CN104474920B - A kind of flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane - Google Patents
A kind of flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane Download PDFInfo
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Abstract
The present invention discloses a kind of high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane, by cellulose acetate 7.0% ~ 26.0%(w/w), additive 2.0% ~ 16.0%(w/w), nano titanium oxide 0.1% ~ 5.0%(w/w), Graphene 0.05% ~ 0.1%(w/w) and dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE and acetone mixed solvent add dissolving tank in certain sequence, 25 ~ 90 DEG C of stirring and dissolving 3 ~ 15h, to full and uniform, obtain blended forward osmosis membrane casting solution; Backing material prepares high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane with phase inversion.Forward osmosis membrane 1M prepared by the present invention? NaCl does to drive liquid, deionized water makes material liquid, and in the testing time of 1h, pure water flux reaches 17.5L/m
2more than h, reverse flux salt is less than 3.0g/m
2h.
Description
Technical field
The present invention relates to technical field of membrane, especially relate to a kind of high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane.
Background technology
The scarcity of water resource has become the bottleneck of restriction social progress and economic development, and new water resource development also becomes global question of common concern.Because seawater resources on the earth are very abundant, desalinization has become the strategic choice solving water resources crisis.At present, business-like desalination technology mainly contains Re Fa and embrane method, reverse osmosis seawater desalting has become one of most important desalination technology, but the shortcomings such as its operating pressure is high, energy ezpenditure is large, film service life is shorter, Water Sproading rate is lower show the relatively little development space of hyperfiltration desalinization, make it the bottleneck encountering development.Becoming research emphasis and the focus of field of seawater desalination as the positive infiltration technology for solving this key issue and the low energy consumption of being born, high Water Sproading rate, having had important strategic importance to solution shortage of water resources problem.
Just permeate (forwardosmosis, FO) be a kind of membrane separation technique relying on film both sides osmotic pressure to drive, just day by day come into one's own, relevant Theory and applications research achieves larger progress, has been successfully applied to the fields such as desalinization, wastewater treatment, food medicine, the energy.Compared with counter-infiltration, positive infiltration technology has that Water Sproading rate is high, concentrated water discharge is few, fouling membrane is comparatively light, without the need to advantages such as external pressures, being expected to replace counter-infiltration becomes the purifying of water and the new way of desalination.At present, common forward osmosis membrane mainly contains three cellulose acetate membrane, cellulose diacetate film, polybenzimidazole membrane, polyamide composite film etc., commercialization degree is not high mainly lacks forward osmosis membrane of good performance and suitable driving liquid, and forward osmosis membrane is the key point of whole positive process of osmosis.Desirable forward osmosis membrane should have following characteristics: (1) fine and close, the cortex of low porosity, high salt-stopping rate; (2) cortex of film has good hydrophily, higher water flux; (3) supporting layer of film is as far as possible thin, and porosity is high; (4) alap interior concentration polarization; (5) higher mechanical strength; (6) higher resistance to chemical corrosion.These all with the material character of forward osmosis membrane and the structure of film closely related, membrane material and the forward osmosis membrane preparation method of visible function admirable are particularly important.Common forward osmosis membrane preparation method has interfacial polymerization, two selection tunic preparation method and NF membrane modification three kinds.In positive osmosis composite membrane prepared by interfacial polymerization, concentration polarization is more serious; Two selection tunic effectively reduces interior concentration polarization, but preparation technology is comparatively complicated; NF membrane Modified Membrane to the rejection of monovalent salt and water flux all lower; Therefore, need to develop new forward osmosis membrane preparation technology to improve the separating property of forward osmosis membrane.
