CN102921300A - Agent and method for surface treatment on nanofiltration membrane - Google Patents

Agent and method for surface treatment on nanofiltration membrane Download PDF

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CN102921300A
CN102921300A CN2012104151641A CN201210415164A CN102921300A CN 102921300 A CN102921300 A CN 102921300A CN 2012104151641 A CN2012104151641 A CN 2012104151641A CN 201210415164 A CN201210415164 A CN 201210415164A CN 102921300 A CN102921300 A CN 102921300A
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membrane
agent
conditioning agent
surface conditioning
surface treatment
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CN102921300B (en
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梁松苗
吴宗策
金焱
许国扬
陶健
蔡志奇
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Wharton Technology Co ltd
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Vontron Technology Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

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Abstract

The invention provides an agent and a method for surface treatment on a nanofiltration membrane. The agent for surface treatment comprises 0.01 to 10wt% of antibacterial nano-particles, 0.1 to 30wt% of one or more active agents and the balance one or more solvents. A preparation method of the agent comprises the following steps of dispersing the antibacterial nano-particles in the one or more solvents, stirring at a temperature of 20 to 40 DEG C until uniform dispersion, adding the one or more active agents into the mixed solution, and stirring for 1 to 10 hours until dissolution to obtain the agent for surface treatment on a nanofiltration membrane. The method for surface treatment on a nanofiltration membrane comprises the following steps of 1, coating or dipping of the agent for surface treatment on a nanofiltration membrane, 2, air-knife surface drying, and 3, drying in an oven. The agent and the method for surface treatment on a nanofiltration membrane have the advantages that a high desalinization rate is maintained and a nanofiltration membrane treated by the agent and the method has high flux under low pressure so that a nanofiltration membrane product having excellent flux performances and good desalination effects is obtained. The agent has high efficiency, can be operated easily, and has low equipment requirements and strong practicality.

Description

A kind of surface conditioning agent of NF membrane and surface treatment method
Technical field
The present invention relates to a kind of surface conditioning agent and surface treatment method of NF membrane, belong to water treatment field.
Background technology
NF membrane very easily is subject to organic contamination, and the characteristics such as its surface charge, hydrophobicity, roughness have significant impact to organic adsorption fouling and the obstruction of film.On the one hand, polar organic matter may carry out with hydrogen bond action, dispersion force absorption and hydrophobic effect in the lip-deep absorption of NF membrane; The formation of these adsorption layer of surface active agent makes hydrone will see through film and just must consume higher energy; Exactly because the activation energy of this increase finally causes the decline of aquifer yield.On the other hand, the interaction between hydrophobicity organic matter and water is enriched on the film surface the slow organic matter of these diffusions, and namely the low diffusible organic matter of macromolecule can be concentrated on the film surface; And also being conducive to them, the concentration polarization of macromolecule organic is adsorbed on the film surface; And the water intermediate ion (mainly is Ca 2-) interact with organic matter functional group, also can change hydrophobicity and the diffusivity of these organic molecules, thereby so that nonpolar organic matter, hydrophobicity Adsorption of Organic cause on the NF membrane surface film to pollute.
The NF membrane separation has two characteristics, i.e. sieve effect and charge effect.Sieve effect refers to that molecular weight holds back tunicle greater than the material of the molecular cut off of film, otherwise then sees through; Charge effect is called again the Donnan effect, refers to ion and the charged electrostatic interaction of film.Mainly be to be sieve effect by steric effect to the filtration of uncharged molecule, utilize the sieve effect can be with the separating substances of different molecular weight; And mainly be by electric charging effect to the filtration with the material of electric charge, NF membrane surface separating layer can be made of polyelectrolyte, the film surface is with certain electric charge, the surface of most of NF membrane is with negative electrical charge, they pass through electrostatic interaction, hinder the infiltration of multivalent ion, this is that NF membrane still has the major reason than the high desalination performance under lower pressure.NF membrane commonly used mostly is charged membrane at present, compares with non-charged nanofiltration membrane, and some specific ions are had preferably removal effect, but the impurity in the easy adsorbed water of charged membrane causes film to pollute, thereby causes film properties to descend.Change an angle, if utilize this characteristic, make film adsorption functional mass, then can by change the film surface nature, such as improving hydrophily, roughness, fill fenestra and improve rejection etc., thereby improve the NF membrane overall performance.
CN1293138C discloses a kind of synthetic polymeric membrane with the surface preparation of surface conditioning agent and synthetic polymeric membrane, be that special ethylene base co-polymer by being contained the nitrogen organic group by side chain and the surface conditioning agent of lubricant carry out certain processing to the synthetic polymeric membrane surface, given the electrostatic prevention of synthetic polymeric membrane excellence, antifog property and excellent sliding.But this scheme is not suitable for high but the problem that membrane flux is lower of NF membrane removal efficiency that solves.
Summary of the invention
The invention provides a kind of surface conditioning agent and surface treatment method of NF membrane, solved the NF membrane removal efficiency high, make the film surface be vulnerable to pollute and make the lower problem of membrane flux.
Technical scheme of the present invention is as described below.
A kind of surface conditioning agent of NF membrane is characterized in that: by antimicrobial nano particle, activating agent and solvent composition; Wherein, the content of antimicrobial nano particle is that the content of 0.01~10wt%, activating agent is 0.1~30wt%, and all the other are solvent;
Described antimicrobial nano particle refers to any or several combination in titanium dioxide, aluminium oxide, silica, zinc oxide, zirconia, imvite and the CNT;
The particle diameter of described antimicrobial nano particle is 1~500nm, is optimized for 10~200nm;
Described solvent refer in water, ethanol, methyl alcohol, isopropyl alcohol, the tert-butyl alcohol and the acetone any or several;
Described activating agent refers to monoethanolamine, diethanol amine, triethanolamine, dimethylethanolamine, phosphoric acid acyl monoethanolamine, N methyldiethanol amine, N, the N-diethyl ethylene diamine, phenolethanolamine, triethanolamine oleate, PVOH amine, the boron trifluoride zirconium triethanolamine complex, the N-aminoethanolamine, Octopirox, N-benzyl ethyl alcohol amine, the monoethanolamine thioglycolate salt, N butyl diethanol amine, tert-butyl group monoethanolamine, coconut oleoyl diethanol amine, triethanolamine hydrochloride, triethanolamine phosphate, myristoyl phosphoric acid acyl monoethanolamine, glycerine, in glycerin ether and the dodecyltriethanolamine sulfate etc. any or several;
The surface conditioning agent of above-mentioned NF membrane, its preparation method are that nano particle is scattered in the solvent, are stirred to be uniformly dispersed under 20~40 ℃, add activating agent, stir 1~10h, obtain surface conditioning agent after the dissolving.
A kind of surface treatment method of NF membrane mainly may further comprise the steps:
(1) surface conditioning agent applies or dipping: above-mentioned surface conditioning agent evenly is coated on the NF membrane surface, perhaps with the NF membrane surface impregnation in surface conditioning agent;
(2) surface drying is processed: adopt the air knife surface drying to process to NF membrane;
(3) drying and processing: place baking oven, at 15-80 ℃ of lower drying and processing 0.1~1h, get final product.
Coating in the described step (1) refers to adopt the mode of blade coating, spraying, and surface conditioning agent evenly is coated on the NF membrane face, and the inorganic agent that is sprayed on the face is 10~200g/m 2, solution keeps 0.1~10min at face after the spraying.
Dipping in the described step (1) refers to the NF membrane diaphragm is immersed in 0.1~10min in 10~60 ℃ the surface conditioning agent.
Beneficial effect of the present invention: nano particle in the reagent treatment, such as the introducing of TiO 2 particles, can improve the antibacterial ability of NF membrane in running, and improve to a certain extent the desalting performance of NF membrane; The introducing of activating agent can be by the effect of residual groups on itself and the NF membrane desalination layer and polyamide network the flux of Effective Raise diaphragm; Because the NF membrane salt rejection rate after activating agent is processed has decline to a certain degree, the introducing of nano particle can the equilibrium activity agent for the inhibition of desalting performance; Selected solvent in the surface conditioning agent has promoted the raising of flux.Adopt surface conditioning agent of the present invention and surface treatment method, in the situation that keep than equipment with high desalinization, can make NF membrane under the low pressure condition, possess higher flux, the acquisition desalination is better, and the NF membrane product of flux performance excellence, have efficient, easy-operating characteristics, lower for the requirement of equipment, practicality is very strong.
The specific embodiment
In order to deepen that the present invention is understood, the present invention is described in further detail below in conjunction with embodiment, and this embodiment only is used for explaining the present invention, does not consist of the restriction to protection domain of the present invention.
Embodiment 1
50g titanium dioxide nano-particle (particle diameter 60nm) is scattered in the 4900g deionized water, under 20 ° of C fully dispersed with stirring evenly after, add the 50g monoethanolamine, stir 1h, be mixed with surface conditioning agent.Get 20cm * 20cm specification VNF1 NF membrane and impregnated in the suspension, take out behind the 0.1min, in 80 ° of C baking ovens, heat-treat after removing remained on surface solution with air knife, namely get the NF membrane behind the Nanoparticle Modified behind the processing time 10min.
Embodiment 2
100g aluminium oxide nano particle (particle diameter 500nm) is dissolved in the 4900g ethanol, under 25 ° of C fully dispersed with stirring evenly after, add 50g phosphoric acid acyl monoethanolamine, stir 3h, be mixed with surface conditioning agent.Get 20cm * 20cm specification VNF1 NF membrane and impregnated in the ethylene glycol amine aqueous solution, take out behind the 4min, in 60 ° of C baking ovens, heat-treat after removing remained on surface solution with air knife, namely get the NF membrane of ethylene glycol after amine-modified behind the processing time 30min.
Embodiment 3
50g Nano particles of silicon dioxide (particle diameter 200nm) is scattered in the 4850g methyl alcohol, under 30 ° of C fully dispersed with stirring evenly after, add the 100g dimethylethanolamine and join in the suspension, stir 57h, be mixed with surface conditioning agent.Get 20cm * 20cm specification VNF1 NF membrane and impregnated in the suspension, take out behind the 8min, with in 40 ° of C baking ovens, heat-treating behind the air knife removal remained on surface solution, namely get the NF membrane after surface conditioning agent is modified behind the processing time 40min.
Embodiment 4
50g zinc oxide nano-particle (particle diameter 100nm) is scattered in the 4850g isopropyl alcohol, under 35 ° of C fully dispersed with stirring evenly after, add the 100g triethanolamine in suspension, stir 7h, be mixed with surface conditioning agent.Get 20cm * 20cm specification VNF1 NF membrane and impregnated in the suspension, take out behind the 10min, with in 15 ° of C baking ovens, heat-treating behind the air knife removal remained on surface solution, namely get the NF membrane after surface conditioning agent is modified behind the processing time 60min.
Embodiment 5
50g zirconium oxide nano-particle (particle diameter 10nm) is scattered in the 4950g tert-butyl alcohol, under 40 ° of C fully dispersed with stirring evenly after, add the 50g diethanol amine, stir 10h, be mixed with surface conditioning agent.Get 20cm * 20cm specification VNF1 NF membrane and impregnated in the suspension, take out behind the 6min, in 70 ° of C baking ovens, heat-treat after removing remained on surface solution with air knife, namely get the NF membrane behind the Nanoparticle Modified behind the processing time 20min.
Get 6 of Vontron commercialization VNF1 NF membrane, wherein 5 each NF membrane that obtains after the described method of embodiment 1--5 is processed are test product, remaining 1 is reference substance without any surface treatment, in the test of diaphragm monitor station, be 70psi at operating pressure, temperature is 25 ℃, the pH value is under the test condition of 6.5-7.5, obtain 2000ppm NaCl aqueous solution water flux (GFD), and 2000ppm MgSO4 aqueous solution water flux (GFD), the results are shown in Table 1.
The flux of table 1 NF membrane and salt rejection rate
Figure BDA00002308092500041
Figure BDA00002308092500051
As shown in Table 1, compare with the NF membrane without any processing, adopt surface conditioning agent of the present invention and surface treatment method, can effectively regulate flux and the salt rejection rate of NF membrane.After adopting the embodiment of the invention 1 described method to process NF membrane, the flux of NF membrane descends to some extent, but its salt rejection rate obviously rises; After adopting the embodiment of the invention 2 described methods to process NF membrane, the flux of NF membrane obviously rises, but its salt rejection rate also descends to some extent; After adopting the embodiment of the invention 3 and 4 described methods to process NF membrane, flux and the salt rejection rate of NF membrane all are improved; After adopting the embodiment of the invention 5 described methods to process NF membrane, the flux of NF membrane slightly descends, but salt rejection rate obviously improves.

Claims (9)

1. the surface conditioning agent of a NF membrane is characterized in that: by antimicrobial nano particle, activating agent and solvent composition; Wherein, the content of antimicrobial nano particle is that the content of 0.01~10wt%, activating agent is 0.1~30wt%, and all the other are solvent;
2. the surface conditioning agent of a kind of NF membrane according to claim 1 is characterized in that: described antimicrobial nano particle refers to any or several combination in titanium dioxide, aluminium oxide, silica, zinc oxide, zirconia, imvite and the CNT;
3. the surface conditioning agent of a kind of NF membrane according to claim 2, it is characterized in that: the particle diameter of described antimicrobial nano particle is 1~500nm, is optimized for 10~200nm;
4. the surface conditioning agent of a kind of NF membrane according to claim 1 is characterized in that: described solvent refer in water, ethanol, methyl alcohol, isopropyl alcohol, the tert-butyl alcohol and the acetone any or several;
5. the surface conditioning agent of a kind of NF membrane according to claim 1, it is characterized in that: described activating agent refers to monoethanolamine, diethanol amine, triethanolamine, dimethylethanolamine, phosphoric acid acyl monoethanolamine, N methyldiethanol amine, N, the N-diethyl ethylene diamine, phenolethanolamine, triethanolamine oleate, PVOH amine, the boron trifluoride zirconium triethanolamine complex, the N-aminoethanolamine, Octopirox, N-benzyl ethyl alcohol amine, the monoethanolamine thioglycolate salt, N butyl diethanol amine, tert-butyl group monoethanolamine, coconut oleoyl diethanol amine, triethanolamine hydrochloride, triethanolamine phosphate, myristoyl phosphoric acid acyl monoethanolamine, glycerine, in glycerin ether and the dodecyltriethanolamine sulfate etc. any or several;
6. the surface conditioning agent of a kind of NF membrane according to claim 1, it is characterized in that: its preparation method is that nano particle is scattered in the solvent, is stirred to be uniformly dispersed under 20~40 ℃, adds activating agent, stir 1~10h, obtain surface conditioning agent after the dissolving.
7. the surface treatment method of a NF membrane is characterized in that: mainly may further comprise the steps:
(1) surface conditioning agent applies or dipping: each described surface conditioning agent of claim 1 ~ 6 evenly is coated on the NF membrane surface, perhaps with the NF membrane surface impregnation in surface conditioning agent;
(2) surface drying is processed: adopt the air knife surface drying to process to NF membrane;
(3) drying and processing: place baking oven, at 15-80 ℃ of lower drying and processing 0.1~1h, get final product.
8. the surface treatment method of a kind of NF membrane according to claim 7, it is characterized in that: the coating in the described step (1) refers to adopt the mode of blade coating, spraying, surface conditioning agent evenly is coated on the NF membrane face, and the inorganic agent that is sprayed on the face is 10~200g/m 2, solution keeps 0.1~10min at face after the spraying.
9. the surface treatment method of a kind of NF membrane according to claim 7 is characterized in that: the dipping in the described step (1) refers to the NF membrane diaphragm is immersed in 0.1~10min in 10~60 ℃ the surface conditioning agent.
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103288179A (en) * 2013-06-27 2013-09-11 江苏省环境科学研究院 Method for improving reverse osmosis defluorination efficiency
CN106925121A (en) * 2017-05-02 2017-07-07 华东理工大学 A kind of Mg2+And Li+Separate triple channel endodermis positively charged nanofiltration membranes and preparation method thereof
CN107082444A (en) * 2017-04-05 2017-08-22 南方科技大学 Antibacterial agent, antibacterial filter membrane, and preparation method and application thereof
CN108201790A (en) * 2018-01-05 2018-06-26 中国科学院宁波材料技术与工程研究所 A kind of electrostatic spraying prepares the method and its product of NF membrane
CN109216548A (en) * 2018-10-22 2019-01-15 东莞理工学院 A kind of perovskite solar battery scrapes coating preparation method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3644119B2 (en) * 1996-03-12 2005-04-27 Jfeエンジニアリング株式会社 Membrane filtration device and membrane filtration method
CN101053782A (en) * 2007-05-16 2007-10-17 河北科技大学 Antibiotic cellulose acetate nanofiltration membrane and its preparation method
CN101700473A (en) * 2009-10-30 2010-05-05 北京工业大学 Self-assembly method of inorganic nano particle hybridization organic membrane
CN101940883A (en) * 2010-08-03 2011-01-12 浙江大学 Preparation method of reverse osmosis composite membrane containing nano zeolite molecular sieves

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3644119B2 (en) * 1996-03-12 2005-04-27 Jfeエンジニアリング株式会社 Membrane filtration device and membrane filtration method
CN101053782A (en) * 2007-05-16 2007-10-17 河北科技大学 Antibiotic cellulose acetate nanofiltration membrane and its preparation method
CN101700473A (en) * 2009-10-30 2010-05-05 北京工业大学 Self-assembly method of inorganic nano particle hybridization organic membrane
CN101940883A (en) * 2010-08-03 2011-01-12 浙江大学 Preparation method of reverse osmosis composite membrane containing nano zeolite molecular sieves

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103288179A (en) * 2013-06-27 2013-09-11 江苏省环境科学研究院 Method for improving reverse osmosis defluorination efficiency
CN107082444A (en) * 2017-04-05 2017-08-22 南方科技大学 Antibacterial agent, antibacterial filter membrane, and preparation method and application thereof
CN107082444B (en) * 2017-04-05 2019-09-17 南方科技大学 Antibacterial agent, antibacterial filter membrane, and preparation method and application thereof
CN106925121A (en) * 2017-05-02 2017-07-07 华东理工大学 A kind of Mg2+And Li+Separate triple channel endodermis positively charged nanofiltration membranes and preparation method thereof
CN106925121B (en) * 2017-05-02 2020-04-24 华东理工大学 Mg2+And Li+Separating three-channel inner skin layer positively-charged nanofiltration membrane and preparation method thereof
CN108201790A (en) * 2018-01-05 2018-06-26 中国科学院宁波材料技术与工程研究所 A kind of electrostatic spraying prepares the method and its product of NF membrane
CN108201790B (en) * 2018-01-05 2019-12-03 中国科学院宁波材料技术与工程研究所 A kind of method and its product of electrostatic spraying preparation nanofiltration membrane
CN109216548A (en) * 2018-10-22 2019-01-15 东莞理工学院 A kind of perovskite solar battery scrapes coating preparation method

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