CN1935340A - Polysulfone amide separating membrane and its modifying method utilizing nanotitanium dioxide - Google Patents
Polysulfone amide separating membrane and its modifying method utilizing nanotitanium dioxide Download PDFInfo
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- CN1935340A CN1935340A CN 200610010489 CN200610010489A CN1935340A CN 1935340 A CN1935340 A CN 1935340A CN 200610010489 CN200610010489 CN 200610010489 CN 200610010489 A CN200610010489 A CN 200610010489A CN 1935340 A CN1935340 A CN 1935340A
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- polysulfonamides
- diffusion barrier
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- titanium dioxide
- membrane
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- 239000012528 membrane Substances 0.000 title claims abstract description 32
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical compound [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 title claims abstract description 15
- 238000000034 method Methods 0.000 title claims description 10
- 150000001408 amides Chemical class 0.000 title claims 2
- 229920002492 poly(sulfone) Polymers 0.000 title claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000008367 deionised water Substances 0.000 claims abstract description 22
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 22
- 239000003960 organic solvent Substances 0.000 claims abstract description 14
- 238000002360 preparation method Methods 0.000 claims abstract description 11
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000004888 barrier function Effects 0.000 claims description 61
- 238000009792 diffusion process Methods 0.000 claims description 61
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 24
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 16
- 239000011148 porous material Substances 0.000 claims description 13
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 12
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 12
- 229960000583 acetic acid Drugs 0.000 claims description 8
- FPCJKVGGYOAWIZ-UHFFFAOYSA-N butan-1-ol;titanium Chemical compound [Ti].CCCCO.CCCCO.CCCCO.CCCCO FPCJKVGGYOAWIZ-UHFFFAOYSA-N 0.000 claims description 8
- 239000012362 glacial acetic acid Substances 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 7
- WFKAJVHLWXSISD-UHFFFAOYSA-N isobutyramide Chemical compound CC(C)C(N)=O WFKAJVHLWXSISD-UHFFFAOYSA-N 0.000 claims description 6
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 5
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 4
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 4
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical group [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 238000011010 flushing procedure Methods 0.000 claims description 3
- 235000019270 ammonium chloride Nutrition 0.000 claims description 2
- 229920002678 cellulose Polymers 0.000 claims description 2
- 239000001913 cellulose Substances 0.000 claims description 2
- FDPIMTJIUBPUKL-UHFFFAOYSA-N dimethylacetone Natural products CCC(=O)CC FDPIMTJIUBPUKL-UHFFFAOYSA-N 0.000 claims description 2
- 238000001471 micro-filtration Methods 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 238000001223 reverse osmosis Methods 0.000 claims description 2
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 2
- 235000011152 sodium sulphate Nutrition 0.000 claims description 2
- 239000004408 titanium dioxide Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 1
- 239000002105 nanoparticle Substances 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 8
- 229940124530 sulfonamide Drugs 0.000 abstract 8
- 150000003456 sulfonamides Chemical class 0.000 abstract 8
- 229920000265 Polyparaphenylene Polymers 0.000 abstract 7
- -1 polyphenylene Polymers 0.000 abstract 7
- 238000002715 modification method Methods 0.000 abstract 2
- 238000002791 soaking Methods 0.000 abstract 2
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 abstract 1
- 229920006389 polyphenyl polymer Polymers 0.000 abstract 1
- 230000004048 modification Effects 0.000 description 12
- 238000012986 modification Methods 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 8
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 6
- 238000011161 development Methods 0.000 description 5
- 238000011160 research Methods 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000005266 casting Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000003373 anti-fouling effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- 230000000845 anti-microbial effect Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The present invention relates to a polyphenylene sulfonamide separation membrane and its modification method by using nano titanium dioxide. Said polyphenylene sulfonamide separation membrane is made up by using (by wt%) 5%-20% of polyphenylene sulfonamide, 78%-94% of organic solvent and 1%-5% of pore-forming agent through a certain preparation process. Its modification method includes the following steps: a), soaking the polyphenylene sulfonamide separation membrane in concentrated sulfuric acid for 1-3hr, then cleaning said polyphenylene sulfonamide separation membrane by using deionized water; and b) soaking the polyphenylene sulfonamide separation membrane in the nano titanium dioxide sol for 5-15min, finally using deionized water to wash said polyphenylene sulfonamide separation membrane so as to obtain the invented nano titaminum dioxide modified polyphenyl sulfonamide separation membrane.
Description
Technical field
The present invention relates to a kind of macromolecule organic separation membrane and method of modifying thereof, be specifically related to a kind of polysulfonamides diffusion barrier and utilize the method for nano titanium oxide its modification.
Background technology
Water is the valuable source that the mankind depend on for existence and development.China's water resources ownership per capita is 2200m
3, be 1/4 of world average level only, belong to water scarcity country.The municipal wastewater treatment plant effluent quality does not satisfy " water standard of reclaimed water ", and its direct discharging also can cause the eutrophication of water body, has both caused the significant wastage of water resource, has brought the serious environmental pollution again.The municipal sewage as a resource technology both can have been opened up city second water resource, can alleviate water environment pollution again, was that urban sustainable development presses for one of new and high technology of research.
Along with the development of membrane material and membrane technology, membrane bioreactor (MBR) wastewater treatment and reuse technology can overcome the deficiency of other reusing sewage technology preferably in recent years.MBR technology is compared with traditional biologic treating technique as a kind of emerging efficient biological wastewater treatment technology, and the detersive efficiency height does not have suspension in the water outlet; Stable effluent quality; Floor space is little; Biodegradation to some hardly degraded organic substance is very favourable; Surplus sludge volume is few; Disposal costs is low; Digestion power is strong; Compact conformation; Be easy to control and operational management automatically.Particularly it is having more potentiality aspect waste water reclaiming and the reuse.
Ultrafiltration membrane bioreactor (Ultrafiltration Membrane Bioreactor is called for short UMBR) is a kind of novel water technology that the milipore filter isolation technics is combined with bioreactor.UMBR was attempted the earliest the latter stage sixties, and people such as Smith use it for filter activity mud, thereby had begun its research of disposing of sewage.UMBR has and does not establish secondary sedimentation tank, is not afraid of sludge bulking, the treatment effeciency height, realizes integrated automatic control, the easy advantage of design operation operation easily, but also exist shortcomings such as the diffusion barrier flux is little, the life-span short, easy obstruction, apply being very restricted.
Eliminating film, to pollute the most basic and direct approach be to research and develop efficiently, high strength, have the membrane material of better anti-fouling performance.Therefore the organic milipore filter modification of macromolecule is become the main direction of people's research to strengthen its separating property and resistance tocrocking.Improve the antifouling property of film, reduce concentration polarization, keep the stable and prolongation membrane lifetime of film properties, strengthen the efficient of film, saving energy is one of main trend of development of membrane bioreactor.And practice also shows, the stronger film of exploitation contamination resistance is the key point of membrane bioreactor to the higher level development.
Milipore filter is applied to the normal film blockage problem that takes place in the membrane bioreactor (MBR).Film pollutes and generally derives from cake layer, dissolubility organic matter and three aspects of microbial contamination, and wherein microorganism is the main cause that film pollutes.
Summary of the invention
In order to solve the microbiological pollution of milipore filter, the invention provides a kind of polysulfonamides diffusion barrier and utilize the method for nano titanium oxide its modification.
Polysulfonamides diffusion barrier of the present invention is made by 5%~20% polysulfonamides, 78%~94% organic solvent, 1%~5% pore former according to percentage by weight.
Utilize nano titanium oxide to be: a, the polysulfonamides diffusion barrier to be immersed in 1~3h in the concentrated sulfuric acid to the method that above-mentioned polysulfonamides diffusion barrier carries out modification, rinse well with deionized water then, described diffusion barrier is made by 5%~20% polysulfonamides, 78%~94% organic solvent, 1%~5% pore former according to percentage by weight; B, the polysulfonamides diffusion barrier is immersed in 5~15min in the nano titanic oxide sol, with removing the ionized water flushing, makes nano-titanium dioxide modified polysulfonamides diffusion barrier at last.
Nano titanium oxide has good photocatalytic oxidation properties, can suppress the generation that membrane micro pollutes under the irradiation of ultraviolet light effectively.The present invention utilizes nano titanium oxide that the polysulfonamides diffusion barrier is carried out modification, polysulfonamides diffusion barrier after the modification has not only kept the original good characteristic of polysulfonamides diffusion barrier, but also improved the surface property of polysulfonamides diffusion barrier, improved antimicrobial pollution capacity.The present invention has following advantage:
(1) film-forming process is simple, ripe, is easy to industrialization;
(2) flux of the polysulfonamides diffusion barrier after the modification improves 10%;
(3) the polysulfonamides diffusion barrier after the modification has improved the contamination resistance of film, will prolong 25% service life;
(4) the polysulfonamides diffusion barrier after the modification does not change the characteristic of polysulfonamides diffusion barrier, and preparation cost improves seldom.
The specific embodiment
The specific embodiment one: the polysulfonamides diffusion barrier of present embodiment is made by 5%~20% polysulfonamides, 78%~94% organic solvent, 1%~5% pore former according to percentage by weight.
In the present embodiment, described pore former is calcium nitrate, lithium chloride, ammonium chloride, sodium sulphate or PEG.
In the present embodiment, described organic solvent is N-N dimethylacetylamide, dimethylacetylamide, dimethyl formamide or acetone.
In the present embodiment, the molecular weight of described polysulfonamides is 10000~1000000 dalton.
In the present embodiment, described polysulfonamides diffusion barrier is flat sheet membrane, tubular membrane, hollow cellulose film, capillary-pipe film, spiral wound membrane, micro-filtration membrane, diffusion barrier, reverse osmosis membrane or NF membrane.
The specific embodiment two: what present embodiment and the specific embodiment one were different is that the polysulfonamides diffusion barrier of present embodiment is made by 18% polysulfonamides, 80% organic solvent, 2% pore former according to percentage by weight.
The specific embodiment three: what present embodiment and the specific embodiment one were different is that the polysulfonamides diffusion barrier of present embodiment is made by 6% polysulfonamides, 90% organic solvent, 4% pore former according to percentage by weight.
The specific embodiment four: what present embodiment and the specific embodiment one were different is that the polysulfonamides diffusion barrier of present embodiment is made by 10% polysulfonamides, 87% organic solvent, 3% pore former according to percentage by weight.
The specific embodiment five: present embodiment prepares nano-titanium dioxide modified polysulfonamides diffusion barrier according to following step:
1, the polysulfonamides after will making with extra care is dissolved in the organic solvent, adds pore former immediately, stirs the casting solution that homogeneous phase is made in also heating (30~50 ℃);
2, at room temperature leave standstill slaking, deaeration 1d;
3, make film under 20~30 ℃ of conditions, natural evaporation 30s puts into deionized water with the film of making then, and gel becomes the polysulfonamides diffusion barrier;
4, the preparation of nano titanic oxide sol:
(1) at room temperature gets in 2/3 the absolute ethyl alcohol that a certain amount of butyl titanate is dissolved in aequum, form A liquid;
(2) 1/3 the absolute ethyl alcohol of getting aequum in addition adds secondary deionized water, adds a certain amount of glacial acetic acid again and mixes and form B liquid;
(3) A liquid is poured in the beaker, 30~45 ℃ of water-bath heating dropwise add B liquid under stirring, and between 1~3, make nano titanic oxide sol with the salt acid for adjusting pH value; Butyl titanate wherein: absolute ethyl alcohol: secondary deionized water: the mol ratio of glacial acetic acid is 1: 10: 2: 1;
5, the polysulfonamides diffusion barrier is immersed in 1~3h in 20% the concentrated sulfuric acid, rinses well with deionized water then;
6, the polysulfonamides diffusion barrier is immersed in 5~15min in the nano titanic oxide sol, the back makes nano-titanium dioxide modified polysulfonamides diffusion barrier with removing the ionized water flushing.
In the present embodiment, the particle diameter of described titanium dioxide granule is 1nm~10 μ m.
The specific embodiment six: present embodiment prepares nano-titanium dioxide modified polysulfonamides diffusion barrier according to following step:
One, the preparation of polysulfonamides diffusion barrier:
The polysulfonamides diffusion barrier precipitates polysulfonamides solution in deionized water, displace the solvent dimethyl formamide, and is dry down at 50 ℃ then.Get the polysulfonamides 10g after making with extra care, be dissolved in the dimethylacetylamide organic solvent of 87g, add pore former Ca (NO again
3)
2H
2O3g, stirring is also heated the casting solution of making homogeneous phase under 50 ℃.At room temperature leave standstill behind slaking, the deaeration 1d knifing at room temperature, natural evaporation 30s adds deionized water and displaces additive and solvent, and gel becomes the polysulfonamides diffusion barrier.
Two, the preparation of nano titanic oxide sol:
(1) at room temperature gets in 2/3 the absolute ethyl alcohol that a certain amount of butyl titanate is dissolved in aequum, form A liquid; (2) 1/3 the absolute ethyl alcohol of getting aequum in addition adds secondary deionized water, adds a certain amount of glacial acetic acid again and mixes and form B liquid; (3) A liquid is poured in the beaker, 35 ℃ of water-bath heating dropwise add B liquid under stirring, and are 2 with the salt acid for adjusting pH value, make nano titanic oxide sol; Butyl titanate wherein: absolute ethyl alcohol: secondary deionized water: the mol ratio of glacial acetic acid is 1: 10: 2: 1.
Three, modification:
The polysulfonamides diffusion barrier is immersed in 2h in 20% the concentrated sulfuric acid, rinses well with deionized water; Then the polysulfonamides diffusion barrier is immersed in 10min in the nano titanic oxide sol, uses deionized water rinsing at last, make nano-titanium dioxide modified polysulfonamides diffusion barrier.
The specific embodiment seven: present embodiment prepares nano-titanium dioxide modified polysulfonamides diffusion barrier according to following step:
One, the preparation of polysulfonamides diffusion barrier:
The polysulfonamides diffusion barrier precipitates polysulfonamides solution in deionized water, displace the solvent dimethyl formamide, and is dry down at 40 ℃ then.Get the polysulfonamides 15g after making with extra care, be dissolved in the N-N dimethylacetylamide organic solvent of 84g, add pore former lithium chloride 1g again, stir also and heat the casting solution of making homogeneous phase down at 50 ℃.At room temperature leave standstill behind slaking, the deaeration 1d knifing at room temperature, natural evaporation 30s adds deionized water and displaces additive and solvent, and gel becomes the polysulfonamides diffusion barrier.
Two, the preparation of nano titanic oxide sol:
(1) at room temperature gets in 2/3 the absolute ethyl alcohol that a certain amount of butyl titanate is dissolved in aequum, form A liquid; (2) 1/3 the absolute ethyl alcohol of getting aequum in addition adds secondary deionized water, adds a certain amount of glacial acetic acid again and mixes and form B liquid; (3) A liquid is poured in the beaker, 35 ℃ of water-bath heating dropwise add B liquid under stirring, and are 1.5 with the salt acid for adjusting pH value, make nano titanic oxide sol; Butyl titanate wherein: absolute ethyl alcohol: secondary deionized water: the mol ratio of glacial acetic acid is 1: 10: 2: 1.
Three, modification:
The polysulfonamides diffusion barrier is immersed in 1.5h in 20% the concentrated sulfuric acid, rinses well with deionized water; Then the polysulfonamides diffusion barrier is immersed in 15min in the nano titanic oxide sol, uses deionized water rinsing at last, make nano-titanium dioxide modified polysulfonamides diffusion barrier.
Claims (10)
1, a kind of polysulfonamides diffusion barrier is characterized in that described diffusion barrier made by following compositions according to percentage by weight: 5%~20% polysulfonamides, 78%~94% organic solvent, 1%~5% pore former.
2, polysulfonamides diffusion barrier according to claim 1 is characterized in that described pore former is calcium nitrate, lithium chloride, ammonium chloride, sodium sulphate or PEG.
3, polysulfonamides diffusion barrier according to claim 1 is characterized in that described organic solvent is N-N dimethylacetylamide, dimethylacetylamide, dimethyl formamide or acetone.
4, polysulfonamides diffusion barrier according to claim 1, the molecular weight that it is characterized in that described polysulfonamides is 10000~1000000 dalton.
5, polysulfones amide diffusion barrier according to claim 1 is characterized in that described polysulfonamides diffusion barrier is micro-filtration membrane, diffusion barrier, reverse osmosis membrane or NF membrane.
6, polysulfonamides diffusion barrier according to claim 1 is characterized in that described polysulfonamides diffusion barrier is flat sheet membrane, tubular membrane, hollow cellulose film, capillary-pipe film or spiral wound membrane.
7, a kind of method of utilizing nano-titanium dioxide modified polysulfonamides diffusion barrier, it is characterized in that described method is: a, the polysulfonamides diffusion barrier is immersed in 1~3h in the concentrated sulfuric acid, rinse well with deionized water then, described diffusion barrier is made by 5%~20% polysulfonamides, 78%~94% organic solvent, 1%~5% pore former according to percentage by weight; B, the polysulfonamides diffusion barrier is immersed in 5~15min in the nano titanic oxide sol, with removing the ionized water flushing, makes nano-titanium dioxide modified polysulfonamides diffusion barrier at last.
8, the preparation method of nano-titanium dioxide modified polysulfonamides diffusion barrier according to claim 7, it is characterized in that described nano titanic oxide sol prepares according to following steps: at room temperature get in 2/3 the absolute ethyl alcohol that a certain amount of butyl titanate is dissolved in aequum (1), forms A liquid; (2) 1/3 the absolute ethyl alcohol of getting aequum in addition adds secondary deionized water, adds a certain amount of glacial acetic acid again and mixes and form B liquid; (3) A liquid is poured in the beaker, 30~45 ℃ of water-bath heating dropwise add B liquid under stirring, and between 1~3, make nano titanic oxide sol with the salt acid for adjusting pH value.
9, the preparation method of nano-titanium dioxide modified polysulfonamides diffusion barrier according to claim 7, the particle diameter that it is characterized in that described titanium dioxide nanoparticle is 1nm~10 μ m.
10, the preparation method of nano-titanium dioxide modified polysulfonamides diffusion barrier according to claim 7 is characterized in that the butyl titanate among the described nano titanic oxide sol preparation method: absolute ethyl alcohol: secondary deionized water: the mol ratio of glacial acetic acid is 1: 10: 2: 1.
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101912741A (en) * | 2010-08-05 | 2010-12-15 | 贵阳时代沃顿科技有限公司 | Polyamide composite reverse osmosis membrane containing nano materials |
CN102505351A (en) * | 2011-11-16 | 2012-06-20 | 上海大学 | Method for preparing polysulfonamide separating films by aid of electrostatic spinning |
CN102698611A (en) * | 2012-06-27 | 2012-10-03 | 上海大学 | Method for preparing polysulfone amide hollow fiber separation membrane by wet spinning |
CN103044917A (en) * | 2013-01-07 | 2013-04-17 | 中国科学院青岛生物能源与过程研究所 | Polyarylsulfone amido porous membrane, and preparation method and application thereof |
CN105435647A (en) * | 2014-08-22 | 2016-03-30 | 中国石油化工股份有限公司 | A preparing method of an antifouling reverse osmosis membrane and the reverse osmosis prepared by the method |
CN108380061A (en) * | 2018-03-10 | 2018-08-10 | 张玲 | A kind of method that boracic maceration extract prepares ultrafiltration membrane |
CN114053890A (en) * | 2021-12-09 | 2022-02-18 | 天津工业大学 | High-performance alkali-resistant nanofiltration membrane and preparation method thereof |
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2006
- 2006-09-04 CN CNB2006100104896A patent/CN100427190C/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101912741A (en) * | 2010-08-05 | 2010-12-15 | 贵阳时代沃顿科技有限公司 | Polyamide composite reverse osmosis membrane containing nano materials |
CN102505351A (en) * | 2011-11-16 | 2012-06-20 | 上海大学 | Method for preparing polysulfonamide separating films by aid of electrostatic spinning |
CN102698611A (en) * | 2012-06-27 | 2012-10-03 | 上海大学 | Method for preparing polysulfone amide hollow fiber separation membrane by wet spinning |
CN103044917A (en) * | 2013-01-07 | 2013-04-17 | 中国科学院青岛生物能源与过程研究所 | Polyarylsulfone amido porous membrane, and preparation method and application thereof |
CN103044917B (en) * | 2013-01-07 | 2015-09-09 | 中国科学院青岛生物能源与过程研究所 | A kind of aromatic polysulfonamide Quito pore membrane and its preparation method and application |
CN105435647A (en) * | 2014-08-22 | 2016-03-30 | 中国石油化工股份有限公司 | A preparing method of an antifouling reverse osmosis membrane and the reverse osmosis prepared by the method |
CN108380061A (en) * | 2018-03-10 | 2018-08-10 | 张玲 | A kind of method that boracic maceration extract prepares ultrafiltration membrane |
CN114053890A (en) * | 2021-12-09 | 2022-02-18 | 天津工业大学 | High-performance alkali-resistant nanofiltration membrane and preparation method thereof |
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