Eighties of last century sixties, the external research having started positive infiltration technology, adopt the application study that existing reverse osmosis membrane or NF membrane are just being permeated, result proves that existing reverse osmosis membrane or NF membrane are difficult to use in positive process of osmosis, but also demonstrate the performance of forward osmosis membrane and membrane material simultaneously, membrane structure is closely related; Subsequently, all multimembrane scientific workers start basic research prepared by forward osmosis membrane.The research such as Tang has found the hydrophilic film material that can be used for preparing desirable forward osmosis membrane; QIANYANG, V.Kurdakova, KaiYuWang adopt polybenzimidazoles as raw material, have prepared forward osmosis membrane by phase inversion; SuiZhang etc. have then adopted L-S legal system for the CAM with ultra-thin selection layer, significantly reduce interior concentration polarization; Improve the water flux of forward osmosis membrane.The research group, Yip etc. of MenachemElimelech research group of Yale, Nanyang Technological University then respectively with polysulfones or polyether sulfone for membrane material preparation supports counterdie, prepare compound forward osmosis membrane by interfacial polymerization, all improve permeability of the membrane energy and separating property.JincaiSu etc. adopt phase inversion to prepare hollow fiber nanofiltration membrane, prepare forward osmosis membrane, improve the performance of film by heat treatment modification.Result of study shows, by selecting suitable membrane material, film preparation technique, and can the excellent forward osmosis membrane of processability.The research of the positive infiltration technology of China is started late, at present the domestic research aligning infiltration technology, no matter is film preparation or membrane process research, is still in the exploratory stage.Liu Leilei etc., Li Lili etc., Zhao wait the preparation condition exploring cellulose triacetate and cellulose diacetate forward osmosis membrane respectively quietly, have studied the impact of various factors on forward osmosis membrane performance, but cannot prepare can the forward osmosis membrane of business-like function admirable; The Synthesis and applications research of forward osmosis membrane still shoulders heavy responsibilities.The studying enlightenments in early stage we, utilize blending technology modified membrane, be expected to improve the water flux of forward osmosis membrane, salt-stopping rate, mechanical performance and anti-fouling performance.
Nano titanium oxide (nTiO
2) be a kind of amphoteric oxide of white powder, there is photocatalytic, can degrade gas chromatography and have microbe killing properties can, be subject to scholars and more and more pay close attention to, be widely used in solving various environmental problem; In addition, nano titanium oxide has larger specific area, also has hydrophily.Graphene has good surface-active and specific area, and make graphene oxide have extremely strong hydrophily, simultaneous oxidation Graphene has biocidal property.Itself and acetyl cellulose blend are prepared forward osmosis membrane, and be expected to, while the high water flux of acquisition, also make forward osmosis membrane product have stain resistance and biocidal property, this is that the research and development of forward osmosis membrane material and application provide new thinking.
How while obtaining hydrophilic nmature, make again forward osmosis membrane have resistance tocrocking and keep the stability of water flux, this is the film scientific worker difficult problem thinking always and studying in recent years.The present invention adopts nano titanium oxide to improve the structure of forward osmosis membrane and hydrophilic research, there is not yet bibliographical information both at home and abroad.
Summary of the invention
The object of this invention is to provide a kind of high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane, while having compared with high-hydrophilic matter, make again forward osmosis membrane have resistance tocrocking and keep the stability of water flux.
The invention discloses a kind of high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane, adopt following methods to make:
Consisting of of flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane formula of casting: cellulose acetate 7.0% ~ 26.0%(w/w), pore-foaming agent is polyethylene glycol or polyvinylpyrrolidone 2.0% ~ 16.0%(w/w), nano titanium oxide 0.1% ~ 5.0%(w/w), Graphene 0.05% ~ 0.1%(w/w), remaining is the mixed solvent of dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE and acetone, and its volume ratio is dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE: acetone=1:0.1 ~ 5.0;
First nano titanium oxide is joined in dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE, utilize the ultrasonic nano titanium oxide that makes dispersed fully wherein, join after having disperseed in dissolving tank, successively acetone, pore-foaming agent are joined in dissolving tank subsequently, cellulose acetate is added after uniform stirring 5 ~ 60min, at 25 ~ 90 DEG C of temperature, stirring and dissolving 3 ~ 15 is little of full and uniform, is mixed with high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane casting solution;
Then, by the casting solution that obtains static 8 ~ 24 hours at the reaction temperatures, bubble remaining in casting solution is removed;
Finally, being poured into by a certain amount of casting solution is covered with on the glass plate of supporting layer, by Flat Membrane scraper striking film forming, immerse solidification forming in the constant temperature coagulating bath water tank of 10 ~ 80 DEG C, after film shaping automatically disengages glass plate, soak 24 ~ 48 hours in deionized water, change a water every 12 hours, deionized water is cleaned and is namely obtained high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane.
The forward osmosis membrane of the invention described above, preferred: described supporting layer is the one of non-woven fabrics, cotton yarn filter cloth, filter paper, nylon cloth and polyester screen etc., and its pore size is 50 ~ 300 orders.
The forward osmosis membrane of the invention described above, preferred: described cellulose acetate is one in cellulose diacetate and Triafol T or two kinds.
The forward osmosis membrane of the invention described above, preferred: the molecular weight of described pore-foaming agent polyethylene glycol is 400MW.
The forward osmosis membrane of the invention described above, preferred: described nano titanium oxide is anatase titanium dioxide, and particle diameter is 20-40nm; Described Graphene is graphene oxide, and its sheet footpath is 60nm ~ 10 μm.
The forward osmosis membrane of the invention described above, preferred: described forward osmosis membrane formula of casting: cellulose acetate 10.0% ~ 20.0%(w/w), pore-foaming agent 5.0% ~ 10.0%(w/w), nano titanium oxide 1.0% ~ 3.0%(w/w), Graphene 0.05% ~ 0.1%(w/w), dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE: acetone=1:0.2 ~ 1.0.
In the preparation of high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane, by controlling the cellulose acetate of casting solution, pore-foaming agent, the content of nano titanium oxide and index and casting solution stirring and dissolving temperature, coagulation bath temperature and the setting time such as the kind of mixed solvent and ratio, the Structure and Properties of prepared blended forward osmosis membrane can be controlled well.Along with the content of cellulose acetate increases, film strength increases, but pure water infiltration coefficient decreases, and it has a significant impact by researcher is in the industry confirmed the stuctures and properties of film.And the content of nano titanium oxide determines the structure change of prepared blended forward osmosis membrane and the power of stain resistance, and show with the size of the pure water infiltration coefficient of film and reverse flux salt, stain resistance and operation stability, need the principal element controlled when being also the blended forward osmosis membrane of preparation high-performance.
High performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane prepared by the present invention, while acquisition is compared with high-hydrophilic, high water flux, also makes forward osmosis membrane product have stain resistance.
Detailed description of the invention
Embodiment 1
By 1.5%(W/W) nano titanium oxide (anatase titanium dioxide, particle diameter is 30nm) and 0.1%(w/w) graphene oxide (its sheet footpath is 200nm) join 46.0%(W/W) dimethyl formamide (DMF) in, utilize the ultrasonic nano titanium oxide that makes dispersed fully under normal temperature wherein, join after having disperseed in dissolving tank, subsequently successively by 27.4%(W/W) acetone, polyethylene glycol (PEG400) 9.0%(W/W) joins in dissolving tank, add 16%(W/W after uniform stirring 30min) cellulose acetate, at 55 DEG C of temperature, stirring and dissolving 6h is to full and uniform, preparation high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane casting solution.Then, by the casting solution static 12h at the reaction temperatures obtained, bubble remaining in casting solution is removed.Finally, a certain amount of casting solution is poured on the glass plate being covered with 120 order polyester screen, by Flat Membrane scraper striking film forming, immerse solidification forming in the constant temperature coagulating bath water tank of 60 DEG C, after film shaping automatically disengages glass plate, soak 24 hours in deionized water, changed a water every 12 hours, deionized water is put into concentration after cleaning be process 48 hours in the glycerite of 50%, namely obtains high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane.Utilize 1MNaCl as driving liquid, deionized water is as material liquid, and in the testing time of 1h, the pure water flux of prepared film reaches 17.5L/m
2more than h, reverse flux salt is less than 3.0g/m
2h.
Embodiment 2
The ratio of nano titanium oxide, acetone is adjusted to 1.0%(W/W respectively), 27.9%(W/W), remaining is with embodiment 1.The performance of then obtained high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane is: utilize 1MNaCl as driving liquid, deionized water is as material liquid, and in the testing time of 1h, the pure water flux of prepared film is greater than 15.5L/m
2h, reverse flux salt is less than 3.5g/m
2h.
Embodiment 3
The ratio of polyethylene glycol PEG400 is adjusted to 6%(W/W), the ratio of dimethyl formamide, acetone is adjusted to 47.5%(W/W respectively), 28.9%(W/W), remaining is with embodiment 1.The performance of then obtained high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane is: utilize 1MNaCl as driving liquid, deionized water is as material liquid, and in the testing time of 1h, the pure water flux of prepared film is greater than 15.0L/m
2h, reverse flux salt is less than 3.0g/m
2h.
Embodiment 4
The ratio of cellulose acetate is adjusted to 13%(W/W), the ratio of dimethyl formamide, acetone is adjusted to 47.5%(W/W respectively), 28.9%(W/W), remaining is with embodiment 1.The performance of then obtained high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane is: utilize 1MNaCl as driving liquid, deionized water is as material liquid, and in the testing time of 1h, the pure water flux of prepared film is greater than 18.5L/m
2h, reverse flux salt is less than 5.0g/m
2h.
Embodiment 5
Coagulation bath temperature is adjusted to 30 DEG C, remaining is with embodiment 1.The performance of then obtained high performance flat formula cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane is: utilize 1MNaCl as driving liquid, deionized water is as material liquid, and in the testing time of 1h, the pure water flux of prepared film is greater than 19.0L/m
2h, reverse flux salt is less than 6.0g/m
2h.
Comparative example 1
By 16%(W/W) cellulose acetate, 8.0%(W/W) polyethylene glycol join 76%(W/W) dimethyl formamide and acetone mixed solvent (dimethyl formamide: acetone=1:0.6) join in a certain order in dissolving tank, at 30 DEG C of temperature, stirring and dissolving 6h is to full and uniform, prepares flat Cellulose acetate forward osmotic membrane casting solution.Then, by the casting solution static 12h at the reaction temperatures obtained, bubble remaining in casting solution is removed.Finally, a certain amount of casting solution is poured on the glass plate being covered with 120 order polyester screen, by Flat Membrane scraper striking film forming, immerse solidification forming in the constant temperature coagulating bath water tank of 60 DEG C, after film shaping automatically disengages glass plate, soak 24 hours in deionized water, changed a water every 12 hours, deionized water is put into concentration after cleaning be process 48 hours in the glycerite of 50%, namely obtains flat Cellulose acetate forward osmotic membrane.Utilize 1MNaCl as driving liquid, deionized water is as material liquid, and in the testing time of 1h, the pure water flux of prepared film reaches 16.5L/m
2more than h, reverse flux salt is less than 7.5g/m
2h.
Claims (6)
1. flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane, is characterized in that adopting following methods to make:
Consisting of of flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane formula of casting: cellulose acetate 7.0% ~ 26.0%(w/w), pore-foaming agent is polyethylene glycol or polyvinylpyrrolidone 2.0% ~ 16.0%(w/w), nano titanium oxide 0.1% ~ 5.0%(w/w), Graphene 0.05% ~ 0.1%(w/w), remaining is the mixed solvent of dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE and acetone, and its volume ratio is dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE: acetone=1:0.1 ~ 5.0;
First nano titanium oxide, Graphene are joined in dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE, utilize ultrasonic nano titanium oxide, the Graphene of making dispersed fully wherein, join after having disperseed in dissolving tank, successively acetone, pore-foaming agent are joined in dissolving tank subsequently, cellulose acetate is added after uniform stirring 5 ~ 60min, at 25 ~ 90 DEG C of temperature, stirring and dissolving 3 ~ 15 is little of full and uniform, is mixed with flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane casting solution;
Then, by the casting solution that obtains static 8 ~ 24 hours at the reaction temperatures, bubble remaining in casting solution is removed;
Finally, being poured into by a certain amount of casting solution is covered with on the glass plate of supporting layer, by Flat Membrane scraper striking film forming, immerse solidification forming in the constant temperature coagulating bath water tank of 10 ~ 80 DEG C, after film shaping automatically disengages glass plate, soak 24 ~ 48 hours in deionized water, change a water every 12 hours, deionized water is cleaned and is namely obtained flat cellulose acetate/nanometer titanium dioxide blending forward osmosis membrane.
2. forward osmosis membrane according to claim 1, is characterized in that: described supporting layer is the one of non-woven fabrics, cotton yarn filter cloth, filter paper, nylon cloth and polyester screen etc., and its pore size is 50 ~ 300 orders.
3. forward osmosis membrane according to claim 1, is characterized in that described cellulose acetate is one in cellulose diacetate and Triafol T or two kinds.
4. forward osmosis membrane according to claim 1, is characterized in that: the molecular weight of described pore-foaming agent polyethylene glycol is 400MW.
5. forward osmosis membrane according to claim 1, is characterized in that: described nano titanium oxide is anatase titanium dioxide, and particle diameter is 20-40nm; Described Graphene is graphene oxide, and its sheet footpath is 60nm ~ 10 μm.
6. forward osmosis membrane according to claim 1, it is characterized in that: described forward osmosis membrane formula of casting: cellulose acetate 10.0% ~ 20.0%(w/w), pore-foaming agent 5.0% ~ 10.0%(w/w), nano titanium oxide 1.0% ~ 3.0%(w/w), Graphene 0.05% ~ 0.1%(w/w), dimethyl formamide or dimethylacetylamide or 1-METHYLPYRROLIDONE: acetone=1:0.2 ~ 1.0.
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| CN105749762B (en) * | 2016-01-26 | 2018-06-12 | 浙江工商大学 | A kind of polymer compound film material with photocatalytic activity and preparation method thereof |
| CN105642132B (en) * | 2016-04-15 | 2017-12-12 | 北京碧水源膜科技有限公司 | A kind of polyvinylidene fluoride film being modified through targetting synergy nano-functional material and preparation method thereof |
| CN105727759A (en) * | 2016-04-20 | 2016-07-06 | 中国科学院城市环境研究所 | High-performance forward permeable membrane and electrostatic spinning preparation method thereof |
| CN105921034A (en) * | 2016-06-21 | 2016-09-07 | 北京林业大学 | Preparation and application of graphene oxide-modified cellulose acetate forward osmosis membrane |
| CN106902637A (en) * | 2017-02-22 | 2017-06-30 | 济南大学 | High performance flat formula forward osmosis membrane and preparation method based on hydroxyl carbon nano tube |
| CN106925138A (en) * | 2017-02-22 | 2017-07-07 | 济南大学 | High performance flat formula forward osmosis membrane and preparation method based on carboxylic carbon nano-tube |
| CN106902646A (en) * | 2017-02-22 | 2017-06-30 | 济南大学 | High performance flat formula forward osmosis membrane and preparation method based on aminated carbon nano tube |
| TWI664150B (en) * | 2018-05-30 | 2019-07-01 | National Taiwan University Of Science And Technology | Oil separation membrane and producing method thereof |
| CN109012181B (en) * | 2018-09-13 | 2019-05-07 | 青岛科技大学 | A kind of synthetic method and gained permeable membrane of the modified Cellulose acetate forward osmotic membrane of ZIF-8 |
| CN111825873A (en) * | 2020-07-14 | 2020-10-27 | 江苏天佑新材料科技有限公司 | Photocatalytic and physical adsorption antibacterial regenerated bamboo cellulose membrane and preparation method thereof |
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