CN106064024B - Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof - Google Patents

Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof Download PDF

Info

Publication number
CN106064024B
CN106064024B CN201610469322.XA CN201610469322A CN106064024B CN 106064024 B CN106064024 B CN 106064024B CN 201610469322 A CN201610469322 A CN 201610469322A CN 106064024 B CN106064024 B CN 106064024B
Authority
CN
China
Prior art keywords
graphene oxide
polysulfones
fibre membrane
hollow
preparation
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
CN201610469322.XA
Other languages
Chinese (zh)
Other versions
CN106064024A (en
Inventor
张敏敏
姚勇
秦舒浩
张凯舟
杨敬葵
谢高艺
邵慧菊
靳进波
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.)
Guizhou Yihua Membrane Technology Co.,Ltd.
Original Assignee
GUIZHOU MATERIAL TECHNOLOGY INNOVATION BASE
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 GUIZHOU MATERIAL TECHNOLOGY INNOVATION BASE filed Critical GUIZHOU MATERIAL TECHNOLOGY INNOVATION BASE
Priority to CN201610469322.XA priority Critical patent/CN106064024B/en
Publication of CN106064024A publication Critical patent/CN106064024A/en
Application granted granted Critical
Publication of CN106064024B publication Critical patent/CN106064024B/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
    • B01D71/66Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
    • B01D71/68Polysulfones; Polyethersulfones
    • 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
    • B01D67/0079Manufacture of membranes comprising organic and inorganic components
    • 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
    • B01D69/08Hollow fibre membranes
    • 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
    • B01D71/02Inorganic material
    • B01D71/021Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2325/00Details relating to properties of membranes
    • B01D2325/24Mechanical properties, e.g. strength

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses a kind of polysulfones-graphene oxide hollow-fibre membranes and preparation method thereof.The present invention is directed to polysulfones(PSF)The problem of doughnut film properties, introduce graphene oxide, surface modification is carried out to graphene oxide using super critical CO 2 technology, can it is fully dispersed in a polymer matrix, and it is arranged in pairs or groups using specific component, both the toughness of ps hollow fiber uf membrane had been improved, increase the application range of polysulfones base hollow-fibre membrane, under the premise of so that ps hollow fiber uf membrane is kept preferable water flux and rejection again, the comprehensive mechanical performance and antifouling property of ps hollow fiber uf membrane, the more stable doughnut film composite material of forming properties can be improved.

Description

Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof
Technical field
The present invention relates to technical field of polymer materials, especially a kind of polysulfones-graphene oxide hollow-fibre membrane and its Preparation method.
Background technology
Polysulfones is due to its good chemical stability, water resistance, heat resistance, dimensional stability and preferable film forming And mechanical strength, it has been obtained widely in micro-filtration, reverse osmosis, ultrafiltration, electrodialysis, gas separation, bioengineering, medical treatment etc. Using being particularly suitable for application to the excellent hemodialysis membrane of processability, polysulfones material is a kind of membrane material for applying very much Material.But existing ps hollow fiber uf membrane there is also hydrophilies problem not high, easy to pollute, water is handled in practical applications It is inefficient, while film is easy to be contaminated, and the service life of film is caused to reduce.
Invention content
The purpose of the present invention is:A kind of polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof is provided, it is significantly carried The hydrophily of PS membrane has been supplied, and has improved mechanical strength and hardness, permeability and resistance tocrocking are also very excellent, to overcome The deficiencies in the prior art.
The invention is realized in this way:Polysulfones-graphene oxide hollow-fibre membrane, is calculated, including according to the mass fraction with 15- 20 parts of polysulfones, 1.2-1.7 parts of sulfonated polysulfone, 33-37 parts of polyethylene glycol, 42-48 parts of DMAC N,N' dimethyl acetamides and 0.01-1 Part graphene oxide.
The preparation method of polysulfones-graphene oxide hollow-fibre membrane takes each component, by above-mentioned quality by above-mentioned mass fraction Number takes each component, includes the following steps:
1) polysulfones and sulfonated polysulfone are dried in vacuo 12-24 hours at 65-75 DEG C respectively;
2) processed graphene oxide is added in n,N-dimethylacetamide, then oxidation stone is made by ultrasonic power Black alkene is dispersed in DMAC N,N' dimethyl acetamide;
3) then be included in it is dry after sulfonated polysulfone, polyethylene glycol and it is dry after polysulfones filled under conditions of 65-75 DEG C Divide stirring 10-15h, form it into homogeneous casting solution, and carry out vacuum defoamation, then passes through spinneret and form dynamic analysis of spinning, warp It crosses the air gap between spinneret and coagulating bath to immerse in coagulating bath, passes through solvent n,N-dimethylacetamide and non-solvent water Mass transfer exchange and form hollow-fibre membrane.
Air gap length between the spinneret and coagulating bath is 1-5cm, and the temperature of the air gap is 20-50 DEG C, humidity 50-80%.The temperature and humidity for ensureing the air gap, exclude the influence of environment.Control the warm and humid of the air gap Degree, being capable of effective solution environment temperature and influence of the humidity to hollow fiber film structure and performance.
The graphene oxide by graphene oxide, modifying agent and cosolvent before use, be first put into overcritical dioxy Change in carbon reaction kettle, carries out, reacted under conditions of reaction temperature is 40 DEG C, reaction pressure >=20MPa, reaction time are 2h Cheng Hou, fast pressure relief 3-5 times repeatedly, obtain the graphene oxide of supercritical carbon dioxide treatment, using by overcritical dioxy Change graphene oxide and the preparation of carbon processing.
The ultrasonic power of the ultrasonic power is 50-300W, time 0.5-2h.
The polyethylene glycol polymeric degree is 400-6000, and the sulfonation degree of sulfonated polysulfone is 15-30%.
When using supercritical carbon dioxide treatment graphene oxide, modifying agent is added, modifier used is:Quaternary ammonium salt The mass ratio of Lei, phosphonium salts classes or silane coupling agent, the modifying agent of addition and graphene oxide to be modified is 1-100: 10-100.
The quaternary ammonium salt is cetyl ammonium bromide;Suo Shu phosphonium salt classes are cetyl phosphonium chloride or ethoxy three Ben Ji phosphonium chlorides;The silane coupling agent is KH550 or KH560.
The homogeneous casting solution of the formation is specifically that under 60-75 DEG C of temperature condition, the polyethylene glycol of half is added It in the n,N-dimethylacetamide solution evenly dispersed to graphene oxide, is sufficiently stirred, then by the polysulfones and sulphur after drying Change polysulfones to be uniformly mixed by high-speed mixer, is divided into tripartite, in mass ratio example 4: 3: 3, puts into solution in batches, often Minor tick 1.5-2.5h, while solution is added in remaining polyethylene glycol incessantly, it is sufficiently stirred 10-15h, is formed it into The casting solution of phase.
By adopting the above-described technical solution, compared with prior art, the present invention is directed to polysulfones (PSF) doughnut film property The problem of energy, introduces graphene oxide, and surface modification is carried out to graphene oxide using super critical CO 2 technology, It fully dispersed and can be arranged in pairs or groups in a polymer matrix using specific component, both improve ps hollow fiber uf membrane Toughness, increase the application range of polysulfones base hollow-fibre membrane, and ps hollow fiber uf membrane is made to keep preferable water flux and cut Under the premise of staying rate, the comprehensive mechanical performance and antifouling property of ps hollow fiber uf membrane can be improved, forming properties are more steady Fixed doughnut film composite material.
Specific implementation mode
The present invention is further described specifically by the following examples.In following embodiment, each component Dosage is weight consumption.It is necessarily pointed out that following embodiment is served only for, the present invention is described further, no It can be interpreted as limiting the scope of the invention, field technology skilled person is the present invention according to aforementioned present invention content Go out some nonessential modifications and adaptations, still falls within protection scope of the present invention.
The embodiment of the present invention 1:Polysulfones-graphene oxide hollow-fibre membrane, is calculated according to the mass fraction, including with 18.5 parts Polysulfones, 1.5 parts of sulfonated polysulfone, 35.6 parts of polyethylene glycol 400,44.4 parts of DMAC N,N' dimethyl acetamides and 0.05 part of graphite oxide Alkene.
The preparation method of polysulfones-graphene oxide hollow-fibre membrane takes each component by above-mentioned mass fraction, including walks as follows Suddenly:
1) polysulfones and sulfonated polysulfone are dried in vacuo 24 hours at 70 DEG C respectively;
2) graphene oxide described in before use, first graphene oxide is put into supercritical carbon dioxide reaction kettle, It carries out under conditions of reaction temperature is 40 DEG C, reaction pressure >=20MPa, reaction time are 2h, after the completion of reaction, quickly unloads Pressure, 3-5 times repeatedly, obtains the graphene oxide of supercritical carbon dioxide treatment, using by supercritical carbon dioxide treatment Graphene oxide and preparation;It adds graphene oxide into n,N-dimethylacetamide, then oxidation stone is made by ultrasonic power Black alkene is dispersed in DMAC N,N' dimethyl acetamide;The ultrasonic power of the ultrasonic power is 200W, time 1h;
3) then be included in it is dry after sulfonated polysulfone, polyethylene glycol 400 and it is dry after polysulfones filled under conditions of 70 DEG C Divide stirring 12h, form it into homogeneous casting solution, and carry out vacuum defoamation, then dynamic analysis of spinning is formed by spinneret, by spray The air gap between filament plate and coagulating bath is immersed in coagulating bath, and the biography of solvent n,N-dimethylacetamide and non-solvent water is passed through Mass transter and form hollow-fibre membrane;The temperature of the air gap between the spinneret and coagulating bath is 30 DEG C, humidity≤ 20%.
After testing, the performance indicator of the product of embodiment 1 is:Internal diameter 500-700um, wall thickness 200-300um, pure water flux ≥180L·m-2·h-1, to rejection >=98% of bovine serum albumin (67000).
The embodiment of the present invention 2:Polysulfones-thermoplastic elastomer (TPE)-organo montmorillonite blend hollow fiber membrane, by mass fraction Calculate, include with 15 parts of polysulfones, 1.7 parts of sulfonated polysulfone, 33 parts of polyethylene glycol 400,48 parts of n,N-dimethylacetamide and 0.01 part of graphene oxide.
The preparation method is the same as that of Example 1.
After testing, the performance indicator of the product of embodiment 1 is:Internal diameter 1000-1200um, wall thickness 100-150um, pure water are logical Amount >=250Lm-2·h-1, to rejection >=90% of bovine serum albumin (67000).
The embodiment of the present invention 3:Polysulfones-thermoplastic elastomer (TPE)-organo montmorillonite blend hollow fiber membrane, by mass fraction Calculate, include with 20 parts of polysulfones, 1.2 parts of sulfonated polysulfone, 37 parts of polyethylene glycol 400,42 parts of n,N-dimethylacetamide and 0.01 part of graphene oxide.
The preparation method is the same as that of Example 1.
After testing, the performance indicator of the product of embodiment 1 is:Internal diameter 500-700um, wall thickness 200-250um, pure water flux ≥180L·m-2·h-1, to rejection >=95% of bovine serum albumin (67000).
Comparative example 1
By comparing a kind of patent of invention " preparation method of permanent hydrophilic type polysulfone ultrafiltration membrane " embodiment seven, solid content For the pure water flux 130Lm of 20% polysulfone ultrafiltration membrane-2·h-1, bovine serum albumin rejection 96%, by add it is modified Graphene oxide, under the conditions of identical solid content, using this patent preparation method, the pure water of polysulfones/graphene oxide of preparation Flux >=180Lm-2·h-1, 38.5% is improved, to rejection >=98% of bovine serum albumin (67000), performance is obviously excellent In comparison PS membrane.
The experimental result of experimental data and comparative example according to the embodiment is it is known that technical scheme of the present invention improves The toughness of ps hollow fiber uf membrane, increase polysulfones base hollow-fibre membrane application range, and make ps hollow fiber uf membrane keep compared with Under the premise of good water flux and rejection, the comprehensive mechanical performance and antifouling property of ps hollow fiber uf membrane can be improved, The more stable doughnut film composite material of forming properties.

Claims (9)

1. a kind of polysulfones-graphene oxide hollow-fibre membrane, it is characterised in that:It calculates according to the mass fraction, including poly- with 15-20 parts Sulfone, 1.2-1.7 part sulfonated polysulfone, 33-37 parts of polyethylene glycol, 42-48 parts of N, N- dimethylacetylamides and 0.01-1 parts of oxidations Graphene;It is prepared as follows:
Each component is taken by above-mentioned mass fraction, is included the following steps:
1)Polysulfones and sulfonated polysulfone are dried in vacuo 12-24 hours at 65-75 DEG C respectively;
2)Processed graphene oxide is added to N, in N- dimethylacetylamides, then graphite oxide is made by ultrasonic power Alkene is dispersed in N, in N- dimethylacetylamides;
3)Then the polysulfones after addition is dry after sulfonated polysulfone, polyethylene glycol and drying fully stirs under conditions of 65-75 DEG C 10-15h is mixed, forms it into homogeneous casting solution, and carry out vacuum defoamation, then dynamic analysis of spinning is formed by spinneret, by spray The air gap between filament plate and coagulating bath is immersed in coagulating bath, by solvent N, N- dimethylacetylamides and non-solvent water Mass transfer exchanges and forms hollow-fibre membrane;
The graphene oxide by graphene oxide, modifying agent and cosolvent before use, be first put into supercritical carbon dioxide In reaction kettle, carried out under conditions of reaction temperature is 40 DEG C, reaction pressure >=20MPa, reaction time are 2h, reaction is completed Afterwards, fast pressure relief 3-5 times repeatedly, obtains the graphene oxide of supercritical carbon dioxide treatment, using by overcritical titanium dioxide The graphene oxide of carbon processing participates in preparing;
When using supercritical carbon dioxide treatment graphene oxide, modifying agent is added, modifier used is:Quaternary ammonium salt, The mass ratio of phosphonium salt class or silane coupling agent, the modifying agent of addition and graphene oxide to be modified is 1-100:10-100.
2. a kind of preparation method of polysulfones as described in claim 1-graphene oxide hollow-fibre membrane, it is characterised in that:It presses Above-mentioned mass fraction takes each component, includes the following steps:
1)Polysulfones and sulfonated polysulfone are dried in vacuo 12-24 hours at 65-75 DEG C respectively;
2)Processed graphene oxide is added to N, in N- dimethylacetylamides, then graphite oxide is made by ultrasonic power Alkene is dispersed in N, in N- dimethylacetylamides;
3)Then the polysulfones after addition is dry after sulfonated polysulfone, polyethylene glycol and drying fully stirs under conditions of 65-75 DEG C 10-15h is mixed, forms it into homogeneous casting solution, and carry out vacuum defoamation, then dynamic analysis of spinning is formed by spinneret, by spray The air gap between filament plate and coagulating bath is immersed in coagulating bath, by solvent N, N- dimethylacetylamides and non-solvent water Mass transfer exchanges and forms hollow-fibre membrane.
3. the preparation method of polysulfones according to claim 2-graphene oxide hollow-fibre membrane, it is characterised in that:It is described Spinneret and coagulating bath between air gap length be 1-5cm, the temperature of the air gap is 20-50 DEG C, humidity 50- 80%。
4. the preparation method of polysulfones according to claim 2-graphene oxide hollow-fibre membrane, it is characterised in that:It is described Graphene oxide before use, first graphene oxide, modifying agent and cosolvent are put into supercritical carbon dioxide reaction kettle, It carries out under conditions of reaction temperature is 40 DEG C, reaction pressure >=20MPa, reaction time are 2h, after the completion of reaction, quickly unloads Pressure, 3-5 times repeatedly, obtains the graphene oxide of supercritical carbon dioxide treatment, using by supercritical carbon dioxide treatment Graphene oxide participates in preparing.
5. the preparation method of polysulfones according to claim 2-graphene oxide hollow-fibre membrane, it is characterised in that:It is described Ultrasonic power ultrasonic power be 50-300W, time 0.5-2h.
6. the preparation method of polysulfones according to claim 2-graphene oxide hollow-fibre membrane, it is characterised in that:It is described Polyethylene glycol polymeric degree be 400-6000, the sulfonation degree of sulfonated polysulfone is 15-30%.
7. the preparation method of polysulfones according to claim 4-graphene oxide hollow-fibre membrane, it is characterised in that:It is adopting When with supercritical carbon dioxide treatment graphene oxide, modifying agent is added, modifier used is:Quaternary ammonium salt, phosphonium salts class or The mass ratio of silane coupling agent, the modifying agent of addition and graphene oxide to be modified is 1-100:10-100.
8. the preparation method of polysulfones according to claim 7-graphene oxide hollow-fibre membrane, it is characterised in that:It is described Quaternary ammonium salt be cetyl ammonium bromide;Suo Shu phosphonium salt classes are cetyl phosphonium chloride or hydroxyethyl triphenyl phosphonium chloride; The silane coupling agent is KH550 or KH560.
9. the preparation method of polysulfones according to claim 2-graphene oxide hollow-fibre membrane, it is characterised in that:It is described The homogeneous casting solution of formation be specifically that under 60-75 DEG C of temperature condition, the polyethylene glycol of half is added to graphene oxide In evenly dispersed N, N- dimethylacetamide solution, be sufficiently stirred, then by after drying polysulfones and sulfonated polysulfone pass through height Fast mixing machine is uniformly mixed, and is divided into tripartite, in mass ratio example 4:3:3, it puts into solution in batches, per minor tick 1.5- 2.5h, while solution is added in remaining polyethylene glycol incessantly, it is sufficiently stirred 10-15h, forms it into homogeneous casting film Liquid.
CN201610469322.XA 2016-06-25 2016-06-25 Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof Active CN106064024B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610469322.XA CN106064024B (en) 2016-06-25 2016-06-25 Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610469322.XA CN106064024B (en) 2016-06-25 2016-06-25 Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof

Publications (2)

Publication Number Publication Date
CN106064024A CN106064024A (en) 2016-11-02
CN106064024B true CN106064024B (en) 2018-10-26

Family

ID=57420608

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610469322.XA Active CN106064024B (en) 2016-06-25 2016-06-25 Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof

Country Status (1)

Country Link
CN (1) CN106064024B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106582298A (en) * 2016-12-09 2017-04-26 西安建筑科技大学 Three-dimensional GO sheet sphere particle modified organic composite ultra/micro filtering membrane preparing method
CN107570021B (en) * 2017-01-17 2021-09-10 贵州师范大学 Hydrophilic polysulfone/silicon dioxide blended hollow fiber membrane and preparation method thereof
IT201800010402A1 (en) * 2018-11-16 2020-05-16 Consiglio Nazionale Ricerche METHOD FOR THE TREATMENT OF A POROUS SUBSTRATE
CN110813110B (en) * 2019-11-14 2021-06-25 泰州清润环保科技有限公司 Graphene composite photocatalytic ultrafiltration membrane and preparation method thereof
CN112642308A (en) * 2019-12-03 2021-04-13 贵州省材料技术创新基地 Polysulfone-biochar blending separation membrane and preparation method thereof
CN112175177B (en) * 2020-10-15 2023-01-20 贵州省材料技术创新基地 Catalyst and preparation method thereof, and preparation method of polylactic acid
CN112403291A (en) * 2020-11-12 2021-02-26 杭州艾珀耐特工程科技有限公司 High-performance PVDF film and preparation method thereof
CN112774468A (en) * 2020-12-18 2021-05-11 任国峰 Graphene polysulfone ultrafiltration membrane and preparation method thereof
CN112844082A (en) * 2020-12-30 2021-05-28 桐乡市艾维科技有限公司 Porous graphene grafted polysulfone high-flux gas separation membrane material and preparation method thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104096488A (en) * 2014-08-01 2014-10-15 天津工业大学 Preparation method of polymer/graphene oxide composite separating membrane
CN105582821A (en) * 2016-02-22 2016-05-18 国家海洋局第三海洋研究所 Membrane casting solution of functionalized graphene composite ultrafiltration membrane and preparation method of functionalized graphene composite ultrafiltration membrane

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104096488A (en) * 2014-08-01 2014-10-15 天津工业大学 Preparation method of polymer/graphene oxide composite separating membrane
CN105582821A (en) * 2016-02-22 2016-05-18 国家海洋局第三海洋研究所 Membrane casting solution of functionalized graphene composite ultrafiltration membrane and preparation method of functionalized graphene composite ultrafiltration membrane

Also Published As

Publication number Publication date
CN106064024A (en) 2016-11-02

Similar Documents

Publication Publication Date Title
CN106064024B (en) Polysulfones-graphene oxide hollow-fibre membrane and preparation method thereof
CN109289550B (en) Preparation method and application of anti-pollution polyvinylidene fluoride hybrid ultrafiltration membrane
CN102114390A (en) Reinforced type polyvinylidene fluoride hollow fiber hydrophobic membrane and preparation method thereof
CN106031847B (en) A kind of preparation method for adulterating inorganic/organic nano particle forward osmosis membrane
CN104607063B (en) PVDF permanently hydrophilic ultrafiltration membrane and modification method thereof
CN102755841A (en) Preparation method and product of hydrophobic PVDF (Polyvinylidene Fluoride) microporous membrane with beta crystalline phase structure
CN106693728A (en) In-situ compatibilization organic-inorganic hybrid membrane and preparation method
CN105597552A (en) Forward osmosis membrane with high water flux and high salt rejection rate and method for preparing forward osmosis membrane with one-step method
CN109464917A (en) The preparation method of the modified doughnut desalination membrane of graphene oxide
CN106268371A (en) A kind of polyacrylonitrile hollow fiber ultrafilter membrane and preparation method thereof
CN102029114A (en) Hydrophilic hollow fiber membrane and preparation method thereof
CN107008164A (en) A kind of method that high flux PVDF perforated membranes are prepared based on metal hydroxides nanofiber
CN112354366B (en) High-flux composite reverse osmosis membrane and preparation method thereof
CN106000133B (en) Polysulfones-thermoplastic elastomer (TPE)-organo montmorillonite blend hollow fiber membrane and preparation method thereof
CN106898802A (en) A kind of high-performing car hydrogen fuel cell composite nano-powder material and preparation method thereof
CN107570021B (en) Hydrophilic polysulfone/silicon dioxide blended hollow fiber membrane and preparation method thereof
CN108043234A (en) The preparation method of ultrafiltration membrane
CN112808019A (en) Method for preparing polyaryletherketone tubular membrane by using green solvent thermal-induced phase method
CN102512987B (en) Method for preparing high-flux polyvinylidene fluoride hollow fiber membrane
CN110975636A (en) Preparation method of ultrafiltration membrane
CN116212640A (en) Preparation method of quaternized and sulfonated polyethersulfone ultrafiltration membrane
CN113893710B (en) High-flux polyethylene water treatment membrane and preparation method thereof
CN109499384A (en) A kind of method that hot water post-processing prepares high-flux nanofiltration membrane with pH regulation
CN108565380B (en) Preparation method of lithium ion battery diaphragm
CN107413209A (en) A kind of gas separation membrane based on molybdenum disulfide/CNT polyether block amide

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
TR01 Transfer of patent right

Effective date of registration: 20211130

Address after: 550000 Room 516, building B, Shuobo entrepreneurship Park, Guiyang National High tech Industrial Development Zone, Guiyang City, Guizhou Province

Patentee after: Guizhou Yihua Membrane Technology Co.,Ltd.

Address before: 550025 Baiyun North Road New Material Industrial Park, Baiyun District, Guiyang City, Guizhou Province

Patentee before: GUIZHOU MATERIAL TECHNOLOGY INNOVATION BASE

TR01 Transfer of patent right