CN106632922B - The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment - Google Patents

The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment Download PDF

Info

Publication number
CN106632922B
CN106632922B CN201610918203.8A CN201610918203A CN106632922B CN 106632922 B CN106632922 B CN 106632922B CN 201610918203 A CN201610918203 A CN 201610918203A CN 106632922 B CN106632922 B CN 106632922B
Authority
CN
China
Prior art keywords
block polymer
structural unit
hydrophilic segment
containing hydrophilic
formula
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.)
Active
Application number
CN201610918203.8A
Other languages
Chinese (zh)
Other versions
CN106632922A (en
Inventor
白仁碧
张干伟
周晓吉
沈舒苏
杨晶晶
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou University of Science and Technology
Original Assignee
Suzhou University of Science and Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Suzhou University of Science and Technology filed Critical Suzhou University of Science and Technology
Priority to CN201610918203.8A priority Critical patent/CN106632922B/en
Publication of CN106632922A publication Critical patent/CN106632922A/en
Application granted granted Critical
Publication of CN106632922B publication Critical patent/CN106632922B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F293/00Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule
    • C08F293/005Macromolecular compounds obtained by polymerisation on to a macromolecule having groups capable of inducing the formation of new polymer chains bound exclusively at one or both ends of the starting macromolecule using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/147Microfiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D67/00Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081After-treatment of organic or inorganic membranes
    • B01D67/0093Chemical modification
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D69/00Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/02Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D71/00Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06Organic material
    • B01D71/30Polyalkenyl halides
    • B01D71/32Polyalkenyl halides containing fluorine atoms
    • B01D71/34Polyvinylidene fluoride
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00Chemical modification by after-treatment
    • C08F8/10Acylation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/36Hydrophilic membranes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2438/00Living radical polymerisation
    • C08F2438/01Atom Transfer Radical Polymerization [ATRP] or reverse ATRP

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The method for the block polymer modified polyvinilidene fluoride microfiltration membranes containing hydrophilic segment that the present invention provides a kind of comprising following steps: Step 1: polyvinylidene fluoride microporous filtering film is impregnated 1~100 minute in modifier solution;Step 2: the polyvinylidene fluoride microporous filtering film after immersion is irradiated 1~48 hour under ultraviolet light, washs to remove uncrosslinked block polymer, obtain the polyvinylidene fluoride microporous filtering film of hydrophilic modifying.The modifying process of hydrophilic modifying PVDF microfiltration membranes of the invention is easy to operate, and there is the Modified Membrane obtained good stability and good hydrophily and antifouling property therefore can be widely applied to the every field such as food industry, water process and environmental protection.

Description

The preparation method and its modified polyvinilidene fluoride of block polymer containing hydrophilic segment The method of microfiltration membranes
Technical field
The invention belongs to polymeric film material fields, in particular to a kind of micro- by block polymer modified polyvinilidene fluoride The method of filter membrane.
Background technique
Micro-filtration is also known as micro porous filtration, in the case where certain pressure pushes, is retained in solution using miillpore filter as filter medium Some solid particles, drop or other biologic grains etc., and a large amount of solvents, small molecule and a small amount of macromolecular solute can penetrate The separation process of film.In the subtractive process of water, micro-filter technology can remove bacterium and solid impurity, can be used for medicine, beverage With the production of water.In the preparation of electronics industry ultrapure water, micro-filtration can be used for ultrafiltration and the pretreatment of reverse osmosis process and product Terminal security personnel's filtering.Micro-filter technology also can be used for the filtering of the various drinks such as beer, yellow rice wine, to remove yeast therein, mould With other microorganisms, product is clarified, and extends storage period.It includes oiliness sewage treatment that micro-filter technology, which can be used for sewage treatment, Etc..Micro-filter technology is also widely used in fields such as drug degerming, biological detections.
The main component for realizing micro-filtration operation is membrane material.Wherein Kynoar (PVDF) is a kind of for UF membrane skill The excellent polymeric film material of art, it has good chemical stability, heat resistance and mechanical stability.But the surface of PVDF Can be very low, hydrophobicity is very strong, therefore is highly susceptible to pollute, and so as to cause membrane flux rapid decay, film reduced service life is simultaneously And operating cost is increased, it is limited in the application in UF membrane field.And dirt can be reduced by improving membrane material surface hydrophilicity Object is contaminated in the absorption of film surface, is a kind of important method for solving pvdf membrane pollution, is also become the research of researcher's recent years Hot spot.Currently, the method to pvdf membrane hydrophilic modifying mainly has chemical method and physical method two major classes.Wherein, chemical method Including direct surface processing and surface grafting etc..Physical method has physical blending and surface coating etc..
Direct surface processing is to be handled using strong acid, highly basic, strong oxidizer or plasma etc. film surface, in film Surface generates the hydrophilic polars functional groups such as hydroxyl, carboxyl, amino and peroxy-radical, improves film to a certain extent to the affine of water Property.Such as Chinese patent CN 102179189 A of 103831027 A and CN, using plasma technology is to polyvinylidene fluoride film It is chemically modified and is modified, by increasing film surface hydrophilic radical number and optimizing the distribution of hydrophilic radical, to improve and change The hydrophily of kind film surface, and then achieve the purpose that improve film antifouling property.But this method is hydrophilic in enhancing film Meanwhile membrane body performance and membrane structure may be made to be destroyed to a certain extent, and the parent that this processing method illustrates Water base group is smaller, is easy to migrate with polymer segment movement to membrane body, becomes modified effect slowly in use Difference.
The method of surface grafting is to introduce hydrophilic radical in film surface by way of Covalent bonding together.Generally first with table The methods of face chemical treatment, corona treatment, gamma-ray irradiation or UV irradiation first introduce active reaction point in film surface, then Hydrophilic radical is introduced by the method for grafting to improve the hydrophilicity of film.101293184 A of Chinese patent CN passes through gamma-rays Radiation grafted method introduces acrylate copolymer in PVDF doughnut membrane aperture and film surface, makes the hydrophily and anti-pollution of film Dye ability is significantly improved.Pvdf membrane is placed in plasma by 103831024 A of Chinese patent CN to be pre-processed, Then the reaction of surface grafting acrylic acid is carried out, and it is molten that the modified pvdf membrane in polyacrylic acid surface is placed in polyanion electrolyte It is adsorbed in liquid, polycation electrolyte solution or zwitterionic betaines quasi polymer solution, obtains that there is charged surface And its outermost surface is the polyvinylidene fluoride porous film of electronegativity, electropositivity or electroneutral.Have obtained by final charged more The polyvinylidene fluoride separation membrane on sample surface shows preferable antifouling property.103962011 A of Chinese patent CN will be dredged Water PVDF seperation film is placed in progress plasma discharge processing in plasma processing apparatus, and film surface is made to generate hydroxyl isoreactivity Group site recycles the orientation reaction of PEG and TMC high activity functional group, realizes the effective chemical graft of film surface.Final gained The antifouling property of modified PVDF membrane significantly improves.Although hydrophilic radical can be passed through chemical method key by the method for surface grafting It closes in film surface, but condition needed for grafting process is relative complex, generally requires multi step strategy.And grafting site may it is uneven or Person's negligible amounts, to influence the performance of final Modified Membrane.
Physical blending can be completed in film-forming process, be a kind of method being easily achieved.Through frequently with inorganic nano-particle Son, polyvinyl alcohol or amphipathic nature block polymer etc. and film base material blending and modifying, to improve the hydrophilicity of film and resist Pollutant performance.102350232 A of Chinese patent CN is blended that preparation good hydrophilic property, resistance tocrocking are strong to be total to by polysulfones and with PVDF Mixed micro-filtration flat sheet membrane, product good hydrophilic property, contamination resistance are strong.103127839 A of Chinese patent CN, by different nanoparticles Son mixing is added in casting solution, prepares PVDF blend film using phase inversion.Pvdf membrane is significantly improved using the method Contamination resistance.Film forming is blended in amphipathic copolymer and PVDF by 103007787 A of Chinese patent CN, preparation it is amphipathic total Polymerized pvdf membrane product has the characteristics that permanent hydrophilic, antifouling property are excellent.104174304 A of Chinese patent CN Film forming is blended with PVDF for chitosan and alkylated chitosan respectively with 104190267 A of CN, effectively increases PVDF seperation film Hydrophily and antifouling property.104437121 A of Chinese patent CN is blended using block copolymer PEO-b-PMMA and PVDF Film forming is blended film surface in PVDF and increases block copolymer PEO-b-PMMA, effectively raises the hydrophily of PVDF blend film, The antifouling property for enhancing film solves tradition and the technical problem that the decline of membrane flux is fast, service life is short is blended.Although above-mentioned special Modifying agent used in benefit and PVDF are blended the hydrophily and contamination resistance that can effectively improve polymer film, however additive and poly- It is to have to the problem of facing that it is less, which to close the distribution of the compatibility and modifying agent of object matrix on surface,.
Surface coating be a kind of raising film surface hydrophily technology that comparison is easy, mainly by by modifying agent dispersion or it is molten Solution is applied to film surface afterwards in a solvent to obtain the polymer film that surface has modifying agent coating.Modifying agent used can be height Molecularly Imprinted Polymer is also possible to inorganic nano-particle.Chinese patent CN 102166485A uses TiO2Nano particle passes through physics It is carried out dynamic membrane modifying coated on PVDF hollow fiber form micro-filtration film surface by effect, is declined so as to improve PVDF doughnut The hydrophily and contamination resistance of filter membrane, the results showed that the Dynamic Membrane has lower fouling membrane rate of rise.But this method It is faced with TiO2Nano particle is combined with the surface insecure, the problems such as being easy to fall off and modified effect is caused to fade away.
In conclusion the existing method for pvdf membrane hydrophilic modifying is unstable there are effect or duration is bad etc. asks Topic.
Summary of the invention
In view of the foregoing deficiencies of prior art, the purpose of the present invention is to provide a kind of improvement PVDF microfiltration membranes are hydrophilic Property method, by directly coating the modifying agent of Photocrosslinkable in PVDF micro-filtration film surface to form coating, then using ultraviolet Light irradiation, crosslinks coating, and then fix its structure, to realize the hydrophilic modifying to PVDF microfiltration membranes.
It is a still further object of the present invention to provide a kind of for being modified the modifying agent of PVDF microfiltration membranes, the modifying agent be containing The block polymer of hydrophilic segment, can be carried out photo-crosslinking.
It is a still further object of the present invention to provide a kind of preparation methods of block polymer containing hydrophilic segment.
In order to achieve the above objects and other related objects, the present invention provides a kind of block polymer containing hydrophilic segment and changes The method of property polyvinylidene fluoride microporous filtering film comprising following steps:
Step 1: polyvinylidene fluoride microporous filtering film is impregnated 1~100 minute in modifier solution;
Step 2: the polyvinylidene fluoride microporous filtering film after immersion is irradiated 1~48 hour under ultraviolet light, wash to remove not The block polymer of crosslinking obtains the polyvinylidene fluoride microporous filtering film of hydrophilic modifying;
Wherein, the modifying agent is by Formulas I structural unit and Formula II structural unit or Formulas I structural unit and formula III structure The block polymer containing hydrophilic segment of unit composition:
Wherein, R1 is hydrogen atom or methyl, and R2 is the acylated acrylatoalkoxysilanes ester of cortex cinnamomi, and R3 is hydrogen atom or methyl, R4 is the Arrcostab containing methoxyl group and ethyoxyl;N is integer in formula III structure.
Preferably, in step 1, the modifier solution solvent for use is tetrahydrofuran, dioxane, acetone, benzene first One of ether, methylene chloride or chloroform, the mass concentration of the modifier solution are 1~25%;Tetrahydro is used in step 2 One of furans, dioxane, acetone, methyl phenyl ethers anisole, methylene chloride or chloroform wash polyvinylidene fluoride microporous filtering film to remove not The block polymer of crosslinking.
Preferably, in step 2, the ultraviolet light is the ultraviolet light that commercial ultraviolet lamp issues, and the ultraviolet lamp power is 30 Watt~1000 watts.
Preferably, the polyvinylidene fluoride microporous filtering film aperture is 0.1~10 μm, with a thickness of 10~200 μm, porosity 10 ~80%.
A kind of block polymer containing hydrophilic segment, structural formula are as follows:
The block polymer containing hydrophilic segment is by Formulas I structural unit and Formula II structural unit or Formulas I structure list The block polymer of member and formula III structural unit composition;
Wherein, R1 is hydrogen atom or methyl, and R2 is the acylated acrylatoalkoxysilanes ester of cortex cinnamomi, and R3 is hydrogen atom or methyl, R4 is the Arrcostab containing methoxyl group and ethyoxyl;The integer that n is 0~500 in formula III structure.
Preferably, in the Formulas I structural unit, R2 is the hydroxyethyl methacrylate that cortex cinnamomi is acylated or cortex cinnamomi is acylated third One of olefin(e) acid hydroxyl ethyl ester.
Preferably, in the Formula II structural unit, R4 is 2- ihethoxyethyl methacrylate or 2- (2- methoxyl group second One of oxygroup) ethylmethyl acrylate.
Preferably, the formula III structural unit be MPEG200, MPEG400, MPEG500, MPEG700, MPEG1000, One of MPEG1500, MPEG2000, MPEG5000, MPEG10000 or MPEG20000.
Preferably, Formulas I and the number of Formula II structural unit are 1~500.
A kind of preparation method preparing the above-mentioned block polymer containing hydrophilic segment, it is poly- by atom transferred free radical Conjunction method is prepared.
Specifically includes the following steps:
Step 1) prepares the brominated macromole evocating agent generated by Formula II structural unit or the polymerization of formula III structural unit;
Macromolecular initiation made from hydroxyethyl methacrylate, step 1) is added in step 2) in the round-bottomed flask of 100ml Reaction system stirring and dissolving is led to argon gas Gu and steeped 30 minutes by agent and 2,2'- bipyridyl and solvent, then deoxygenation, then by reactant System is transferred in the round-bottomed flask of the 100ml equipped with cuprous bromide, and in 50 DEG C of progress polymerization reaction 8h, reaction product is deposited in second It in ether, is deposited in ether and is repeated twice again after methanol dissolution, be then dried in vacuo under the conditions of 40 DEG C for 24 hours to constant weight, Obtain poly- Formula II structural unit-b- poly hydroxy ethyl acrylate block polymer or the poly- methyl-prop of poly- formula III structural unit-b- Olefin(e) acid hydroxyl ethyl ester block polymer;
Block polymer, 50mL pyridine made from step 2) is added in step 3) in the round-bottomed flask of 100ml, stirs molten Depolymerize object, and cinnamoyl chloride is added under condition of ice bath, is stirred to react at room temperature for 24 hours, and reaction product precipitates in methyl alcohol, It precipitates in methyl alcohol and is repeated twice again after chloroform dissolution, be then dried in vacuo under the conditions of 40 DEG C for 24 hours to constant weight, obtain meat The acylated poly- Formula II structural unit-b- poly hydroxy ethyl acrylate block polymer in osmanthus or the poly- first of poly- formula III structural unit-b- Base hydroxy-ethyl acrylate block polymer.
The present invention, which uses to have, can be carried out photo-crosslinking and the block polymer containing hydrophilic segment for modifying agent, by it It is directly coated on PVDF micro-filtration film surface and forms coating, then fix its knot using ultraviolet light crosslinked block polymer coating Structure, to realize the hydrophilic modifying to PVDF microfiltration membranes.
As described above, the side of the block polymer modified polyvinilidene fluoride microfiltration membranes disclosed by the invention containing hydrophilic segment Method has the advantages that
(1) block polymer containing hydrophilic segment used in the present invention can make coating stable after ultraviolet light cross-linking Ground is attached to PVDF micro-filtration film surface, to increase the stability of coating, has gained hydrophilic modifying PVDF microfiltration membranes fine Durability;
(2) block polymer of the invention containing hydrophilic segment can assign PVDF microfiltration membranes good hydrophilicity, Since hydrophilic polymeric segment has the ability of anti-organic contamination, it is thus possible to improve the antifouling property of PVDF microfiltration membranes;
(3) modifying process of hydrophilic modifying PVDF microfiltration membranes of the invention is easy to operate, and the Modified Membrane obtained has very Therefore good stability and good hydrophily and antifouling property can be widely applied to food industry, water process and environmental protection Etc. every field.
Specific embodiment
Embodiments of the present invention are illustrated by particular specific embodiment below, those skilled in the art can be by this explanation Content disclosed by book is understood other advantages and efficacy of the present invention easily.
Embodiment 1
A kind of preparation method can be carried out photo-crosslinking and the block polymer containing hydrophilic segment, including following step It is rapid:
15.77g 2- ihethoxyethyl methacrylate, 0.268g2- bromine isobutyl are added in the round-bottomed flask of 100ml Reaction system stirring and dissolving is led to argon gas Gu by sour mono methoxy glycol ester, 0.376g 2,2'- bipyridyl and 13ml methyl phenyl ethers anisole Reaction system, is then transferred in the round-bottomed flask of the 100ml equipped with 0.172g cuprous bromide by bubble 30 minutes, then deoxygenation, 70 DEG C of progress polymerization reaction 5h, reaction product are crossed neutral alumina pillar and then are deposited in ether, four after being diluted with methyl phenyl ethers anisole It is deposited in ether and is repeated twice again after the dissolution of hydrogen furans, be then dried in vacuo for 24 hours to constant weight, obtain under the conditions of 40 DEG C The brominated poly- 2- ihethoxyethyl methacrylate macromole evocating agent in end, chain length is about 100.
The brominated poly- 2- methoxy in addition 7.82g hydroxyethyl methacrylate, the end 13.14g in the round-bottomed flask of 100ml Base ethylmethyl acrylate macromole evocating agent, 0.313g 2,2'- bipyridyl and 20ml N, dinethylformamide, will be anti- System stirring and dissolving is answered, leads to argon gas Gu and steeps 30 minutes, then deoxygenation, then reaction system is transferred to equipped with 0.143g cuprous bromide 100ml round-bottomed flask in, in 50 DEG C of progress polymerization reaction 8h, reaction product is deposited in ether, methanol dissolution after again It is deposited in ether and is repeated twice, be then dried in vacuo under the conditions of 40 DEG C for 24 hours to constant weight, obtain poly- 2- methoxy ethyl first Base acrylate-b- poly hydroxy ethyl acrylate block polymer, poly hydroxy ethyl acrylate chain length is about 50.
15.15g 2- ihethoxyethyl methacrylate-b- polymethylacrylic acid is added in the round-bottomed flask of 100ml Methyl esters block polymer, 50mL pyridine, stirring and dissolving polymer 7.51g cinnamoyl chloride are added under condition of ice bath, in room temperature condition Under be stirred to react for 24 hours, reaction product precipitates in methyl alcohol, precipitates in methyl alcohol and is repeated twice again after chloroform dissolution, then It is dried in vacuo under the conditions of 40 DEG C for 24 hours to constant weight, obtains the acylated poly- first of poly- 2- ihethoxyethyl methacrylate-b- of cortex cinnamomi Base hydroxy-ethyl acrylate block polymer.
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
The above-mentioned block polymer of 0.5g is dissolved in 20mL methyl phenyl ethers anisole.The PVDF micro-filtration for being 0.22 μm by aperture specification Film impregnates 1 minute in copolymer solution.It drains to place it under 500 watts of ultraviolet lamps after solution and irradiate 1 hour.Then by spoke According to treated, film removes uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, and the PVDF of hydrophilic modifying can be obtained Microfiltration membranes.
Embodiment 2
A kind of preparation method can be carried out photo-crosslinking and the block polymer containing hydrophilic segment, including following step It is rapid:
The dry PEG5000 of 20.1g is dispersed in 100ml anhydrous methylene chloride, 0.51g pyridine is added, in ice-water bath Under the conditions of instill 1.09g 2- bromine isobutyl acylbromide.Then cancellation ice-water bath is warming up to naturally by reaction system reacts under room temperature Then 4h is successively washed with 0.1mol/L sodium hydroxide, 0.1mol/L hydrochloric acid solution, saturated sodium-chloride water solution.It is organic It is deposited in ether after being mutually concentrated, repeats washing of precipitate twice, vacuum drying obtains brominated PEG macromole evocating agent.
The brominated PEG macromolecular of 7.85g hydroxyethyl methacrylate, 5.01g is added in the round-bottomed flask of 100ml to cause Reaction system stirring and dissolving is led to argon gas Gu and steeped 30 minutes by agent, 0.315g 2,2'- bipyridyl and 15ml methanol, then deoxygenation, so Reaction system is transferred to afterwards in the round-bottomed flask of the 100ml equipped with 0.145g cuprous bromide, in 50 DEG C of progress polymerization reaction 8h, Reaction product is deposited in ether, is deposited in ether and is repeated twice again after methanol dissolution, then true under the conditions of 40 DEG C Sky is dry for 24 hours to constant weight, obtains PEG5000-b- poly hydroxy ethyl acrylate block polymer, poly hydroxy ethyl acrylate Chain length is about 50.
10.15g 2- ihethoxyethyl methacrylate-b- polymethylacrylic acid is added in the round-bottomed flask of 100ml Methyl esters block polymer, 50mL pyridine, stirring and dissolving polymer 7.35g cinnamoyl chloride are added under condition of ice bath, in room temperature condition Under be stirred to react for 24 hours, reaction product precipitates in methyl alcohol, precipitates in methyl alcohol and is repeated twice again after chloroform dissolution, then It is dried in vacuo under the conditions of 40 DEG C for 24 hours to constant weight, obtains the acylated PEG5000-b- poly hydroxy ethyl acrylate block of cortex cinnamomi Polymer.
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
The above-mentioned prepared block polymer of 0.5g is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 1 minute in copolymer solution.It drains to place it under 500 watts of ultraviolet lamps after solution and irradiate 1 hour. Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, hydrophilic change can be obtained The PVDF microfiltration membranes of property.
Embodiment 3
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
Block polymer prepared by 2g embodiment 1 is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 1 minute in copolymer solution.It drains to place it under 500 watts of ultraviolet lamps after solution and irradiate 1 hour. Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, hydrophilic change can be obtained The PVDF microfiltration membranes of property.
Embodiment 4
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
Block polymer prepared by 5g embodiment 1 is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 30 minutes in copolymer solution.Drain that irradiation 1 under 500 watts of ultraviolet lamps is placed it in after solution is small When.Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, parent can be obtained The modified PVDF microfiltration membranes of water.
Embodiment 5
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
Block polymer prepared by 1g embodiment 1 is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 60 minutes in copolymer solution.Drain that irradiation 24 under 30 watts of ultraviolet lamps is placed it in after solution is small When.Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, parent can be obtained The modified PVDF microfiltration membranes of water.
Embodiment 6
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
Block polymer prepared by 2g embodiment 2 is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 1 minute in copolymer solution.It drains to place it under 500 watts of ultraviolet lamps after solution and irradiate 1 hour. Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, hydrophilic change can be obtained The PVDF microfiltration membranes of property.
Embodiment 7
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
Block polymer prepared by 5g embodiment 2 is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 30 minutes in copolymer solution.Drain that irradiation 1 under 500 watts of ultraviolet lamps is placed it in after solution is small When.Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, parent can be obtained The modified PVDF microfiltration membranes of water.
Embodiment 8
A kind of method that PVDF micro-filtration is film hydrophilically modified, is realized by following steps:
Block polymer prepared by 3g embodiment 2 is dissolved in 20mL methyl phenyl ethers anisole.It is 0.22 μm by aperture specification PVDF microfiltration membranes are impregnated 10 minutes in copolymer solution.Drain that irradiation 24 under 30 watts of ultraviolet lamps is placed it in after solution is small When.Then the film after radiation treatment is removed into uncrosslinked block polymer with methyl phenyl ethers anisole washing by soaking three times, parent can be obtained The modified PVDF microfiltration membranes of water.
The hydrophilic modifying PVDF microfiltration membranes that embodiment is prepared are tested for the property below.Test method is as follows:
Membrane flux test:
Deionization is poured into ultrafiltration cup, the precompressed 30min under the pressurization of 0.1mpa nitrogen then calculates 100mL penetrating fluid Time used calculates membrane flux.
Rejection test:
The BSA solution of 1000ppm is poured into ultrafiltration cup, then the precompressed 30min under the pressurization of 0.1mpa nitrogen is collected and seeped Transparent liquid surveys its concentration with ultraviolet specrophotometer, calculates infiltration front and back concentration rejection.
Recovery rate test:
Film is polluted by bovine serum albumin, after then cleaning using sodium hypochlorite, calculates the recovery rate of membrane flux.
Water contact angle test:
Hydrolysis feeler is measured 10 points on a membrane sample using contact angle measurement and is averaged using drop method test of lying The water contact angle of film surface after the method for value characterizes before modified.
Underwater oil contact angle test:
Film is immersed under water, oily contact angle is tested using underwater oil drop method, using contact angle measurement in a membrane sample The water contact angle of film surface after the method that 10 points of surface measurements are averaged characterizes before modified.
The performance for the hydrophilic modifying PVDF microfiltration membranes that embodiment 1 to 8 is prepared is as shown in the table:
Table 1: the performance of the made PVDF microfiltration membranes of embodiment 1 to 8:
Above-described embodiment 1 to 8 is hydrophilic modifying PVDF microfiltration membranes, and comparative example is unmodified PVDF microfiltration membranes, can be seen Out, hydrophilic modifying PVDF microfiltration membranes of the invention membrane flux and in terms of be substantially better than unmodified pvdf membrane.
In addition, PVDF microfiltration membranes service life obtained by embodiment 1 to 8 is considerably longer than comparative example under equal conditions.
The above-described embodiments merely illustrate the principles and effects of the present invention, and is not intended to limit the present invention.It is any ripe The personage for knowing this technology all without departing from the spirit and scope of the present invention, carries out modifications and changes to above-described embodiment.Cause This, institute is complete without departing from the spirit and technical ideas disclosed in the present invention by those of ordinary skill in the art such as At all equivalent modifications or change, should be covered by the claims of the present invention.
The invention belongs to polymeric film material fields, and in particular to one kind can be carried out photo-crosslinking and contain hydrophilic segment Block polymer, and by the modified vinylidene microfiltration membranes of the block polymer to improve its hydrophilic and antifouling property side Method.
The shortcomings that in order to overcome existing PVDF microfiltration membranes hydrophilic modification method and deficiency, the primary purpose of the present invention is that mentioning It can be carried out photo-crosslinking and containing the block polymer of hydrophilic segment for a kind of.
It can be carried out photo-crosslinking and containing the block polymerization of hydrophilic segment another object of the present invention is to provide above-mentioned The preparation method of object.
A further object of the present invention is to provide a kind of methods that PVDF micro-filtration is film hydrophilically modified, are handed over by the above-mentioned light that can be carried out The connection reaction and block polymer coating containing hydrophilic segment in film surface and carries out photo-crosslinking and obtains.
The purpose of the invention is achieved by the following technical solution:
It is a kind of to can be carried out photo-crosslinking and the block polymer containing hydrophilic segment, it is by Formulas I and Formula II structural unit The block polymer of block polymer or Formulas I structural unit and the formula III composition of composition;Wherein, Formulas I and Formula II structural unit Number be 1-500;The number of Formula II structural unit is 1-500;The numerical value of n is 0-500 in formula III structure;
In Formulas I, R1 is hydrogen atom or methyl, and R2 is the acylated acrylatoalkoxysilanes ester of cortex cinnamomi, the acylated acyloxy of cortex cinnamomi Alkoxy ester can make to be crosslinked between polymer molecule under ultraviolet light;
Preferably, Formulas I structural unit is the acylated hydroxyethyl methacrylate of cortex cinnamomi, the acylated hydroxy-ethyl acrylate of cortex cinnamomi One of;
In Formula II, R3 is hydrogen atom or methyl, and R4 is the Arrcostab containing methoxyl group and ethyoxyl, can assign polymer Hydrophilicity;
Preferably, Formula II structural unit is 2- ihethoxyethyl methacrylate, 2- (2- methoxy ethoxy) ethyl One of methacrylate;
Formula III is mono methoxy polyethylene glycol quasi polymer (MPEG), has excellent hydrophilicity;
Preferably, formula III MPEG200, MPEG400, MPEG500, MPEG700, MPEG1000, MPEG1500, One of MPEG2000, MPEG5000, MPEG10000, MPEG20000.
It is above-mentioned to can be carried out photo-crosslinking and block polymer containing hydrophilic segment be by atom transfer freedom Base polymerization is prepared.
A kind of method that PVDF micro-filtration is film hydrophilically modified can be carried out photo-crosslinking and containing the embedding of hydrophilic segment by above-mentioned Section polymer is realized by following steps:
(1) PVDF microfiltration membranes are impregnated 1-100 minutes in copolymer solution;
(2) the PVDF microfiltration membranes after immersion are irradiated 1-48 hours under ultraviolet light, removes uncrosslinked block polymer The PVDF microfiltration membranes of hydrophilic modifying are obtained afterwards;
PVDF micro-filtration membrane aperture described in step (1) is 0.1-10 μm, with a thickness of 10-200 μm, porosity 10-80%;
The mass concentration of the polymer solution is 1-25%, and solvent is tetrahydrofuran, dioxane, acetone, benzene first One of ether, methylene chloride, chloroform;
Step (2) described ultraviolet light can use the ultraviolet light that commercial ultraviolet lamp issues, and the power of ultraviolet lamp tube can be 30 watts -1000 watts;
It is described remove uncrosslinked block polymer be using the method for solvent washing, solvent used be tetrahydrofuran, One of dioxane, acetone, methyl phenyl ethers anisole, methylene chloride, chloroform;
The principle of the present invention is: using with can be carried out photo-crosslinking and block polymer containing hydrophilic segment to change Property agent form coating in PVDF micro-filtration film surface using the method directly coated, it is then poly- using ultraviolet light crosslinked block It closes object coating and fixes its structure, to realize the hydrophilic modifying to PVDF microfiltration membranes.
Since hydrophilic polymeric segment has the ability of anti-organic contamination, it is thus possible to improve the anti-pollution of PVDF microfiltration membranes Metachromia energy.And crosslinkable polymer block is attached to PVDF microfiltration membranes table with can making coating stable after ultraviolet light cross-linking Face, to increase the stability and durability of coating.
The present invention has the following advantages and effects with respect to the prior art:
(1) block polymer used in the present invention had not only contained hydrophilic segment but also can carry out photo-crosslinking, to guarantee Gained hydrophilic modifying PVDF microfiltration membranes have good durability.
(2) block polymer of the invention can assign PVDF microfiltration membranes good hydrophilicity, so as to improve it Antifouling property.
(3) modifying process of hydrophilic modifying PVDF microfiltration membranes of the invention is very simple, and the Modified Membrane obtained has very Good stability and good hydrophilicity and antifouling property, therefore, can be widely used in food industry, water process, The every field such as environmental protection.

Claims (9)

1. a kind of method of the block polymer modified polyvinilidene fluoride microfiltration membranes containing hydrophilic segment, which is characterized in that including Following steps:
Step 1: polyvinylidene fluoride microporous filtering film is impregnated 1~100 minute in modifier solution;
Step 2: the polyvinylidene fluoride microporous filtering film after immersion is irradiated 1~48 hour under ultraviolet light, wash uncrosslinked to remove Block polymer, obtain the polyvinylidene fluoride microporous filtering film of hydrophilic modifying;
Wherein, the modifying agent is by Formulas I structural unit and Formula II structural unit or Formulas I structural unit and formula III structural unit The block polymer containing hydrophilic segment of composition:
Wherein, R1 is hydrogen atom or methyl, and R2 is the acylated acrylatoalkoxysilanes ester of cortex cinnamomi, and R3 is hydrogen atom or methyl, and R4 is Arrcostab containing methoxyl group and ethyoxyl;N is integer in formula III structure;In the Formula II structural unit, R4 is 2- methoxyl group One of ethylmethyl acrylate or 2- (2- methoxy ethoxy) ethylmethyl acrylate.
2. the method for the block polymer modified polyvinilidene fluoride microfiltration membranes according to claim 1 containing hydrophilic segment, It is characterized by: the modifier solution solvent for use is tetrahydrofuran, dioxane, acetone, methyl phenyl ethers anisole, two in step 1 One of chloromethanes or chloroform, the mass concentration of the modifier solution are 1~25%;In step 2 using tetrahydrofuran, It is uncrosslinked to remove that one of dioxane, acetone, methyl phenyl ethers anisole, methylene chloride or chloroform wash polyvinylidene fluoride microporous filtering film Block polymer.
3. the method for the block polymer modified polyvinilidene fluoride microfiltration membranes according to claim 1 containing hydrophilic segment, It is characterized by: in step 2, the ultraviolet light is the ultraviolet light that commercial ultraviolet lamp issues, the ultraviolet lamp power is 30 watts~ 1000 watts.
4. micro- to the block polymer modified polyvinilidene fluoride described in 3 any one containing hydrophilic segment according to claim 1 The method of filter membrane, it is characterised in that: the polyvinylidene fluoride microporous filtering film aperture is 0.1~10 μm, with a thickness of 10~200 μm, hole Gap rate is 10~80%.
5. a kind of block polymer containing hydrophilic segment, which is characterized in that its structural formula are as follows:
The block polymer containing hydrophilic segment be by Formulas I structural unit and Formula II structural unit or Formulas I structural unit with The block polymer of formula III structural unit composition;
Wherein, R1 is hydrogen atom or methyl, and R2 is the acylated acrylatoalkoxysilanes ester of cortex cinnamomi, and R3 is hydrogen atom or methyl, and R4 is Arrcostab containing methoxyl group and ethyoxyl;The integer that n is 0~500 in formula III structure;In the Formula II structural unit, R4 is One of 2- ihethoxyethyl methacrylate or 2- (2- methoxy ethoxy) ethylmethyl acrylate.
6. the block polymer according to claim 5 containing hydrophilic segment, it is characterised in that: the Formulas I structural unit In, R2 is the acylated hydroxyethyl methacrylate of cortex cinnamomi or one of the hydroxy-ethyl acrylate that cortex cinnamomi is acylated.
7. the block polymer according to claim 5 containing hydrophilic segment, it is characterised in that: the formula III structure list Member be MPEG200, MPEG400, MPEG500, MPEG700, MPEG1000, MPEG1500, MPEG2000, MPEG5000, One of MPEG10000 or MPEG20000.
8. the block polymer according to any one of claims 5 to 7 containing hydrophilic segment, it is characterised in that: Formulas I and The number of Formula II structural unit is 1~500.
9. a kind of preparation method for preparing the block polymer according to any one of claims 8 containing hydrophilic segment, it is characterised in that: logical It crosses atom transfer radical polymerization method and the block polymer, structural formula is prepared are as follows:
The block polymer containing hydrophilic segment be by Formulas I structural unit and Formula II structural unit or Formulas I structural unit with The block polymer of formula III structural unit composition;Wherein, R1 is hydrogen atom or methyl, and R2 is the acylated acyloxy alcoxyl of cortex cinnamomi Base ester, R3 are hydrogen atom or methyl, and R4 is 2- ihethoxyethyl methacrylate or 2- (2- methoxy ethoxy) ethyl first One of base acrylate;The integer that n is 0~500 in formula III structure.
CN201610918203.8A 2016-10-21 2016-10-21 The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment Active CN106632922B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610918203.8A CN106632922B (en) 2016-10-21 2016-10-21 The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610918203.8A CN106632922B (en) 2016-10-21 2016-10-21 The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment

Publications (2)

Publication Number Publication Date
CN106632922A CN106632922A (en) 2017-05-10
CN106632922B true CN106632922B (en) 2018-12-21

Family

ID=58856577

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610918203.8A Active CN106632922B (en) 2016-10-21 2016-10-21 The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment

Country Status (1)

Country Link
CN (1) CN106632922B (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109908776B (en) * 2019-04-04 2021-07-16 苏州科技大学 Anti-pollution composite distillation membrane based on amphiphilic network and preparation method thereof
EP3838388A1 (en) * 2019-12-19 2021-06-23 Solvay SA Polymer additive comprising zwitterionic moieties for vinylidene fluoride polymer based membranes
CN111467970A (en) * 2020-04-30 2020-07-31 郑州轻工业大学 Preparation method based on novel charged loose nanofiltration membrane
CN114525674B (en) * 2022-01-19 2024-03-22 河北钢铁集团矿业有限公司 High-performance anti-scaling modified filter cloth for vacuum filter and preparation method thereof
CN114522546B (en) * 2022-02-24 2022-11-29 泰州南潇新材料科技有限公司 High-hydrophilicity polysulfone ultrafiltration membrane and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999062510A2 (en) * 1998-06-01 1999-12-09 Angiotech Pharmaceuticals, Inc. Compositions comprising anti-microtubule agents for treating or preventing inflammatory diseases
US20090074708A1 (en) * 2005-01-05 2009-03-19 Yoa-Pu Hu Oliver Inhibitors and Enhancers of Uridine Diphosphate-Glucuronosyltransferase 2B (UGT2B)
CN102423644A (en) * 2011-08-15 2012-04-25 中科院广州化学有限公司 Hydrophobic porous composite membrane, preparation method, and application thereof
WO2014058252A1 (en) * 2012-10-10 2014-04-17 전북대학교 산학협력단 Ph-sensitive block copolymer containing cinnamaldehyde derivatives, and method for preparing same
CN104437121A (en) * 2014-10-17 2015-03-25 南京理工大学 PEO-b-PMMA modified PVDF ultrafiltration membrane and preparation process thereof
CN105289331A (en) * 2015-12-09 2016-02-03 苏州科技学院 Amphipathic three-block polymer PS(x)MAA(y)-g-fPEG(z) modified PVDF ultrafiltration membrane and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5794452B2 (en) * 2011-08-29 2015-10-14 林先文 Composition applied to skin and method for producing the same
KR101722827B1 (en) * 2015-01-29 2017-04-04 전북대학교산학협력단 Anticancer polymer for inducing formation of hydroxy radical and method for preparing the same

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999062510A2 (en) * 1998-06-01 1999-12-09 Angiotech Pharmaceuticals, Inc. Compositions comprising anti-microtubule agents for treating or preventing inflammatory diseases
US20090074708A1 (en) * 2005-01-05 2009-03-19 Yoa-Pu Hu Oliver Inhibitors and Enhancers of Uridine Diphosphate-Glucuronosyltransferase 2B (UGT2B)
CN102423644A (en) * 2011-08-15 2012-04-25 中科院广州化学有限公司 Hydrophobic porous composite membrane, preparation method, and application thereof
WO2014058252A1 (en) * 2012-10-10 2014-04-17 전북대학교 산학협력단 Ph-sensitive block copolymer containing cinnamaldehyde derivatives, and method for preparing same
CN104437121A (en) * 2014-10-17 2015-03-25 南京理工大学 PEO-b-PMMA modified PVDF ultrafiltration membrane and preparation process thereof
CN105289331A (en) * 2015-12-09 2016-02-03 苏州科技学院 Amphipathic three-block polymer PS(x)MAA(y)-g-fPEG(z) modified PVDF ultrafiltration membrane and preparation method thereof

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
Preparation and characterization of block copolymers containing cinnamate groups with end-capped ZnO;Florentina Jitaru,等;《Central European Journal of Chemistry》;20130930;第11卷(第9期);第1492-1504页 *
Preparing and structuring of block copolymers with cinnamate and adamantane moieties;Emil C. Buruiana,等;《Designed Monomers and Polymers》;20120815;第16卷(第1期);第1-13页 *
Structure and Ultrasonic Sensitivity of the Superparticles Formed by Self-Assembly of Single Chain Janus Nanoparticles;Feng Zhou,等;《Macromolecules》;20131117;第47卷;第365-372页 *
光敏性双亲嵌段共聚物的ATRP法合成及其胶束化行为的研究;奚朝晖;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20060815(第08期);B014-94页 *

Also Published As

Publication number Publication date
CN106632922A (en) 2017-05-10

Similar Documents

Publication Publication Date Title
CN106632922B (en) The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of block polymer containing hydrophilic segment
CN100411722C (en) Porous polyvinylidene blending porous membrane and process for producing same
Wang et al. Tailoring membrane surface properties and ultrafiltration performances via the self-assembly of polyethylene glycol-block-polysulfone-block-polyethylene glycol block copolymer upon thermal and solvent annealing
Feng et al. Highly effective antifouling performance of N-vinyl-2-pyrrolidone modified polypropylene non-woven fabric membranes by ATRP method
CN102755844B (en) Preparation method for surface ionization modified polysulfone ultrafiltration membrane
CN100562356C (en) Hydrophilic polyvinyl chloride alloy doughnut filter membrane and preparation method thereof
CN101513593B (en) Hydrophilic polyvinyl chloride membrane and preparation method thereof
Yang et al. Improved antifouling and antimicrobial efficiency of ultrafiltration membranes with functional carbon nanotubes
CN101112675A (en) Method for modifying compound film surface
CN106807257A (en) Based on metal-doped g C3N4Visible light catalytic hollow fiber ultrafiltration membrane and preparation method
Xing et al. MOFs self-assembled molecularly imprinted membranes with photoinduced regeneration ability for long-lasting selective separation
CN100384521C (en) Method for improving hydrophilicity of polymer porous membrane by dentritic branching molecule
CN105617882A (en) Chitosan modified graphene oxide nano composite positive osmotic membrane and preparation method thereof
Goushki et al. Free radical graft polymerization of 2-hydroxyethyl methacrylate and acrylic acid on the polysulfone membrane surface through circulation of reaction media to improve its performance and hemocompatibility properties
CN106478975B (en) The method of the preparation method and its modified polyvinilidene fluoride microfiltration membranes of difunctional block polymer
CN110538578B (en) Sewage treatment membrane with high decontamination efficiency and preparation method thereof
CN104258738A (en) Forward osmosis organic-inorganic composite membrane and preparation method thereof
CN105148750A (en) Method for modifying surface of polyamide composite film
CN107899432A (en) A kind of plate compounding NF membrane for water filter purification and preparation method thereof
CN109012245A (en) Imidazole salt poly ion liquid modified polyvinilidene fluoride charged membrane and preparation method
CN102512997B (en) Hydrophilic polyethersulfone with cardo alloy ultrafiltration membrane and preparation method thereof
Niu et al. Modification of a polyethersulfone membrane with a block copolymer brush of poly (2-methacryloyloxyethyl phosphorylcholine-co-glycidyl methacrylate) and a branched polypeptide chain of Arg–Glu–Asp–Val
CN106693730A (en) Nonmetal multi-doped nTiO2-based visible light catalysis hollow fiber ultrafiltration membrane and preparation method
JP2011156519A (en) Polymer water treatment film, water treatment method, and method for maintaining polymer water treatment film
CN109304105B (en) Forward osmosis membrane for efficiently adsorbing and removing heavy metal ions and preparation method and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant