressure equalization method |
Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2485293Y (en) * | 2001-07-05 | 2002-04-10 | 杨文玮 | Hollow fiber ultrafiltering membrane elements with pressure housing |
| WO2004069391A1 (en) * | 2003-02-03 | 2004-08-19 | Toyo Boseki Kabushiki Kaisha | Hollow fiber membrane module and module arrangement group thereof |
| CN201240892Y (en) * | 2008-05-20 | 2009-05-20 | 浙江玉泉环境工程有限公司 | Pure water production apparatus with reverse osmosis membrane |
| CN201404723Y (en) * | 2009-03-24 | 2010-02-17 | 杭州科诺过滤器材有限公司 | Filter element |
| CN201578994U (en) * | 2010-01-22 | 2010-09-15 | 苏州膜华材料科技有限公司 | A Submerged Flat Plate Membrane Separator |
| CN201592061U (en) * | 2010-01-01 | 2010-09-29 | 浙江东洋环境工程有限公司 | Hollow fiber filter membrane module |
| CN102527251A (en) * | 2010-12-30 | 2012-07-04 | 北京清大膜科膜技术有限公司 | Small-bore reeled type ultrafiltration membrane |
| CN103332813A (en) * | 2013-06-14 | 2013-10-02 | 河海大学 | Pretreatment device for domestic drinking water |
| CN104258733A (en) * | 2014-07-02 | 2015-01-07 | 深圳市诚德来实业有限公司 | A water purifier and a reverse osmosis membrane element thereof |
| CN104787917A (en) * | 2015-04-09 | 2015-07-22 | 宁波摩尔森膜环保科技有限公司 | Household integrated filter |
| CN204918077U (en) * | 2015-06-25 | 2015-12-30 | 北京大井易通科技发展有限公司 | Novel single -ended encapsulation filtering component |
| CN106039999A (en) * | 2016-07-07 | 2016-10-26 | 北京碧水源膜科技有限公司 | Unidirectional grid device with reverse osmosis membrane elements and method for manufacturing unidirectional grid device |
| CN106076123A (en) * | 2016-08-22 | 2016-11-09 | 厦门建霖工业有限公司 | A kind of big flow long-life coiled reverse osmosis membrane element |
| CN206240334U (en) * | 2016-08-31 | 2017-06-13 | 北京碧水源膜科技有限公司 | A kind of slit is aerated rolling hollow fiber uf membrane system |
-
2017
- 2017-11-07 CN CN201711083380.XA patent/CN107890781A/en active Pending
Patent Citations (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2485293Y (en) * | 2001-07-05 | 2002-04-10 | 杨文玮 | Hollow fiber ultrafiltering membrane elements with pressure housing |
| WO2004069391A1 (en) * | 2003-02-03 | 2004-08-19 | Toyo Boseki Kabushiki Kaisha | Hollow fiber membrane module and module arrangement group thereof |
| CN201240892Y (en) * | 2008-05-20 | 2009-05-20 | 浙江玉泉环境工程有限公司 | Pure water production apparatus with reverse osmosis membrane |
| CN201404723Y (en) * | 2009-03-24 | 2010-02-17 | 杭州科诺过滤器材有限公司 | Filter element |
| CN201592061U (en) * | 2010-01-01 | 2010-09-29 | 浙江东洋环境工程有限公司 | Hollow fiber filter membrane module |
| CN201578994U (en) * | 2010-01-22 | 2010-09-15 | 苏州膜华材料科技有限公司 | A Submerged Flat Plate Membrane Separator |
| CN102527251A (en) * | 2010-12-30 | 2012-07-04 | 北京清大膜科膜技术有限公司 | Small-bore reeled type ultrafiltration membrane |
| CN103332813A (en) * | 2013-06-14 | 2013-10-02 | 河海大学 | Pretreatment device for domestic drinking water |
| CN104258733A (en) * | 2014-07-02 | 2015-01-07 | 深圳市诚德来实业有限公司 | A water purifier and a reverse osmosis membrane element thereof |
| CN104787917A (en) * | 2015-04-09 | 2015-07-22 | 宁波摩尔森膜环保科技有限公司 | Household integrated filter |
| CN204918077U (en) * | 2015-06-25 | 2015-12-30 | 北京大井易通科技发展有限公司 | Novel single -ended encapsulation filtering component |
| CN106039999A (en) * | 2016-07-07 | 2016-10-26 | 北京碧水源膜科技有限公司 | Unidirectional grid device with reverse osmosis membrane elements and method for manufacturing unidirectional grid device |
| CN106076123A (en) * | 2016-08-22 | 2016-11-09 | 厦门建霖工业有限公司 | A kind of big flow long-life coiled reverse osmosis membrane element |
| CN206240334U (en) * | 2016-08-31 | 2017-06-13 | 北京碧水源膜科技有限公司 | A kind of slit is aerated rolling hollow fiber uf membrane system |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336224A (en) * | 2018-11-30 | 2019-02-15 | 佛山市云米电器科技有限公司 | Collect the filter core and water purifier of ultrafiltration and reverse osmosis integrated design |
| CN116726709A (en) * | 2023-07-15 | 2023-09-12 | 广东永聚河科技有限公司 | Hollow fiber ultrafiltration membrane component for water treatment |
| CN117699917A (en) * | 2023-12-29 | 2024-03-15 | 江西国膜环保科技有限公司 | Radial multi-membrane bag reverse osmosis membrane |
| CN117699917B (en) * | 2023-12-29 | 2025-12-09 | 江西国膜环保科技有限公司 | Radial multi-membrane bag reverse osmosis membrane |
| CN120817652A (en) * | 2025-09-12 | 2025-10-21 | 深圳市鹏翔汇星水处理技术有限公司 | A high-flux stainless steel reverse osmosis membrane group and its dynamic pressure equalization method |
| CN120817652B (en) * | 2025-09-12 | 2025-12-09 | 深圳市鹏翔汇星水处理技术有限公司 | High-flux stainless steel reverse osmosis membrane group and dynamic pressure equalization method thereof |
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Address after: 300382 305, room 4, 4 building, Hai Lan De 35, Cai Dao Road, Xiqing,, Tianjin. Applicant after: TIANJIN TIANGONG NEW MATERIAL TECHNOLOGY Co.,Ltd. Address before: 300382 305, room 4, 4 building, Hai Lan De 35, Cai Dao Road, Xiqing,, Tianjin. Applicant before: Technology University (Tianjin) New Material Technology Co.,Ltd. Address after: 300382 305, room 4, 4 building, Hai Lan De 35, Cai Dao Road, Xiqing,, Tianjin. Applicant after: Technology University (Tianjin) New Material Technology Co.,Ltd. Address before: 300382 305, room 4, 4 building, Hai Lan De 35, Cai Dao Road, Xiqing,, Tianjin. Applicant before: TIANJIN LONGYUAN NEW MATERIAL TECHNOLOGY Co.,Ltd. |
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Address after: 300382 Room 305, room 4, No. 35, Hyde building, Xiqing Xuefu Road, Xiqing Xuefu industrial district, Xiqing District, Tianjin Applicant after: Tianjin Tianyuan New Material Technology Co.,Ltd. Address before: 300382 Room 305, room 4, No. 35, Hyde building, Xiqing Xuefu Road, Xiqing Xuefu industrial district, Xiqing District, Tianjin Applicant before: TIANJIN TIANGONG NEW MATERIAL TECHNOLOGY Co.,Ltd. |
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Application publication date: 20180410 |