CN105749766B - A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane - Google Patents

A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane Download PDF

Info

Publication number
CN105749766B
CN105749766B CN201610116417.3A CN201610116417A CN105749766B CN 105749766 B CN105749766 B CN 105749766B CN 201610116417 A CN201610116417 A CN 201610116417A CN 105749766 B CN105749766 B CN 105749766B
Authority
CN
China
Prior art keywords
nano
tio
casting solution
preparation
sol
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
CN201610116417.3A
Other languages
Chinese (zh)
Other versions
CN105749766A (en
Inventor
王志伟
张�杰
王巧英
曾豪
陈妹
郑君健
潘辰
张星冉
王煊博
吴志超
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.)
Tongji University
Original Assignee
Tongji University
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 Tongji University filed Critical Tongji University
Priority to CN201610116417.3A priority Critical patent/CN105749766B/en
Publication of CN105749766A publication Critical patent/CN105749766A/en
Application granted granted Critical
Publication of CN105749766B publication Critical patent/CN105749766B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • 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
    • B01D61/145Ultrafiltration
    • 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
    • B01D67/0002Organic membrane manufacture
    • 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
    • B01D69/12Composite membranes; Ultra-thin membranes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The present invention relates to a kind of Kynoar/TiO2Composite hyperfiltration membrane is made in the preparation method of Nano sol composite hyperfiltration membrane, including the preparation and mixing of Nano sol liquid precursors and reaction medium, the preparation of scattered, pre- casting solution and casting solution of Nano sol, film, the step such as subsequent treatment of extraction and film.The present invention is made by sol-gal process contains nano-TiO2The sol solutionses of nascent particle and with organic solvent be sufficiently mixed it is scattered after be blended into the pre- casting solution of polymer, the dispersed ultrafiltration composite membrane of nanometer is then made using immersion precipitation phase inversion process.Sol solutionses of the present invention process to be uniformly dispersed, stable replace powder state nano-TiO2Particle, effectively overcomes powder state nano particle and is added to and occur reuniting in casting solution and cause the unstable phenomenon of casting solution, the Compound Ultrafiltration film-strength height of gained, flux height, anti-pollution, easy cleaning, and production cost is low.

Description

A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane
Technical field
The present invention relates to a kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane, it is molten to be related to nanometer Glue, casting solution, film forming prepare three phases, and prepared film is applied to embrane method sewage treatment process, especially membrane biological reaction Application in device.
Background technology
Embrane method sewage treatment process is the novel process for developing application of membrane separation technology in sewage treatment area, because of tool Have the advantages that energy consumption is low, stable effluent quality and enjoy favor.Wherein, membrane Bio-reactor Technology is by membrane separation technique and dirt New process for treating waste water caused by the combination of aquatic organism treatment technology, has good effluent quality, facility compact, floor space Less, the advantages that anti impulsion load, operational management facilitate, had broad application prospects in terms of sewage disposal and reuse.As The core of membrane bioreactor and embrane method sewage disposal technology, the performance of film are to influence its service life and system run all right Property an important factor for, fouling membrane be limit application of membrane expand key, therefore its antipollution be modified be technical field of membrane Study hotspot.
Membrane material species is various, wherein being no lack of the polymeric material of function admirable, wherein Kynoar is because with good Chemical stability and film forming, heat resistance and excellent mechanical strength the features such as receive much concern in recent years.But its molecule knot Structure determines the low and stronger hydrophobic essence of its surface energy, therefore when carrying out aqueous phase separation, the Kynoar of one-component Film is easily absorbing the lyophobic dusts such as protein in water, colloidal particle and causes Pore Blocking and pollution, causes membrane filterability It can reduce, it is necessary to frequently clean, so as to shorten service life, limit its application.And to polyvinylidene fluoride film Hydrophilic modifying can reduce the interaction especially between protein between film surface and retention pollutant, so as to reduce pollution The absorption of material, improve the antifouling property of film.The hydrophilic modifying of film mainly has two methods:Surface is modified and this is modifies. The surface of film, which is modified, includes surface grafting, coating and chemical surface treatment etc., but surface modification can not be lasting there is effect The problems such as influence its actual sewage processing in application;Body method of modifying includes blending and modifying and modification by copolymerization, wherein common Mixed modification method can closely be tied due to additive between film matrix by various chemical bonds and other physics chemical actions Close, modified effect is stable, and operates relatively simple and receive significant attention.The material of blending and modifying includes such as polyvinyl alcohol, gathered The hydrophilic high molecular material of ether sulfone etc. and such as Nano-meter SiO_22, nano-TiO2Deng inorganic nano material.In recent years, nano material Because the property such as its small-size effect, hydrophilic is widely used in membrane modifying, wherein nano-TiO2Because belonging to high water wetted material(Contact Angle<18°), there is preferable chemical stability, antibiotic property, nontoxic and turn into study hotspot.But nano particle is higher Surface energy and specific surface area then add nano material Interaction Force and surface-active so that group easily occurs each other for particle Gather and gather, it is difficult to it is dispersed, it have impact on a nanometer blend film modified performance.
The A of CN 102091540 disclose sulfonated polyether sulfone/TiO2The preparation method of nano combined milipore filter, includes successively (1) preparation of hygrometric state sulfonated polyether sulfone milipore filter, (2) nano-TiO2The preparation of colloidal dispersion and (3) sulfonated polyether sulfone/ TiO2The self assembly of nano combined milipore filter prepares three steps.Step (1) and the preparation process class of pre- casting solution in this patent Seemingly.And step (2) is:By the nano-TiO that particle scale is 5-40 nm2Powder and dispersant in mass ratio 1: (0.1-0.2) Add in distilled water, be ultrasonically treated 0.5-1.0 H-shapeds at room temperature into nano-TiO2Colloidal dispersion.Step (3) is:By hygrometric state Sulfonated polyether sulfone milipore filter takes out from coagulating bath, is immersed in step (2) nano-TiO2Sonic oscillation 1-5 in colloidal dispersion Min, stand 1-3 h, nano-TiO2Hygrometric state sulfonated polyether sulfone/TiO is formed in sulfonated polyether sulfone film surface self-organization2It is nano combined Milipore filter, then by alcohol solution washing and 40-50 DEG C of drying of low temperature drying, obtain sulfonated polyether sulfone/TiO2It is nano combined super Filter membrane.First, nano-TiO in the patent2Prepared by colloidal dispersion is the addition by powder state particle, nano-powder The reunion of grain make it that it more difficult is uniformly dispersed.Secondly, sulfonated polyether sulfone/TiO in the patent2Nano combined milipore filter is by receiving Rice grain is self-assembly of poly (ether sulfone) film surface, due to nano-TiO2Particle belongs to highly polar material and sulfonated polyether sulfone The bad adhesion of base-material, and the nano-particle for being dispersed in film surface easily comes off, and the more difficult stabilization of film properties, limits it in actual membrane The application of method sewage treatment area.
The content of the invention
It is an object of the invention to overcome the shortcomings of that conventional nano is modified membrane preparation method, there is provided one kind can be to greatest extent Ground reduces the problem of nanometer skewness of blend film caused by nanometer reunion, ensures casting solution by using Nano sol liquid Stability, lift the strainability and antifouling property of nano composite membrane.
In order to achieve the above object, the technical solution adopted by the present invention is:
Kynoar/nano-TiO involved in the present invention2The preparation method of colloidal sol composite hyperfiltration membrane, including following step Suddenly:
(a) nano-TiO2The preparation of colloidal sol:By butyl titanate and absolute ethyl alcohol with 1:The volume ratio mixing of (9 ~ 18) is stirred 30min is mixed, obtains the precursors of clear homogeneous;By absolute ethyl alcohol and deionized water with 1:The volume ratio mixing group of (6 ~ 12) Into mixed solution, mechanical agitation 20min ~ 30min, and it is 1 ~ 3 with the pH value of dust technology or watery hydrochloric acid regulation mixed solution, obtains To homogeneous transparent solution be reaction medium;Precursors are added dropwise to reaction medium in 40 DEG C ~ 60 DEG C water-baths In, 1 ~ 2h of ultrasound is stirred, obtained faint yellow emulsion is nano-TiO2Sol solutionses;Control nano-TiO2Metatitanic acid in sol solutionses The volume ratio of four butyl esters and deionized water is 1: (0.5~1.5) ;
(b) Kynoar/nano-TiO2The preparation of colloidal sol composite hyperfiltration membrane casting solution:Organic solvent is divided into two parts, It is respectively used to the preparation of pre- casting solution and containing nano-TiO2Sol solutionses it is scattered, Kynoar is added to containing pore-foaming agent and In the mixed liquor of part organic solvent at 80 DEG C 3 ~ 5d of mechanical agitation, form the pre- casting solution of homogeneous;Then by ultrasonic disperse 20 ~ 30min's contains nano-TiO2The remainder organic solvent mixed liquor of sol solutionses is added to 1 ~ 2d of stirring in pre- casting solution, Formation prepares Kynoar/nano-TiO2The casting solution of colloidal sol composite hyperfiltration membrane;Wherein:For disperseing TiO2The amount of sol solutionses Volume ratio with total organic solvent amount is (0.15 ~ 0.35):1;
(c) Kynoar/nano-TiO2The preparation of colloidal sol composite hyperfiltration membrane:By step(B)Gained casting solution is cast in On glass plate or non-woven fabrics, spread to film, relative humidity be make under conditions of 45 ~ 70%, temperature is 15 DEG C ~ 40 DEG C it is organic molten 15 ~ 30s is evaporated in agent, and glass plate or non-woven fabrics then are immersed into 0.5 ~ 24h in the coagulating bath that temperature is 20 DEG C ~ 25 DEG C, make it Gel film forming, then filter membrane is taken out from coagulating bath, dry at room temperature, produce Kynoar/nano-TiO2Colloidal sol is compound super Filter membrane.
In the present invention, the organic solvent in described step (b) is dimethyl sulfoxide, DMA, N, N- bis- NMF, the combination of one or two kinds of arbitrary proportion in 1-METHYLPYRROLIDONE.
In the present invention, the total organic solvent mass concentration in described step (b) is 65 ~ 85%.
It is used to disperse TiO in the present invention, in the organic solvent being divided into two parts in described step (b)2The amount of sol solutionses Ratio with total organic solvent amount is (0.15 ~ 0.35):1.
In the present invention, one kind for polyethylene glycol or in polyvinylpyrrolidone of pore-foaming agent in described step (b) or The combination of two kinds of arbitrary proportions, mass concentration are 6 ~ 12%.
In the present invention, the Kynoar solution mass concentration in described step (b) is 8 ~ 16%.
In the present invention, TiO in the casting solution in described step (b)2Mass content is 0.01 ~ 5%.
In the present invention, the coagulating bath in described step (c) is arbitrarily compared for deionized water or deionized water with absolute ethyl alcohol The mixed liquor of example.
In the present invention, the knifing thickness control in described step (c) is 0.15 ~ 0.35 mm.
The present invention has the advantages that compared to prior art:
1)Instant invention overcomes sol-gal process to prepare nano-TiO2Length experimental period, the characteristics of process complexity, omit Nano-TiO2Two steps of gel and calcining in particulate production, enormously simplify operating process.
2)The present invention effectively overcomes powder state nano-TiO2The reunion precipitation that particle is added in polymeric casting film liquid is existing As so that casting solution is integrally uniform and stable, so as to which the dispersed polymer nanocomposite membrane of nanometer be made.
3)Using the method for organic solvent substep addition in the present invention, it is easy to the nascent particle of nanometer in Nano sol solution Dispersed and film casting solution stabilization.
Brief description of the drawings
Fig. 1 is nano-TiO in the colloidal sol of embodiment 32The TEM figures of nascent particle.
Fig. 2 is to determine casting solution stability result using Turbiscan multiple Scatterings technology in embodiment 1.
Fig. 3 prepares the photo after standing 4 months afterwards and at room temperature for casting solution in embodiment 1.(a) figure is just to prepare Casting solution photo afterwards, (b) figure are the casting solution photo after standing 4 months.
Fig. 4 is the film formation surface shape appearance figure of the nano composite membrane of embodiment 2.
Embodiment
Below in conjunction with specific embodiment, the invention will be further described, but scope of the present invention is not It is confined to the scope involved by embodiment.
Embodiment 1
(a) by butyl titanate and absolute ethyl alcohol with 1:12 ratios mix 30 min and obtain the reaction of clear homogeneous Presoma.Absolute ethyl alcohol and deionized water are with 6:The min of mixed solution mechanical agitation 30 of 1 ratio composition, and with dust technology or Watery hydrochloric acid regulation pH value is 2, and obtained homogeneous transparent solution is reaction medium.By precursors in 50 DEG C of water-baths by It is added dropwise in reaction medium, it is TiO that stirring 60 min of ultrasound, which obtain faint yellow emulsion,2Sol solutionses, TiO2Titanium in sol solutionses The ratio of sour four butyl esters and deionized water is 1:1.
(b) by 8% Kynoar be added to containing in 10% perforating agent and 62% organic solvent mixed liquor in 80 DEG C of machineries 4 d are stirred, form the pre- casting solution of homogeneous.The min of ultrasonic disperse 30 is then contained into 0.15%TiO2Sol solutionses and 20% organic The mixed liquor of solvent, which is added in pre- casting solution to stir to be formed after 2 d, prepares PVDF/ nano-TiOs2The casting solution of sol-gel modified film.
(c) above-mentioned casting solution is cast on non-woven fabrics, spreads to film, relative humidity be 60%, temperature be 25 DEG C Under the conditions of solvent is evaporated 15 s, it is that gel time is in 25 DEG C of coagulating baths that glass plate or non-woven fabrics then are immersed into temperature 0.5 h, make its gel film forming, then filter membrane is taken out from coagulating bath, dry at room temperature, that is, obtain PVDF/ nano-TiOs2Colloidal sol Composite hyperfiltration membrane.
Embodiment 2
(a) by butyl titanate and absolute ethyl alcohol with 1:12 ratios mix 30 min and obtain the reaction of clear homogeneous Presoma.Absolute ethyl alcohol and deionized water are with 6:The min of mixed solution mechanical agitation 30 of 1 ratio composition, and with dust technology or Watery hydrochloric acid regulation pH value is 2, and obtained homogeneous transparent solution is reaction medium.By precursors in 45 DEG C of water-baths by It is added dropwise in reaction medium, it is TiO that stirring 60 min of ultrasound, which obtain faint yellow emulsion,2Sol solutionses, TiO2Titanium in sol solutionses The ratio of sour four butyl esters and deionized water is 1:0.9.
(b) by 7% Kynoar be added to containing in 11% perforating agent and 64% organic solvent mixed liquor in 80 DEG C of machineries 5 d are stirred, form the pre- casting solution of homogeneous.The min of ultrasonic disperse 30 is then contained into 1% TiO2Sol solutionses and 17% organic molten The mixed liquor of agent, which is added in pre- casting solution to stir to be formed after 2 d, prepares PVDF/ nano-TiOs2The casting solution of sol-gel modified film.
(c) above-mentioned casting solution is cast on non-woven fabrics, spreads to film, relative humidity be 50%, temperature be 25 DEG C Under the conditions of solvent is evaporated 25 s, it is that gel time is in 25 DEG C of coagulating baths that glass plate or non-woven fabrics then are immersed into temperature 0.5 h, make its gel film forming, then filter membrane is taken out from coagulating bath, dry at room temperature, that is, obtain PVDF/ nano-TiOs2Colloidal sol Composite hyperfiltration membrane.
Embodiment 3
(a) by butyl titanate and absolute ethyl alcohol with 1:15 ratios mix 30 min and obtain the reaction of clear homogeneous Precursor.Absolute ethyl alcohol and deionized water are with 9:The min of mixed solution mechanical agitation 30 of 1 ratio composition, and with dust technology or Watery hydrochloric acid regulation pH value is 1.5, and obtained homogeneous transparent solution is reaction medium.By precursors in 60 DEG C of water-baths by It is added dropwise in reaction medium, it is TiO that stirring 20 min of ultrasound, which obtain faint yellow emulsion,2Sol solutionses, TiO2Titanium in sol solutionses The ratio of sour four butyl esters and deionized water is 1:0.8.
(b) by 10% Kynoar be added to containing in 8% perforating agent and 60% organic solvent mixed liquor in 80 DEG C of machineries 4 d are stirred, form the pre- casting solution of homogeneous.The min of ultrasonic disperse 30 is then contained into 0.5% TiO2Sol solutionses and 22% organic The mixed liquor of solvent, which is added in pre- casting solution to stir to be formed after 1 d, prepares PVDF/ nano-TiOs2The casting solution of sol-gel modified film.
(c) above-mentioned casting solution is cast on non-woven fabrics, spreads to film, relative humidity be 50%, temperature be 20 DEG C Under the conditions of solvent is evaporated 20 s, it is that gel time is in 25 DEG C of coagulating baths that glass plate or non-woven fabrics then are immersed into temperature 1 h, make its gel film forming, then filter membrane is taken out from coagulating bath, dry at room temperature, that is, obtain PVDF/ nano-TiOs2Colloidal sol is answered Close milipore filter.
In summary embodiment, analytic explanation accompanying drawing are as follows:
Fig. 1 is nano-TiO in the colloidal sol of embodiment 32The TEM figures of nascent particle, as can be seen from Figure nanometer come into being particle Particle diameter is between 5 ~ 10 nm.
Fig. 2 is to determine casting solution stability result using Turbiscan multiple Scatterings technology in embodiment 1, can by figure Find out in the min of minute 30, relatively steady always with height change transmitted light in sample cell, no crest or trough occur, and say Bright sample is stable.
Fig. 3 prepares the photo after standing 4 months afterwards and at room temperature for casting solution in embodiment 1.(a) figure is just to prepare Casting solution photo afterwards, (b) figure are the casting solution photo after standing 4 months.It is seen that sample it is highly stable and without precipitation and Flocculate agglomeration.
Fig. 4 is the film formation surface shape appearance figure of the nano composite membrane of embodiment 2.Nano particle is dispersed in film surface, nothing Obvious agglomeration occurs.

Claims (7)

  1. A kind of 1. Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane, it is characterised in that comprise the following steps:
    (a) nano-TiO2The preparation of colloidal sol:By butyl titanate and absolute ethyl alcohol with 1:The volume ratio of (9 ~ 18) mixes 30min, obtain the precursors of clear homogeneous;By absolute ethyl alcohol and deionized water with 1:The volume ratio mixing composition of (6 ~ 12) Mixed solution, mechanical agitation 20min ~ 30min, and be 1 ~ 3 with the pH value of dust technology or watery hydrochloric acid regulation mixed solution, obtain Homogeneous transparent solution be reaction medium;Precursors are added dropwise in reaction medium in 40 DEG C ~ 60 DEG C water-baths, 1 ~ 2h of ultrasound is stirred, obtained faint yellow emulsion is nano-TiO2Sol solutionses;Control nano-TiO2The fourth of metatitanic acid four in sol solutionses The volume ratio of ester and deionized water is 1: (0.5~1.5);
    (b) Kynoar/nano-TiO2The preparation of colloidal sol composite hyperfiltration membrane casting solution:Organic solvent is divided into two parts, used respectively In the preparation of pre- casting solution and containing nano-TiO2Sol solutionses disperse, and Kynoar is added to be had containing pore-foaming agent and part In the mixed liquor of solvent at 80 DEG C 3 ~ 5d of mechanical agitation, form the pre- casting solution of homogeneous;Then by ultrasonic disperse 20 ~ 30min's contains nano-TiO2The remainder organic solvent mixed liquor of sol solutionses is added to 1 ~ 2d of stirring, shape in pre- casting solution Into preparing Kynoar/nano-TiO2The casting solution of colloidal sol composite hyperfiltration membrane;Wherein:For disperseing TiO2The amount of sol solutionses with The volume ratio of total organic solvent amount is (0.15 ~ 0.35):1;
    (c) Kynoar/nano-TiO2The preparation of colloidal sol composite hyperfiltration membrane:Casting solution obtained by step (b) is cast in glass plate Or on non-woven fabrics, film is spread to, it is to make organic solvent evaporation under conditions of 45 ~ 70%, temperature is 15 DEG C ~ 40 DEG C in relative humidity 15 ~ 30s, glass plate or non-woven fabrics are then immersed into 0.5 ~ 24h in the coagulating bath that temperature is 20 DEG C ~ 25 DEG C, make its gel into Film, then filter membrane is taken out from coagulating bath, dry at room temperature, produce Kynoar/nano-TiO2Colloidal sol composite hyperfiltration membrane.
  2. 2. preparation method according to claim 1, it is characterised in that organic solvent is dimethyl sulfoxide, N, N- dimethylacetamides The combination of one or two kinds of arbitrary proportion in amine, DMF or 1-METHYLPYRROLIDONE.
  3. 3. preparation method according to claim 1, it is characterised in that in casting solution total organic solvent mass concentration be 65 ~ 85%。
  4. 4. preparation method according to claim 1, it is characterised in that pore-foaming agent is polyethylene glycol or polyvinylpyrrolidone One or both of arbitrary proportion combination, in casting solution mass concentration be 6 ~ 12%.
  5. 5. preparation method according to claim 1, it is characterised in that in casting solution Kynoar mass concentration be 8 ~ 16%。
  6. 6. preparation method according to claim 1, it is characterised in that coagulating bath be deionized water or deionized water with it is anhydrous The mixed liquor of ethanol arbitrary proportion.
  7. 7. preparation method according to claim 1, it is characterised in that knifing thickness control is 0.15 ~ 0.35 mm.
CN201610116417.3A 2016-03-02 2016-03-02 A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane Active CN105749766B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610116417.3A CN105749766B (en) 2016-03-02 2016-03-02 A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610116417.3A CN105749766B (en) 2016-03-02 2016-03-02 A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane

Publications (2)

Publication Number Publication Date
CN105749766A CN105749766A (en) 2016-07-13
CN105749766B true CN105749766B (en) 2018-02-09

Family

ID=56332300

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610116417.3A Active CN105749766B (en) 2016-03-02 2016-03-02 A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane

Country Status (1)

Country Link
CN (1) CN105749766B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022104072A1 (en) * 2020-11-13 2022-05-19 Saudi Arabian Oil Company Desalination membranes
WO2022104089A1 (en) * 2020-11-13 2022-05-19 Saudi Arabian Oil Company Desalination membranes

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106220886A (en) * 2016-08-16 2016-12-14 曹健 A kind of preparation method of modified polyvinilidene fluoride film
CN106178974B (en) * 2016-08-23 2018-09-21 北京碧水源膜科技有限公司 A kind of nano modification enhancement type hollow fiber film and preparation method thereof
CN108499363A (en) * 2018-04-28 2018-09-07 广西民族大学 The method of the nano-silicon dioxide modified PVDF dewatering microporous films of fabricated in situ
CN108854549A (en) * 2018-06-28 2018-11-23 江苏泓膜业科技有限公司 A kind of preparation method weaving tube enhancement type hollow fiber ultrafiltration membrane
CN111013555B (en) * 2019-12-31 2020-11-17 胡小青 Water treatment nano material composite membrane and preparation method thereof
CN111530504A (en) * 2020-05-11 2020-08-14 深圳市臻鼎环保科技有限公司 Photocatalytic sewage treatment membrane and preparation method thereof
CN112707438B (en) * 2020-12-08 2022-09-23 浙江理工大学 Preparation method of metal element-doped titanium dioxide/fluorine-containing polymer film composite material with photodegradation function
CN113244791B (en) * 2021-05-12 2022-06-17 佳木斯大学 Preparation method of emodin-blended phenolphthalein polyethersulfone ultrafiltration membrane
CN113457473B (en) * 2021-06-24 2022-08-19 同济大学 Preparation method of natural vermiculite nanoparticle modified PVDF ultrafiltration membrane

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102093717A (en) * 2010-12-28 2011-06-15 中国石油大学(华东) Sulfonated polyethersulfone/TiO2 nano composite material and preparation method thereof
CN102688705A (en) * 2011-03-22 2012-09-26 中国科学院生态环境研究中心 Hydrophilic modification method of PVDF ultrafilter membrane by utilization of nano-TiO2 sol

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100116733A1 (en) * 2008-11-12 2010-05-13 Korea Electrotechnology Research Institute Nanoporous oxide ceramic membranes of tubular and hollow fiber shape and method of making the same

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102093717A (en) * 2010-12-28 2011-06-15 中国石油大学(华东) Sulfonated polyethersulfone/TiO2 nano composite material and preparation method thereof
CN102688705A (en) * 2011-03-22 2012-09-26 中国科学院生态环境研究中心 Hydrophilic modification method of PVDF ultrafilter membrane by utilization of nano-TiO2 sol

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
TiO2对PVDF超滤膜结构与性能的影响;孙秀丽等;《膜科学与技术》;20110825;第31卷(第4期);第17-21页 *
TiO2改性聚偏氟乙烯的性能研究;朱愉洁等;《化工环保》;20090615;第29卷(第3期);第279-282页 *
TiO2溶胶改性PVDF超滤膜的制备与性能研究;余常友等;《塑料工业》;20141220;第42卷(第12期);第83-86页 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022104072A1 (en) * 2020-11-13 2022-05-19 Saudi Arabian Oil Company Desalination membranes
WO2022104089A1 (en) * 2020-11-13 2022-05-19 Saudi Arabian Oil Company Desalination membranes

Also Published As

Publication number Publication date
CN105749766A (en) 2016-07-13

Similar Documents

Publication Publication Date Title
CN105749766B (en) A kind of Kynoar/TiO2The preparation method of Nano sol composite hyperfiltration membrane
Dmitrieva et al. Polymeric membranes for oil-water separation: a review
CN102614783B (en) Method for preparing high-flux composite membrane from dopamine-modified nanometer material
CN108159888A (en) A kind of preparation method of the super hydrophilic ultrafiltration membrane with photocatalysis performance
Zeng et al. Preparation of a novel poly (vinylidene fluoride) ultrafiltration membrane by incorporation of 3-aminopropyltriethoxysilane-grafted halloysite nanotubes for oil/water separation
CN108854603A (en) A kind of preparation method coating modified ultrafiltration membrane altogether using dopamine and functionalized carbon nano-tube
Zhang et al. Treatment of wastewater containing oil using phosphorylated silica nanotubes (PSNTs)/polyvinylidene fluoride (PVDF) composite membrane
CN102166482A (en) Method for preparing nano functionalized high-molecular ultrafiltration membrane
Zhang et al. Polysulfone (PSF) composite membrane with micro-reaction locations (MRLs) made by doping sulfated TiO2 deposited on SiO2 nanotubes (STSNs) for cleaning wastewater
CN106621833A (en) Preparation method of ultrafiltration membrane with anti-fouling performance enhanced by nitrogen-doped graphene oxide/TiO2 composite particles
CN105457504A (en) Novel titanium dioxide nano-particle/polymer hybrid membrane and preparation method thereof
CN102688705A (en) Hydrophilic modification method of PVDF ultrafilter membrane by utilization of nano-TiO2 sol
CN104300164B (en) A kind of preparation method of compound proton exchange membrane
CN105749876B (en) A kind of preparation method of chitosan-modified graphene oxide quantum dot sorbing material
CN103418255B (en) A kind of thermo-sensitive type ultrafiltration membrane and preparation method thereof
CN104258745A (en) Preparation method of hydrophilic polyethersulfone microfiltration membrane
CN106914154A (en) PEG‑TiO2The preparation method of the hydrophilic milipore filters of/PES/PVA and application
CN102091540A (en) Preparation method of sulfonated polyethersulfone/TiO2 nano composite ultrafiltration membrane
Ma et al. Hydrophilic PAA-g-MWCNT/TiO2@ PES nano-matrix composite membranes: Anti-fouling, antibacterial and photocatalytic
CN103127839A (en) Method for improving polyvinylidene fluoride (PVFD) ultrafiltration membrane anti-pollution ability
Wang et al. Design of a novel poly (aryl ether nitrile)-based composite ultrafiltration membrane with improved permeability and antifouling performance using zwitterionic modified nano-silica
CN109260969A (en) A kind of preparation method and applications of graphene oxide/mesoporous silicon oxide composite hyperfiltration membrane
CN102688703B (en) Method for modifying cellulose acetate ultrafiltration membrane
CN106582316A (en) Preparation method of alcoholized GO-SiO2 particle modified flat plate composite forward osmotic membrane
CN107051208B (en) Doping Kynoar mixed-matrix ultrafiltration membrane and its preparation is blended in three-dimensional structure nano-complex

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant