CN1257747A - Process for modifying reverse osmosis composite membrane by inner interface adsorption of surfactant - Google Patents
Process for modifying reverse osmosis composite membrane by inner interface adsorption of surfactant Download PDFInfo
- Publication number
- CN1257747A CN1257747A CN 98120000 CN98120000A CN1257747A CN 1257747 A CN1257747 A CN 1257747A CN 98120000 CN98120000 CN 98120000 CN 98120000 A CN98120000 A CN 98120000A CN 1257747 A CN1257747 A CN 1257747A
- Authority
- CN
- China
- Prior art keywords
- surfactant
- composite membrane
- liquid
- reverse osmosis
- tween
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
A surfactant adsorption process for modifying the reverse osmotic composite membrane is characterized by that said reverse osmotic composite membrane is prepared through preparing porous bearing layer, adsorbing surfactant on said porous bearing layer and forming super-thin function layer. The resultant composite membrane has high salt-intercepting rate up to 94-97% increased by 10% or more and high water-ouptutting rate up to 0.55-1.02 sq.m/sq.m.d increased by over 80%. Its advantages are mild reaction condition, simple and safe operation, no pollution and no influence on the mechanical stability of porous bearing layer.
Description
The invention belongs to the modifying reverse osmosis composite membrane by inner interface adsorption of surfactant method.
Reverse osmosis membrane is used for the dried up and salt of branch, and composite membrane hydrophilic functional group's the increase and the raising of charge all help improving separative efficiency.1987, Allegrezza is at Ultrapure Water (4, reported a series of 7:53) and had high flux, good chlorine resistance and the weak solution of monovalent salt is had the sulfonated polysulfone membrane of good salt-stopping rate, having utilized sulfonic group is the principle of the strongly hydrophilic group that exists with ionic species; 1996, Journal ofMembrane Science (114:39) report Ashish Kulkarni can improve its separating property with processing polyamide composite films such as hydrofluoric acid, because acid makes polyamide ultrathin functional layer generation hydrolysis, carboxyl that produces and the amino hydrophilic radical that is the ionic species existence, the composite membrane performance improves; But the time that the modification of acid treatment composite membrane needs is long, and excessively hydrolysis will make the salt-stopping rate of composite membrane descend significantly, and acid treatment descends the mechanical performance of composite membrane, and the toxicity and the corrosivity of acid are very big, and equipment is required harshness; The chemical stability of SPSF is not as polysulfones.
The object of the invention provides a kind of modifying reverse osmosis composite membrane by inner interface adsorption of surfactant method, and the preparation of composite membrane is divided into preparation, absorption, the ultrathin functional layer formation three phases of surfactant on porous support layer of porous support layer in the inventive method.
The chemical element of the inner boundary in the composite membrane between ultrathin functional layer and porous support layer is formed and charge influences the composite membrane performance; Surfactant forms the selective fixed to adsorption layer of densification by functional group on the porous support layer epidermal area; Non-ionic surface active agent is introduced hydrophilic radical and is improved the hydrophily at interface with the interaction of raising with water; Ionic surfactant has not only been introduced the hydrophilic functional group, and improves salt-stopping rate by the Coulomb repulsion effect; The introducing of the fine and close adsorption layer of inner boundary surfactant has also changed the interface binding energy between ultrathin functional layer and the porous support layer.
The present invention adopts following steps to form reverse osmosis composite membrane:
1). the preparation of asymmetric porous support layer
Casting solution is dissolved in N by 13.5%～18% bisphenol a polysulfone and 2%～10% tributyl phosphate, and dinethylformamide is formed, and prepares asymmetric porous membrane by the Loeb-sourirajan method on polyester non-woven fabric;
2). the formation of fine and close adsorption layer on the porous support layer
With different surfactant obtained aqueous solutions, the surfactant that is adopted has:
(1) nonionic surface active agent: Tween series
(2) have the amphoteric ionic surfactant of following array structure:
Here: R
1=H, CH
3, C
2H
5, C
3H
7, (C
6H
5-R
7)
m, R
7=H, O, SO
2,
CO，CH
2，m＝0～3
R
2＝CH
3，C
2H
5，C
3H
7，H
n(n＝0，1)
R
3、R
4、R
5、R
6＝H，CH
3
M＝Na，K
The aqueous solution with Tween preparation 0.005～0.2ml/l, prepare the aqueous solution of 0.005～5g/l with the amphoteric ionic surfactant of said structure, the temperature of treatment fluid is 10～40 ℃, make the fine and close epidermal area of porous support layer smooth be dipped in this treatment fluid 1～24 hour, with the porous support layer after a large amount of pure water drip washing processing, when with amphoteric ionic surfactant, be washed till the electrical conductivity＜10 μ s/cm of leacheate;
3). the formation of ultrathin functional layer
Ultrathin functional layer forms on the fine and close epidermal area after the processing, and the complex liquid of ultrathin functional layer is divided into A liquid: 2%～2.5 m-phenylene diamine (MPD) aqueous solution; B liquid: the hexane solution of 0.1%～0.25% acyl chlorides, wherein, the ratio of diacid chloride and three acyl chlorides is 2: 3～3: 2; C liquid: 0.1%～0.5% polyvinyl alcohol water solution; Porous support layer was soaked A liquid 3～6 minutes, dry, soaked B liquid 0.5～1.5 minute, soaked C liquid again 0.5～1.5 minute, at last in 97 ± 5 ℃ of following post processings 5～10 minutes;
Composite membrane performance with the inventive method preparation: salt-stopping rate 94%～97%, producing water ratio 0.55m
3/ m
2.d～1.02m
3/ m
2.d; Salt-stopping rate raising rate relatively reaches more than 10%, and producing water ratio raising rate relatively is up to more than 80%;
The gentle easily control of reaction condition of the present invention, easy to operate and safe, reagent is cheap and easy to get, and is pollution-free, and equipment is not had specific (special) requirements; Owing to only be surface absorption, the physical mechanical stability of porous support layer there is not influence, do not influence the chemical stability of composite membrane simultaneously; The present invention makes reverse osmosis composite membrane obtain good separating property under simple formulation and process conditions, and prepared reverse osmosis composite membrane performance has reached higher level.
Embodiment provided by the invention is as follows:
Embodiment 1: casting solution bisphenol a polysulfone concentration 14%, tributyl phosphate concentration 2%; The surfactant Tween-80 aqueous solution of 0.01ml/l, 15 ℃ of temperature, the processing time is 12 hours, A liquid 2% m-phenylene diamine (MPD), B liquid 0.2% acyl chlorides, wherein isophthaloyl chloride: trimesoyl chloride=3: 2, C liquid 0.3% polyvinyl alcohol water solution, soaked A liquid 3 minutes, B liquid 1 minute, C liquid 1 minute, post processing is following 6 minutes in 97 ± 2 ℃, gained composite membrane performance: salt-stopping rate=96.6%, producing water ratio=0.77m
3/ m
2.d.
Embodiment 2: the concentration that only changes the Tween-80 aqueous solution is 0.1ml/l, and all the other conditions are with 1, gained composite membrane performance: salt-stopping rate=95.0%, producing water ratio=0.61m
3/ m
2.d.
Embodiment 3: select Tween-60 for use, its concentration is 0.05ml/l, and the temperature of its aqueous solution is 30 ℃, and all the other conditions are with 1, gained composite membrane performance: salt-stopping rate=96.0%, producing water ratio=0.68m
3/ m
2.d.
Embodiment 4: casting solution bisphenol a polysulfone concentration 13.5%, tributyl phosphate concentration 2%; The surfactant Tween-20 aqueous solution of 0.05ml/l, 20 ℃ of temperature, the processing time is 12 hours, A liquid 2.5% m-phenylene diamine (MPD), B liquid 0.2% acyl chlorides, wherein isophthaloyl chloride: trimesoyl chloride=1: 1, C liquid 0.3% polyvinyl alcohol water solution, soaked A liquid 3 minutes, B liquid 1 minute, C liquid 1 minute, post processing is following 6 minutes in 97 ± 2 ℃, gained composite membrane performance: salt-stopping rate=96.2%, producing water ratio=0.50m
3/ m
2.d.
Embodiment 5: surfactant is sodium sulfanilate: R
1=H, R
2There is not R
3=R
4=R
5=R
6=H, concentration is 0.01g/l, all the other conditions are with 1, gained composite membrane performance: salt-stopping rate=94.2%, producing water ratio=0.77m
3/ m
2.d.
Embodiment 6: the concentration that only changes sodium sulfanilate is 2g/l, and all the other conditions are with 1, gained composite membrane performance: salt-stopping rate=96.8%, producing water ratio=1.02m
3/ m
2.d.
Embodiment 7: the concentration that only changes sodium sulfanilate is 3.5g/l, and all the other conditions are with 1, gained composite membrane performance: salt-stopping rate=97.0%, producing water ratio=0.77m
3/ m
2.d.
Embodiment 8: the casting solution bisphenol A concentration is 15%, tributyl phosphate concentration 5% is selected sulfanilic acid potassium for use, and its concentration is 0.1g/l, aqueous temperature is 35 ℃, in 4 hours processing times, soaked A liquid 5 minutes, B liquid 40 seconds, C liquid 1.5 minutes, post processing in 98 ± 2 ℃ following 8 minutes, gained composite membrane performance: salt-stopping rate=96.4%, producing water ratio=0.75m
3/ m
2.d.
Embodiment 9: selecting structure for use is R
3=R
5=CH
3, R
4=R
6=H, concentration is the dimethyl sodium sulfanilate aqueous solution of 0.1g/l, and all the other conditions are with 1, and gained composite membrane performance is: salt-stopping rate=95.0%, producing water ratio=0.65m
3/ m
2.d.
Embodiment 10: selecting structure for use is R
1=R
2=CH
3, R
3=R
4=R
5=R
6=H, concentration is the amphoteric ionic surfactant aqueous solution of 1g/l, its temperature is 40 ℃, 4 hours processing times, gained composite membrane performance: salt-stopping rate=96.0%, producing water ratio=0.75m
3/ m
2.d.
Claims (4)
1. modifying reverse osmosis composite membrane by inner interface adsorption of surfactant method is characterized in that adopting following steps to form reverse osmosis composite membrane:
1). the preparation of asymmetric porous support layer
Casting solution is dissolved in N by 13.5%～18% bisphenol a polysulfone and 2%～10% tributyl phosphate, and dinethylformamide is formed, and prepares asymmetric porous membrane by the Loeb-sourirajan method on polyester non-woven fabric;
2). the formation of fine and close adsorption layer on the porous support layer
With different surfactant obtained aqueous solutions, the surfactant that is adopted has:
(1) nonionic surface active agent: Tween series
(2) have the amphoteric ionic surfactant of following array structure:
Here: R
1=H, CH
3, C
2H
5, C
3H
7, (C
6H
5-R
7)
m, R
7=H, O, SO
2,
CO，CH
2，m＝0～3
R
2＝CH
3，C
2H
5，C
3H
7，H
n(n＝0，1)
R
3、R
4、R
5、R
6＝H，CH
3
M＝Na，K
The aqueous solution with Tween preparation 0.005～0.2ml/l, prepare the aqueous solution of 0.005～5g/l with the amphoteric ionic surfactant of said structure, the temperature of treatment fluid is 10～40 ℃, make the fine and close epidermal area of porous support layer smooth be dipped in this treatment fluid 1～24 hour, with the porous support layer after a large amount of pure water drip washing processing, when with amphoteric ionic surfactant, be washed till the electrical conductivity＜10 μ s/cm of leacheate;
3). the formation of ultrathin functional layer
Ultrathin functional layer forms on the fine and close epidermal area after the processing, and the complex liquid of ultrathin functional layer is divided into A liquid: 2%～2.5 m-phenylene diamine (MPD) aqueous solution; B liquid: the hexane solution of 0.1%～0.25% acyl chlorides, wherein, the ratio of diacid chloride and three acyl chlorides is 2: 3～3: 2; C liquid: 0.1%～0.5% polyvinyl alcohol water solution; Porous support layer was soaked A liquid 3～6 minutes, dry, soaked B liquid 0.5～1.5 minute, soaked C liquid again 0.5～1.5 minute, at last in 97 ± 5 ℃ of following post processings 5～10 minutes;
2. modifying reverse osmosis composite membrane by inner interface adsorption of surfactant method as claimed in claim is characterized in that described non-ionic surface active agent Tween series is Tween-20, Tween-60, Tween-80;
3. modifying reverse osmosis composite membrane by inner interface adsorption of surfactant method as claimed in claim is characterized in that amphoteric ionic surfactant R
1=H, CH
3
4. modifying reverse osmosis composite membrane by inner interface adsorption of surfactant method as claimed in claim is characterized in that amphoteric ionic surfactant R
2=CH
3, Hn, n=0,1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98120000A CN1114471C (en) | 1998-12-24 | 1998-12-24 | Process for modifying reverse osmosis composite membrane by inner interface adsorption of surfactant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98120000A CN1114471C (en) | 1998-12-24 | 1998-12-24 | Process for modifying reverse osmosis composite membrane by inner interface adsorption of surfactant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1257747A true CN1257747A (en) | 2000-06-28 |
| CN1114471C CN1114471C (en) | 2003-07-16 |
Family
ID=5226554
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98120000A Expired - Fee Related CN1114471C (en) | 1998-12-24 | 1998-12-24 | Process for modifying reverse osmosis composite membrane by inner interface adsorption of surfactant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1114471C (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100398467C (en) * | 2006-04-20 | 2008-07-02 | 上海交通大学 | Organic inductive treatment method for reverse osmosis concentrated solution |
| CN100515550C (en) * | 2003-06-02 | 2009-07-22 | Ge奥斯莫尼克斯公司 | Materials and methods for processing non-aqueous mixtures |
| CN100540126C (en) * | 2006-08-30 | 2009-09-16 | 贵阳时代汇通膜科技有限公司 | The production method of light-pollution reverse osmosis composite film |
| CN101804304A (en) * | 2010-04-09 | 2010-08-18 | 北京化工大学 | Modification method of reverse osmosis membrane surface |
| CN102363113A (en) * | 2011-09-09 | 2012-02-29 | 贵阳时代沃顿科技有限公司 | Method for strengthening contamination resistance of reverse osmosis membrane |
| CN102423646A (en) * | 2011-08-17 | 2012-04-25 | 浙江大学 | Nano-filtration membrane for separating organic compounds and salts, and preparation method thereof |
| CN102553460A (en) * | 2012-02-22 | 2012-07-11 | 富阳梅伊韦尔环保设备有限公司 | Method for preparing pollution-resistant low-pressure reverse osmosis membrane |
| CN103736406A (en) * | 2013-12-31 | 2014-04-23 | 天津工业大学 | Anti-pollution and easily-washable polyamide reverse osmosis composite membrane and preparation method of membrane |
| CN109499395A (en) * | 2018-11-16 | 2019-03-22 | 杭州华滤膜科技有限公司 | A kind of preparation method of the reverse osmosis seawater film of high throughput |
| CN109499388A (en) * | 2010-05-21 | 2019-03-22 | Z纳米有限责任公司 | Self assembly surfactant structure |
| CN111249909A (en) * | 2020-04-15 | 2020-06-09 | 内蒙古科泰隆达环保科技有限公司 | Modification method of reverse osmosis membrane for drinking water purification |
| US11401179B2 (en) | 2010-05-21 | 2022-08-02 | Diamond Gold Investors, Llc | Self-assembled surfactant structures |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5794307A (en) * | 1980-12-03 | 1982-06-11 | Nitto Electric Ind Co Ltd | Treatment of dry composite semipermeable membrane |
| JPS6297980A (en) * | 1985-10-23 | 1987-05-07 | 三菱レイヨン株式会社 | Composite hollow fiber membrane |
| US5693227A (en) * | 1994-11-17 | 1997-12-02 | Ionics, Incorporated | Catalyst mediated method of interfacial polymerization on a microporous support, and polymers, fibers, films and membranes made by such method |
-
1998
- 1998-12-24 CN CN98120000A patent/CN1114471C/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100515550C (en) * | 2003-06-02 | 2009-07-22 | Ge奥斯莫尼克斯公司 | Materials and methods for processing non-aqueous mixtures |
| CN100398467C (en) * | 2006-04-20 | 2008-07-02 | 上海交通大学 | Organic inductive treatment method for reverse osmosis concentrated solution |
| CN100540126C (en) * | 2006-08-30 | 2009-09-16 | 贵阳时代汇通膜科技有限公司 | The production method of light-pollution reverse osmosis composite film |
| CN101804304A (en) * | 2010-04-09 | 2010-08-18 | 北京化工大学 | Modification method of reverse osmosis membrane surface |
| CN109499388A (en) * | 2010-05-21 | 2019-03-22 | Z纳米有限责任公司 | Self assembly surfactant structure |
| US11401179B2 (en) | 2010-05-21 | 2022-08-02 | Diamond Gold Investors, Llc | Self-assembled surfactant structures |
| CN102423646A (en) * | 2011-08-17 | 2012-04-25 | 浙江大学 | Nano-filtration membrane for separating organic compounds and salts, and preparation method thereof |
| CN102423646B (en) * | 2011-08-17 | 2013-08-07 | 浙江大学 | Nano-filtration membrane for separating organic compounds and salts, and preparation method thereof |
| CN102363113A (en) * | 2011-09-09 | 2012-02-29 | 贵阳时代沃顿科技有限公司 | Method for strengthening contamination resistance of reverse osmosis membrane |
| CN102553460A (en) * | 2012-02-22 | 2012-07-11 | 富阳梅伊韦尔环保设备有限公司 | Method for preparing pollution-resistant low-pressure reverse osmosis membrane |
| CN102553460B (en) * | 2012-02-22 | 2014-06-25 | 浙江美易膜科技有限公司 | Method for preparing pollution-resistant low-pressure reverse osmosis membrane |
| CN103736406B (en) * | 2013-12-31 | 2016-01-20 | 天津工业大学 | Polyamide reverse osmosis composite film of a kind of antipollution easy cleaning and preparation method thereof |
| CN103736406A (en) * | 2013-12-31 | 2014-04-23 | 天津工业大学 | Anti-pollution and easily-washable polyamide reverse osmosis composite membrane and preparation method of membrane |
| CN109499395A (en) * | 2018-11-16 | 2019-03-22 | 杭州华滤膜科技有限公司 | A kind of preparation method of the reverse osmosis seawater film of high throughput |
| CN111249909A (en) * | 2020-04-15 | 2020-06-09 | 内蒙古科泰隆达环保科技有限公司 | Modification method of reverse osmosis membrane for drinking water purification |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1114471C (en) | 2003-07-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1114471C (en) | Process for modifying reverse osmosis composite membrane by inner interface adsorption of surfactant | |
| CN101890315B (en) | Carbon nano tube-polymer composite nanofiltration membrane and preparation method thereof | |
| Qiu et al. | Synthesis of high flux forward osmosis membranes by chemically crosslinked layer-by-layer polyelectrolytes | |
| CN104209021A (en) | Preparation method of aromatic polyamide film modified by ZIF-8 type metal-organic framework material | |
| CN103537200B (en) | A kind of Cellulose acetate forward osmotic membrane and preparation method thereof | |
| CN103170257B (en) | Compound forward osmosis membrane and preparation method thereof | |
| CN111790277B (en) | Preparation method of high-performance reverse osmosis membrane for promoting growth of polyamide nano vesicles | |
| CN111992039B (en) | Method for preparing high-performance nanofiltration membrane by constructing ZIF-8 intermediate layer | |
| CN108409981A (en) | A kind of preparation method of modified metal organic frame and composite nanometer filtering film | |
| CN102794116A (en) | Mesoporous silicon dioxide sphere-polymer nano composite nano-filtration membrane and preparation method thereof | |
| WO2006038409A1 (en) | Process for producing semipermeable composite membrane | |
| CN101053779A (en) | Method for preparing hydrophilic low catching molecular composite ultrafiltering membrane | |
| CN110841494A (en) | Amphoteric composite forward osmosis membrane and preparation method and application thereof | |
| CN104785132A (en) | Composite lignin nanofiltration membrane and preparation method thereof | |
| CN112535955B (en) | Decolorizing membrane and preparation method and application thereof | |
| CN112999899A (en) | Renewable ultrathin multilayer composite forward osmosis membrane and preparation method and application thereof | |
| CN103785301B (en) | A kind of Cellulose acetate forward osmotic membrane material and preparation method thereof | |
| CN104548973A (en) | Preparation and catalytic regeneration of functionalized graphene oxide/polyether sulfone blended ultrafiltration membrane | |
| EP1007194A1 (en) | Polyion complex separation membrane with a double structure | |
| CN1277598C (en) | Microporous barrier and preparing method thereof | |
| Xia et al. | Ionic control of functional zeolitic imidazolate framework-based membrane for tailoring selectivity toward target ions | |
| CN1326599C (en) | Method for preparing fixed carrier compound membrane for CO2 separation by utilizing interfacial polymerization | |
| CN1257748A (en) | Alcohol-water system modifying process for inner interface of inverse osmosis membrane | |
| CN112516821B (en) | Dopamine and polyvinyl alcohol composite modified polysulfone forward osmosis membrane, preparation method and application | |
| CN114016285A (en) | Preparation method of functional nanofiber membrane for seawater desalination |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |