WO2004096418A1 - Hollow fiber ultrafilter membrane with poly(phthalazinone ether fulfone), poly(phthalazinone ether ketone) or poly(phthalazinone ether sulfone ketone) and preparation thereof - Google Patents
Hollow fiber ultrafilter membrane with poly(phthalazinone ether fulfone), poly(phthalazinone ether ketone) or poly(phthalazinone ether sulfone ketone) and preparation thereof Download PDFInfo
- Publication number
- WO2004096418A1 WO2004096418A1 PCT/CN2004/000295 CN2004000295W WO2004096418A1 WO 2004096418 A1 WO2004096418 A1 WO 2004096418A1 CN 2004000295 W CN2004000295 W CN 2004000295W WO 2004096418 A1 WO2004096418 A1 WO 2004096418A1
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- WIPO (PCT)
- Prior art keywords
- hollow fiber
- membrane
- diazanaphthalene
- polyethersulfone
- poly
- Prior art date
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- 239000012528 membrane Substances 0.000 title claims abstract description 87
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- -1 poly(phthalazinone ether ketone Chemical class 0.000 title claims abstract description 9
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 title abstract description 12
- IJAPPYDYQCXOEF-UHFFFAOYSA-N phthalazin-1(2H)-one Chemical compound C1=CC=C2C(=O)NN=CC2=C1 IJAPPYDYQCXOEF-UHFFFAOYSA-N 0.000 title abstract 3
- 239000000654 additive Substances 0.000 claims abstract description 15
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract description 11
- 230000000996 additive effect Effects 0.000 claims abstract description 11
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 10
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims abstract description 10
- 150000002576 ketones Chemical class 0.000 claims abstract description 10
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M lithium chloride Chemical compound [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 claims abstract description 10
- IIPYXGDZVMZOAP-UHFFFAOYSA-N lithium nitrate Chemical compound [Li+].[O-][N+]([O-])=O IIPYXGDZVMZOAP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 229920000136 polysorbate Polymers 0.000 claims abstract description 9
- 230000008569 process Effects 0.000 claims abstract description 4
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims abstract description 3
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims abstract description 3
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims abstract description 3
- 238000000108 ultra-filtration Methods 0.000 claims description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 31
- 239000004695 Polyether sulfone Substances 0.000 claims description 28
- 229920006393 polyether sulfone Polymers 0.000 claims description 28
- WCZVZNOTHYJIEI-UHFFFAOYSA-N cinnoline Chemical group N1=NC=CC2=CC=CC=C21 WCZVZNOTHYJIEI-UHFFFAOYSA-N 0.000 claims description 19
- 239000002904 solvent Substances 0.000 claims description 18
- 239000000243 solution Substances 0.000 claims description 15
- 229920001643 poly(ether ketone) Polymers 0.000 claims description 14
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 claims description 12
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- 238000009987 spinning Methods 0.000 claims description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 9
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 9
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 9
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 9
- 239000002202 Polyethylene glycol Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- 229920001223 polyethylene glycol Polymers 0.000 claims description 8
- 239000000945 filler Substances 0.000 claims description 7
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 6
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 claims description 6
- 230000009477 glass transition Effects 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 5
- SOQBVABWOPYFQZ-UHFFFAOYSA-N oxygen(2-);titanium(4+) Chemical compound [O-2].[O-2].[Ti+4] SOQBVABWOPYFQZ-UHFFFAOYSA-N 0.000 claims description 5
- 238000007872 degassing Methods 0.000 claims description 4
- 238000001704 evaporation Methods 0.000 claims description 4
- 230000008020 evaporation Effects 0.000 claims description 4
- 238000001914 filtration Methods 0.000 claims description 4
- 235000006408 oxalic acid Nutrition 0.000 claims description 4
- 229920002818 (Hydroxyethyl)methacrylate Polymers 0.000 claims description 3
- WOBHKFSMXKNTIM-UHFFFAOYSA-N Hydroxyethyl methacrylate Chemical compound CC(=C)C(=O)OCCO WOBHKFSMXKNTIM-UHFFFAOYSA-N 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 3
- 239000005543 nano-size silicon particle Substances 0.000 claims description 3
- 235000005985 organic acids Nutrition 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 238000000465 moulding Methods 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 239000004094 surface-active agent Substances 0.000 claims description 2
- 238000009849 vacuum degassing Methods 0.000 claims description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims 2
- AEMRFAOFKBGASW-UHFFFAOYSA-N Glycolic acid Natural products OCC(O)=O AEMRFAOFKBGASW-UHFFFAOYSA-N 0.000 claims 1
- 229960000583 acetic acid Drugs 0.000 claims 1
- 239000012362 glacial acetic acid Substances 0.000 claims 1
- 229940093915 gynecological organic acid Drugs 0.000 claims 1
- 230000004907 flux Effects 0.000 abstract description 12
- 239000002994 raw material Substances 0.000 abstract description 8
- 239000000126 substance Substances 0.000 abstract description 7
- 239000003513 alkali Substances 0.000 abstract description 6
- 229920002492 poly(sulfone) Polymers 0.000 abstract description 2
- GAWIXWVDTYZWAW-UHFFFAOYSA-N C[CH]O Chemical group C[CH]O GAWIXWVDTYZWAW-UHFFFAOYSA-N 0.000 abstract 1
- 239000003963 antioxidant agent Substances 0.000 abstract 1
- 230000003078 antioxidant effect Effects 0.000 abstract 1
- AINBZKYUNWUTRE-UHFFFAOYSA-N ethanol;propan-2-ol Chemical compound CCO.CC(C)O AINBZKYUNWUTRE-UHFFFAOYSA-N 0.000 abstract 1
- 235000011187 glycerol Nutrition 0.000 abstract 1
- 150000007524 organic acids Chemical class 0.000 abstract 1
- 229920000151 polyglycol Polymers 0.000 abstract 1
- 239000010695 polyglycol Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 description 9
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 6
- 239000012530 fluid Substances 0.000 description 6
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 5
- 229910052801 chlorine Inorganic materials 0.000 description 5
- 239000000460 chlorine Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000005260 corrosion Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 239000002033 PVDF binder Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000007654 immersion Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 229920002239 polyacrylonitrile Polymers 0.000 description 3
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- 108010017384 Blood Proteins Proteins 0.000 description 2
- 102000004506 Blood Proteins Human genes 0.000 description 2
- 108010044091 Globulins Proteins 0.000 description 2
- 102000006395 Globulins Human genes 0.000 description 2
- 239000012888 bovine serum Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000001471 micro-filtration Methods 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000002861 polymer material Substances 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 230000001954 sterilising effect Effects 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229920001214 Polysorbate 60 Polymers 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- RYTLGWCJESCDMY-UHFFFAOYSA-N carbamimidoyl chloride Chemical compound NC(Cl)=N RYTLGWCJESCDMY-UHFFFAOYSA-N 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- XGZRAKBCYZIBKP-UHFFFAOYSA-L disodium;dihydroxide Chemical compound [OH-].[OH-].[Na+].[Na+] XGZRAKBCYZIBKP-UHFFFAOYSA-L 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 108010074605 gamma-Globulins Proteins 0.000 description 1
- 238000001891 gel spinning Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000002086 nanomaterial Substances 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 238000000614 phase inversion technique Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/52—Polyethers
- B01D71/521—Aliphatic polyethers
- B01D71/5211—Polyethylene glycol or polyethyleneoxide
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L81/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing sulfur with or without nitrogen, oxygen or carbon only; Compositions of polysulfones; Compositions of derivatives of such polymers
- C08L81/06—Polysulfones; Polyethersulfones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0011—Casting solutions therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0002—Organic membrane manufacture
- B01D67/0009—Organic membrane manufacture by phase separation, sol-gel transition, evaporation or solvent quenching
- B01D67/0016—Coagulation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/08—Hollow fibre membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/52—Polyethers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/66—Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
- B01D71/68—Polysulfones; Polyethersulfones
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
- C08L71/08—Polyethers derived from hydroxy compounds or from their metallic derivatives
- C08L71/10—Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/22—Thermal or heat-resistance properties
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2325/00—Details relating to properties of membranes
- B01D2325/32—Melting point or glass-transition temperatures
Definitions
- the invention belongs to the technical field of hollow fiber ultrafiltration membrane separation. Specifically, the present invention relates to diazanaphthalene-polyethersulfone, -polyetherketone, and -polyethersulfone-type hollow fiber ultrafiltration membrane and a preparation method thereof. Background technique
- Ultrafiltration membranes are one of the most widely used separation membranes. Ultrafiltration membranes can be used to separate macromolecular, colloidal and small molecule solvents. Ultrafiltration membranes have been widely used in water treatment, wastewater treatment and water resource recycling; or used in petrochemical, biochemical, fine chemical, pharmaceutical and chemical, mechanical metallurgy, textile printing and dyeing, food light industry, agriculture, animal husbandry and aquatic products industries In the separation, purification and concentration of raw materials and products. In the application process of ultrafiltration membranes, due to different processing objects, different operating conditions, different methods of membrane pretreatment, sterilization, and cleaning, different requirements are often imposed on the material of the membrane.
- biotechnology the pillar of economic development in the 21st century, the separation and purification of its products is the key to the transfer of biotechnology from laboratory research to industrial production.
- Purification and separation of most biological products require membranes to withstand high-temperature sterilization above 120 ° C and resistance to organic solvent corrosion.
- ultrafiltration membranes are required to have good characteristics such as resistance to oxidation, acid and alkali, and resistance to free chlorine.
- materials for preparing ultrafiltration membranes include inorganic ceramics and organic polymer materials.
- Inorganic ceramic materials can be resistant to high temperatures, solvents, and chemical corrosion, but the film is expensive to manufacture, expensive, and not conducive to large-scale applications.
- the organic polymer film has low cost and low price, and can be popularized and applied on a large scale.
- the ultrafiltration membrane products provided to users in various countries around the world mainly include cellulose acetate membrane (CA), polysulfone membrane (PSF), polyethersulfone membrane (PES), polyacrylonitrile membrane (PAN), and polyvinylidene fluoride membrane. (PVDF) and so on.
- the operating temperature of these ultrafiltration membranes must not exceed 70 ° C.
- the maximum operating temperature of the CA membrane is 30 ° C
- the maximum operating temperature of the PAN membrane is 60 ° C
- the maximum operating temperature of the PVDF membrane, PSF membrane, and PES membrane At 70 ° C, this limits the application of the membrane.
- the pure water flux was 580 Kg / m 2 .h, and the membrane's rejection rate to polyethylene glycol with a molecular weight of 12,000 was above 90%. After the membrane was treated in water at a temperature of 100 ° C for 10 minutes, the retention rate of the peroxanthracene dye increased, and the flux decreased by 30%.
- hollow fiber membrane Compared with flat membrane, hollow fiber membrane has the advantages of simple membrane module manufacturing process, large filling area and low manufacturing cost, which is conducive to large-scale popularization and application. Summary of the Invention
- the object of the present invention is to provide diazanaphthalene-polyethersulfone, -polyetherketone and -polyethersulfone ketone hollow fiber ultrafiltration membrane and a preparation method thereof.
- the invention selects three novel polymers as membrane materials, and prepares an ultrafiltration membrane with high temperature resistance, solvent resistance, oxidation resistance, acid and alkali resistance, and chlorine resistance, and a large membrane flux.
- the diaza-naphthalene-polyethersulfone, -polyetherketone, or -polyethersulfone ketone hollow fiber ultrafiltration membrane of the present invention contains: a polymer P, which is selected from polyetherketone (PPEK) containing a diazanaphthalene structure 2, polyethersulfone (PPES) containing diaza-naphthalene structure and polyethersulfone (PPESK) containing diaza-naphthalene structure, wherein the polyethersulfone (PPES) containing diaza-naphthalene structure is represented by I) means:
- PPEK polyether ketone
- n 400-600, and their glass transition temperatures are 253-263 ⁇ ; polyethersulfone ketone (PPESK) containing diazanaphthalene structure is represented by formula (m):
- the weight ratio of F / P is 0-1 / 2.
- the invention also provides a method for preparing diazanaphthalene-polyethersulfone, -polyetherketone and -polyethersulfone ketone hollow fiber ultrafiltration membrane, which comprises the following steps:
- a film-forming liquid having the following composition is prepared in a melting pot:
- Polymer P selected from polyethersulfone (PPES) containing a diazanaphthalene structure represented by formula (I), polyetherketone (PPEK) containing a diazanaphthalene structure represented by formula ( ⁇ ), and Polyethersulfone ketone (PPESK) containing a diazanaphthalene structure represented by formula ( ⁇ ),
- Solvent S which is selected from N, N-dimethylacetamide (DMAc :), N-methylpyrrolidone (MP), N, N-dimethylformamide (DMF), chloroform (CHC1 3 ), dichloro Methane (CH 2 C1 2 ) and a mixture of any two of them,
- Additive A which is selected from the group consisting of Tween, polyethylene glycol, polyethylene's pyrrolidone, ethanol, isopropanol, glycerol, acetone, ethylene glycol, diethylene glycol, hydroxyethyl methacrylate, Lithium chloride, lithium nitrate and C 2 ⁇ C 5 organic acids, and '
- Optional filler F selected from nano titanium dioxide and nano silicon dioxide
- the weight ratio of P / (P + S) is 15 ⁇ 25%
- a / P weight ratio is 0.01-1 / 1
- F / P weight ratio is 0-1 / 2;
- the prepared film-forming liquid is stirred at a temperature of 80 to 100 ° C for 15 to 24 hours, so that the polymer P and the additive A are sufficiently dissolved in the solvent S, and the filler F is uniformly dispersed in the film-forming liquid to become Uniform film-forming solution,
- Core fluid ultrafiltration water, or an aqueous solution containing 1 to 50% by weight of the above solvent, the temperature is 5 to 60 ° C, the flow rate is 0.3 to 3.0 IJh,
- Air gap 0 ⁇ 1500mm, evaporation temperature is room temperature,
- First gel bath ultrafiltration water or demineralized water with a hardness of 2 to 3 mol / L, or an aqueous solution containing 1 to 10% by weight of the above-mentioned solvent, which optionally contains 0 to 1% by weight of a surfactant at a temperature of 0 ⁇ 60 ° C,
- Second gel bath ultrafiltration water, temperature 30 ⁇ 60 ° C, '
- the forming steps are:
- the primary ecological fiber membrane is sequentially introduced into the first gel tank and the second gel tank through the air gap, and then directed to the winding roller.
- PPEK polyetherketone
- PPES polyethersulfone
- PPESK polyethersulfone ketone
- the present invention has performed experiments on the chemical stability of these three materials, and the results are shown in Table 2.
- the experimental conditions were: a film with a thickness of 50 to 60 m was prepared from these three materials, and the film was immersed in 11 kinds of aqueous solutions shown in Table 2, the temperature of the solution was 40 ° C, and the soaking time was 30 days. After experimental tests, the quality, thickness, and strength of the film did not change before and after immersion, proving that these three materials have good acid and alkali resistance, oxidation resistance, and chlorine resistance.
- PPESK Solvents used in the present invention include N, N-dimethylacetamide (DMAc), ⁇ , ⁇ -dimethylformamide (DMF), N-methylpyrrolidone (NMP), chloroform (CHC1 3 ), two For chloroformamidine (CH 2 C1 2 ) or a mixture of the two, DMAc or MP is preferably used.
- the percentage concentration of polymers in the hollow-fiber ultrafiltration membrane-forming solution is greater than 14%, which is different from existing literatures. High polymer concentration (10 ⁇ 14%).
- Additives used in the present invention include Tween, polyethylene glycol, polyvinylpyrrolidone, ethanol, isopropanol, glycerol, acetone, ethylene glycol, diethylene glycol, and hydroxyethyl methacrylate , Lithium chloride, lithium nitrate, C 2 ⁇ C 5 organic acids, etc., preferably Tween (T-60, T-40, T-20), polyethylene glycol (molecular weight 400, 600, 1000, 2000) and oxalic acid .
- the additives of the present invention have an important effect on improving membrane flux.
- the filler used in the present invention includes nano titanium dioxide and nano silicon dioxide, and the diameter of the particles is preferably 10 to 50 nm. Since the porous membrane of polymer materials will have a certain degree of shrinkage and deformation at high temperatures, adding a certain amount of inorganic nanomaterials as fillers can improve the stability of the membrane structure and reduce its shrinkage and deformation under high temperature conditions.
- a dry-wet spinning method and a dipping gel phase inversion method are used to prepare a hollow fiber ultrafiltration membrane.
- the hollow fiber ultrafiltration membrane prepared according to the method of the present invention has an outer diameter of 0.5 to 2 ir and a wall thickness of 0.1 to 0.4 mm.
- the present invention measures the pure water flux and rejection rate of the produced hollow fiber membrane.
- the measurement was performed using deionized water at 25 V, the operating pressure was 0.1 MPa, the molecular weight of bovine serum protein was 67,000, and the molecular weight of Y globulin was 150,000.
- the hollow fiber ultrafiltration membrane prepared by the present invention can withstand high temperature and solvent corrosion, and has good oxidation resistance and acid resistance. Alkali and chlorine resistance.
- the water flux measured after treatment in 100 ⁇ of water for 30 minutes was only 1 to 5% lower than that of the untreated membrane.
- the PPESK hollow fiber ultrafiltration membrane prepared by using the oxalic acid as an additive in the present invention has excellent comprehensive performance, not only has good high temperature resistance, oxidation resistance, solvent resistance performance, but also has a large flux.
- This large-throughput ultrafiltration membrane has a sponge-like structure.
- the inner surface pores of the hollow fiber belong to ultrafiltration, and the outer surface pores belong to microfiltration.
- hollow fiber membranes were prepared according to steps 5.1-5.4 of the preparation method described above, wherein the spinning kettle pressure was 0.1 MPa, the spinning dope temperature (pot temperature) was 30 ° C, and the draft speed was 25 m / min, ultrafiltration water with a core fluid of 60 ° C and an air gap of 0, and the first gel bath and the second gel bath are both 60 ⁇ ultrafiltration water.
- the performance of the obtained hollow ultrafiltration membrane was tested. Under the conditions of operating pressure of 0.1 MPa and temperature of 25 ° C, the pure water flux of the membrane was 650 L / m 2 .h, and the rejection rate of the membrane to bovine serum protein was 80%, and the rejection rate to gamma globulin was 91%.
- Example 11 The hollow fiber ultrafiltration membranes of Examples 2 to 10 were prepared with different raw material compositions and preparation conditions shown in Table 3 below. The test performances of the membranes are also listed in Table 3.
- Example 11 The test performances of the membranes are also listed in Table 3.
- hollow fiber membranes are prepared according to steps 5.1-5.4 of the preparation method of the present invention, wherein the spinning kettle pressure is 0.4 MPa, and the spinning dope temperature ( Kettle temperature) 60 V, traction speed 30m / min, 'core fluid temperature is 60 ° C, water flow is 3L / h, air gap is 1500mm, the first gel bath is demineralized water with a hardness of 3 mol / L, the temperature is 60 ° C, the second gel bath is 60 ° C ultrafiltration water.
- the spinning kettle pressure is 0.4 MPa
- the spinning dope temperature Kettle temperature
- traction speed 30m / min traction speed 30m / min
- 'core fluid temperature 60 ° C
- water flow is 3L / h
- air gap is 1500mm
- the first gel bath is demineralized water with a hardness of 3 mol / L
- the temperature is 60 ° C
- the second gel bath is 60 ° C ultrafiltration water.
- the filter membrane has a sponge-like structure.
- the inner surface pores of the hollow fiber belong to ultrafiltration, and the outer surface pores belong to microfiltration.
- the hollow fiber ultrafiltration membranes of Examples 12 to 18 were prepared with different raw material compositions and preparation conditions shown in Table 4 below. The test performances of the membranes are listed in Table 4 at the same time. Examples 19 to 24
- the hollow fiber ultrafiltration membranes of Examples 19 to 26 were prepared by using different raw material compositions and preparation conditions shown in Table 5 below.
- the number in [] is the mass of the raw material for film making (g);
- Ti0 2 nanoparticle diameter of 10 ⁇ 30 nm, particle diameter of the nano Si0 2 is 30 ⁇ 50 nanometers t
- the quantity in [] is the mass of the raw material for film making (g);
- the average molecular weight of PPESK is 220,000;
- Test conditions operating pressure O.lMpa, operating temperature 25 ⁇ .
- the number in [] is the mass of the raw material for film making (g);
- the average molecular weight of PPES is 200,000, and the average molecular weight of PPEK is 160,000;
- Test conditions operating pressure O.lMpa, operating temperature 25 ° C.
Abstract
The present invention provides a hollow fiber ultrafilter membrane with Poly(Phthalazinone Ether Fulfone) (PPES), Poly(Phthalazinone Ether Ketone) (PPEK) or Poly(Phthalazinone Ether Fulfone Ketone) (PPESK) and preparation thereof, wherein using PPES, PPEK or PPESK as raw materials to prepare hollow fiber ultrafilter membrane, whose vitrifying temperature is higher about 63-115°C than that of general commercial polysulfones, and whose chemical stabilitis are very good. Additive selected from tween, polyglycol, polyvinylpyrrolidone, ethanol isopropanol, propanetriol, acetone, ethylene glycol, diglycol, hydroxyethyl metrhacrylate, lithium chloride, lithium nitrate, C2-C5 organic acid ETAL is added into the solution of preparing membrane. The present invention further provides a forming method and process conditions of hollow fiber ultrafilter membrane with PPES, PPEK or PPESK. The hollow fiber ultrafilter membranes prepared thereof exhibit good properties, such as high-temp. Resistance, dissolvant resistance, acid-alkali resistance and antioxidant, as well as a larger membrane permeation flux.
Description
二氮杂萘-聚醚砜、 -聚醚酮和-聚醚砜酮类中空纤维超滤膜及其制备方法 - 技术领域 Diazanaphthalene-polyethersulfone, -polyetherketone and -polyethersulfone-ketone hollow fiber ultrafiltration membrane and preparation method thereof-Technical Field
本发明属于中空纤维超滤膜分离技术领域。 具体地说， 本发明涉及二氮杂萘- 聚醚砜、 -聚醚酮和-聚醚砜酮类中空纤维超滤膜及其制备方法。 背景技术 The invention belongs to the technical field of hollow fiber ultrafiltration membrane separation. Specifically, the present invention relates to diazanaphthalene-polyethersulfone, -polyetherketone, and -polyethersulfone-type hollow fiber ultrafiltration membrane and a preparation method thereof. Background technique
超滤膜是使用最广泛的分离膜之一。 用超滤膜可以实现大分子物质、 胶体物 质与小分子溶剂的分离。 超滤膜已广泛用于水处理、 废水处理和水资源的再生回 用； 或用于石油化工、 生物化工、 精细化工、 医药化工、 机械冶金、 纺织印染、 食品轻工、 农畜水产等工业中进行原料及产品的分离、 提纯及浓缩。 超滤膜在应 用过程中， 由于处理对象不同、 运行条件不同、 膜的预处理、 消毒灭菌、 清洗方 法的不同， 往往对膜的材质提出各种不同的要求。 例如作为 21世纪促进经济发展 支柱的生物技术， 其产品的分离、 提纯是生物技术从实验室研究转为工业化生产 的关键。大多数生物产品的提纯与分离， 要求膜能经受 120°C以上的高温灭菌， 且 耐有机溶剂腐蚀。 又如， 在水处理、 废水处理中应用时要求超滤膜有好的耐氧化、 耐酸碱、 耐游离氯等特性。 Ultrafiltration membranes are one of the most widely used separation membranes. Ultrafiltration membranes can be used to separate macromolecular, colloidal and small molecule solvents. Ultrafiltration membranes have been widely used in water treatment, wastewater treatment and water resource recycling; or used in petrochemical, biochemical, fine chemical, pharmaceutical and chemical, mechanical metallurgy, textile printing and dyeing, food light industry, agriculture, animal husbandry and aquatic products industries In the separation, purification and concentration of raw materials and products. In the application process of ultrafiltration membranes, due to different processing objects, different operating conditions, different methods of membrane pretreatment, sterilization, and cleaning, different requirements are often imposed on the material of the membrane. For example, biotechnology, the pillar of economic development in the 21st century, the separation and purification of its products is the key to the transfer of biotechnology from laboratory research to industrial production. Purification and separation of most biological products require membranes to withstand high-temperature sterilization above 120 ° C and resistance to organic solvent corrosion. For another example, when applied in water treatment and wastewater treatment, ultrafiltration membranes are required to have good characteristics such as resistance to oxidation, acid and alkali, and resistance to free chlorine.
目前， 制备超滤膜的材料有无机陶瓷及有机高分子材料。 无机陶瓷材料可耐 高温、 耐溶剂、 耐化学腐蚀， 但膜制造成本高， 价格昂贵、 不利于大规模推广应 用。 而有机高分子膜成本低， 价格便宜， 可以大规模推广应用。 当前世界各国提 供给用户的超滤膜商品， 主要有醋酸纤维素膜 （CA)、 聚砜膜 （PSF)、 聚醚砜膜 (PES ), 聚丙烯腈膜（PAN)、 聚偏氟乙烯膜 （PVDF) 等。 这些超滤膜的使用温 度均不能超过 70°C， 例如 CA膜的最髙使用温度为 30°C， PAN膜的最高使用温度 为 60°C， PVDF膜、 PSF膜、 PES膜的最高使用温度为 70°C， 这就限制了膜的应 用。 为了满足各个工业领域对超滤膜日益增长的需求， 迫切需要研究和开发同时 兼有耐高温、 耐有机溶剂、 耐酸碱化学腐蚀、 耐氧化、 耐游离氯等性能优良的超 滤膜。 At present, materials for preparing ultrafiltration membranes include inorganic ceramics and organic polymer materials. Inorganic ceramic materials can be resistant to high temperatures, solvents, and chemical corrosion, but the film is expensive to manufacture, expensive, and not conducive to large-scale applications. The organic polymer film has low cost and low price, and can be popularized and applied on a large scale. At present, the ultrafiltration membrane products provided to users in various countries around the world mainly include cellulose acetate membrane (CA), polysulfone membrane (PSF), polyethersulfone membrane (PES), polyacrylonitrile membrane (PAN), and polyvinylidene fluoride membrane. (PVDF) and so on. The operating temperature of these ultrafiltration membranes must not exceed 70 ° C. For example, the maximum operating temperature of the CA membrane is 30 ° C, the maximum operating temperature of the PAN membrane is 60 ° C, and the maximum operating temperature of the PVDF membrane, PSF membrane, and PES membrane At 70 ° C, this limits the application of the membrane. In order to meet the increasing demand for ultrafiltration membranes in various industrial fields, there is an urgent need to research and develop ultrafiltration membranes that have high temperature resistance, organic solvent resistance, acid and alkali chemical corrosion resistance, oxidation resistance, and free chlorine resistance.
蹇锡高等人， Preparation of UF and NF poly (phthalazine ether sulfone ketone) membranes for high temperature application, Journal of membrane science, 1999, 161(1), 185-191,在实验室中用含二氮杂萘结构的聚醚砜酮 (PPESK)制备了平板 超滤膜， 采用 N—甲基吡咯焼酮为溶剂， 以丁酮、 乙二醇甲醚或***作为添加剂 进行制膜。制膜液中 PPESK的质量百分比浓度是 10〜14%，添加剂的质量百分比 浓度为 2〜18%。研究膜材料耐化学腐蚀性的结果表明， 膜在常温下， 在表 1所示 的 8种溶液中浸泡 2周， 膜的厚度保持不变。
表 1 PPESK平板膜在 8种溶液中浸泡 2周的实验结果
他们还考察了聚合物的含量、 添加剂的种类和含量以及蒸发时间对膜性能的 影响。 研究得出， 当 PPESK在制膜液中的含量为 10重量％， 丁酮为添加剂， 蒸 发时间 25秒， 凝胶浴为 60Ό水时， 制出的平板超滤膜在 O.lMPa的压力下纯水通 量为 580Kg/m2.h、 膜对分子量为 12000的聚乙二醇的截留率均在 90%以上。 膜在 温度为 100'C的水中处理 10分钟后， 对双氧氮蒽染料的截留率有所上升， 而通量 下降 30%。 蹇 Xin et al., Preparation of UF and NF poly (phthalazine ether sulfone ketone) membranes for high temperature application, Journal of membrane science, 1999, 161 (1), 185-191, using diaza-naphthalene structures in the laboratory Polyethersulfone (PPESK) was used to prepare a flat ultrafiltration membrane. N-methylpyrrolidone was used as a solvent, and methyl ethyl ketone, ethylene glycol methyl ether or diethyl ether was used as an additive for film formation. The mass percentage concentration of PPESK in the film-forming liquid is 10 to 14%, and the mass percentage concentration of the additives is 2 to 18%. The results of studying the chemical resistance of the film material showed that the film thickness was kept constant after the film was immersed in the eight solutions shown in Table 1 for 2 weeks at normal temperature. Table 1 Experimental results of PPESK flat film immersed in 8 solutions for 2 weeks They also examined the effects of polymer content, types and contents of additives, and evaporation time on film performance. It was found that when the content of PPESK in the film-forming solution was 10% by weight, methyl ethyl ketone was used as an additive, the evaporation time was 25 seconds, and the gel bath was 60Ό water, the flat ultrafiltration membrane produced was under a pressure of 0.1 MPa. The pure water flux was 580 Kg / m 2 .h, and the membrane's rejection rate to polyethylene glycol with a molecular weight of 12,000 was above 90%. After the membrane was treated in water at a temperature of 100 ° C for 10 minutes, the retention rate of the peroxanthracene dye increased, and the flux decreased by 30%.
与平板膜相比， 中空纤维膜具有膜组件制造工艺简单， 装填面积大， 制造成 本低等优点， 利于大规模推广应用。 发明内容 Compared with flat membrane, hollow fiber membrane has the advantages of simple membrane module manufacturing process, large filling area and low manufacturing cost, which is conducive to large-scale popularization and application. Summary of the Invention
本发明的目的是提供二氮杂萘-聚醚砜、 -聚醚酮和 -聚醚砜酮类中空纤维超滤 膜及其制备方法。 本发明选用三种新型高聚物作为膜材料， 制备了耐高温、 耐溶 剂、 耐氧化、 耐酸碱腐蚀和耐氯性能好， 并且具有大的膜通量的超滤膜。 The object of the present invention is to provide diazanaphthalene-polyethersulfone, -polyetherketone and -polyethersulfone ketone hollow fiber ultrafiltration membrane and a preparation method thereof. The invention selects three novel polymers as membrane materials, and prepares an ultrafiltration membrane with high temperature resistance, solvent resistance, oxidation resistance, acid and alkali resistance, and chlorine resistance, and a large membrane flux.
本发明的二氮杂萘-聚醚砜、 -聚醚酮或-聚醚砜酮类中空纤维超滤膜含有： 聚合物 P, 其选自含二氮杂萘结构的聚醚酮（PPEK)、含二氮杂萘结构的聚醚 砜（PPES)和含二氮杂萘结构的聚醚砜酮（PPESK), 其中所述的含二氮杂萘结构 的聚醚砜 (PPES) 由式（I)表示： The diaza-naphthalene-polyethersulfone, -polyetherketone, or -polyethersulfone ketone hollow fiber ultrafiltration membrane of the present invention contains: a polymer P, which is selected from polyetherketone (PPEK) containing a diazanaphthalene structure 2, polyethersulfone (PPES) containing diaza-naphthalene structure and polyethersulfone (PPESK) containing diaza-naphthalene structure, wherein the polyethersulfone (PPES) containing diaza-naphthalene structure is represented by I) means:
其中 n=400— 600， 其玻璃化温度分别为 253-263Ό ; 含二氮杂萘结构的聚醚砜酮 (PPESK)由式 （m)表示: Where n = 400-600, and their glass transition temperatures are 253-263Ό; polyethersulfone ketone (PPESK) containing diazanaphthalene structure is represented by formula (m):
(ΙΠ) 其中 m=200—600， n= 100-500, 其玻璃化转变温度为 264-284 °C； 或任选存在的填充剂 F， 其选自纳米二氧化钛和纳米二氧化硅， (III) where m = 200-600, n = 100-500, and its glass transition temperature is 264-284 ° C; or an optional filler F, which is selected from nano titanium dioxide and nano silica,
其中： F/P的重量比为 0-1/20。 本发明还提供二氮杂萘-聚醚砜、 -聚醚酮和 -聚醚砜酮类中空纤维超滤膜的制 备方法， 其包括以下步骤： Among them: The weight ratio of F / P is 0-1 / 2. The invention also provides a method for preparing diazanaphthalene-polyethersulfone, -polyetherketone and -polyethersulfone ketone hollow fiber ultrafiltration membrane, which comprises the following steps:
( 1 )在溶料釜中配制具有下列组成的制膜液： (1) A film-forming liquid having the following composition is prepared in a melting pot:
. 聚合物 P， 其选自式（I)所示的含二氮杂萘结构的聚醚砜（PPES)、 式（Π) 所示的含二氮杂萘结构的聚醚酮（PPEK)和式 （ΠΙ)所示的含二氮杂萘结构的聚 醚砜酮 (PPESK), Polymer P, selected from polyethersulfone (PPES) containing a diazanaphthalene structure represented by formula (I), polyetherketone (PPEK) containing a diazanaphthalene structure represented by formula (Π), and Polyethersulfone ketone (PPESK) containing a diazanaphthalene structure represented by formula (ΠΙ),
溶剂 S， 其选自 Ν,Ν—二甲基乙酰胺（DMAc：)、 N—甲基吡咯烷酮（ MP)、 Ν,Ν—二甲基甲酰胺（DMF)、 氯仿（CHC13)、 二氯甲烷（CH2C12) 以及其中任意 两者的混合物， Solvent S, which is selected from N, N-dimethylacetamide (DMAc :), N-methylpyrrolidone (MP), N, N-dimethylformamide (DMF), chloroform (CHC1 3 ), dichloro Methane (CH 2 C1 2 ) and a mixture of any two of them,
添加剂 A, 其选自吐温、 聚乙二醇、 聚乙'錄吡咯烷酮、 乙醇、 异丙醇、 丙三 醇、 丙酮、 乙二醇、一縮二乙二醇， 甲基丙烯酸羟乙酯， 氯化锂， 硝酸锂和 C2〜 C5有机酸， 以及 ' Additive A, which is selected from the group consisting of Tween, polyethylene glycol, polyethylene's pyrrolidone, ethanol, isopropanol, glycerol, acetone, ethylene glycol, diethylene glycol, hydroxyethyl methacrylate, Lithium chloride, lithium nitrate and C 2 ~ C 5 organic acids, and '
任选存在的填充剂 F， 其选自纳米二氧化钛和纳米二氧化硅； Optional filler F, selected from nano titanium dioxide and nano silicon dioxide;
其中： P/(P+S)的重量比为 15~25% ，
A/P的重量比为 0.01-1/1, Among them: The weight ratio of P / (P + S) is 15 ~ 25%, A / P weight ratio is 0.01-1 / 1,
F/P的重量比为 0-1/20; F / P weight ratio is 0-1 / 2;
(2)溶解 (2) Dissolved
把所配制的制膜液在 80〜100°C的温度下搅拌 15〜24小时， 使高聚物 P和添 加剂 A充分溶解于溶剂 S中， 使填充剂 F均匀分散在制膜液中， 成为均匀的制膜 液， The prepared film-forming liquid is stirred at a temperature of 80 to 100 ° C for 15 to 24 hours, so that the polymer P and the additive A are sufficiently dissolved in the solvent S, and the filler F is uniformly dispersed in the film-forming liquid to become Uniform film-forming solution,
(3)过滤 (3) Filtration
在热状态下过滤溶解均匀的制膜液以除去不溶杂质， Filter and dissolve the uniform film-forming solution under hot conditions to remove insoluble impurities.
(4)脱气 (4) Degassing
在 25〜35°C条件下进行真空脱气， Vacuum degassing at 25 ~ 35 ° C,
(5)成型 (5) Forming
在下述工艺条件下， 依以下步骤成型： Under the following process conditions, molding according to the following steps:
纺丝釜压力： 0.1〜0.4MPa， Spinning kettle pressure: 0.1 ~ 0.4MPa,
纺丝原液的温度： 30〜60°C， Temperature of spinning dope: 30 ~ 60 ° C,
牵引速度： 10〜40m/min， Traction speed: 10 ~ 40m / min,
芯液： 超滤水， 或含有 1〜50重量％上述溶剂的水溶液， 温度为 5〜60°C， 流量 0.3〜3.0IJh， Core fluid: ultrafiltration water, or an aqueous solution containing 1 to 50% by weight of the above solvent, the temperature is 5 to 60 ° C, the flow rate is 0.3 to 3.0 IJh,
空气间隙： 0〜1500mm, 蒸发气氛空气温度为室温， Air gap: 0 ~ 1500mm, evaporation temperature is room temperature,
第一凝胶浴： 超滤水或硬度为 2〜3 mol/L的软化水， 或含有 1一 10重 量％上述溶剂的水溶液， 其中任选含有 0〜1重量％的表 面活性剂， 温度 0〜60°C， First gel bath: ultrafiltration water or demineralized water with a hardness of 2 to 3 mol / L, or an aqueous solution containing 1 to 10% by weight of the above-mentioned solvent, which optionally contains 0 to 1% by weight of a surfactant at a temperature of 0 ~ 60 ° C,
第二凝胶浴： 超滤水， 温度 30〜60°C , ' Second gel bath: ultrafiltration water, temperature 30 ~ 60 ° C, '
成型步骤依次为： The forming steps are:
(5.1 ) 开启溶料釜放料阀， 使制膜液从喷丝板环隙喷出， (5.1) Open the discharge valve of the melting pot, so that the film-forming liquid is ejected from the ring gap of the spinneret,
(5.2)打开中空纤维纺丝机的内凝胶浴（芯液）， 并通过调节阀使芯液从喷液 板中心孔流出， 形成初生态中空纤维膜， (5.2) Open the inner gel bath (core fluid) of the hollow fiber spinning machine, and make the core fluid flow out from the central hole of the liquid spray plate through the regulating valve to form a preliminary ecological hollow fiber membrane.
(5.3)把初生态纤维膜经空气间隙顺序引入第一凝胶槽和第二凝胶槽， 再引 向绕丝辊， (5.3) The primary ecological fiber membrane is sequentially introduced into the first gel tank and the second gel tank through the air gap, and then directed to the winding roller.
(5.4) 调节牵引速度、 纺丝釜压力和芯液流量， 制出具有合适壁厚的中空纤 维膜。 具体实施方式 (5.4) Adjust the traction speed, spinning kettle pressure, and core fluid flow to produce a hollow fiber membrane with a suitable wall thickness. detailed description
本发明采用含二氮杂萘结构的-聚醚酮 （PPEK)、 -聚醚砜 (PPES) 或-聚醚砜 酮 （PPESK)这三种新材料制备耐高温、 耐溶剂、 耐氧化和耐酸碱的中空纤维超
滤膜。 其中 PPEK的制备见中国专利申请 93109179.9， PPES和 PPESK的制备见 中国专利申请 93109180.2。本发明中所用的 PPEK和 PPES的平均聚合度 n为 400〜 600， 平均分子量大约为 160，000〜280,000， PPESK的平均聚合度为 m=200~600， n= 100〜500， 平均分子量大约为 180，000〜500,000。 本发明对这三种材料的化学 稳定性进行了实验，结果如表 2所示。实验条件为：用这三种材料制备厚度为 50〜 60 m的薄膜， 将膜浸泡于表 2所示的 11种水溶液中， 溶液的温度为 40Ό , 浸泡 时间为 30天。 经实验测试， 浸泡前后膜的质量、 厚度及强度均未发生变化， 证明 这三种材料具有好的耐酸碱、 耐氧化、 耐氯性。 膜在 40°C温度下的化学稳定性实验结果 In the present invention, three new materials with a diaza-naphthalene structure, namely, polyetherketone (PPEK), polyethersulfone (PPES), or polyethersulfone ketone (PPESK), are used to prepare high temperature resistance, solvent resistance, oxidation resistance and resistance. Acid-base hollow fiber super Filter. The preparation of PPEK can be found in Chinese patent application 93109179.9, and the preparation of PPES and PPESK can be found in Chinese patent application 93109180.2. The average degree of polymerization n of PPEK and PPES used in the present invention is 400 to 600, and the average molecular weight is approximately 160,000 to 280,000. The average degree of polymerization of PPESK is m = 200 to 600, n = 100 to 500, and the average molecular weight is approximately 180,000 ~ 500,000. The present invention has performed experiments on the chemical stability of these three materials, and the results are shown in Table 2. The experimental conditions were: a film with a thickness of 50 to 60 m was prepared from these three materials, and the film was immersed in 11 kinds of aqueous solutions shown in Table 2, the temperature of the solution was 40 ° C, and the soaking time was 30 days. After experimental tests, the quality, thickness, and strength of the film did not change before and after immersion, proving that these three materials have good acid and alkali resistance, oxidation resistance, and chlorine resistance. Experimental results of chemical stability of membranes at 40 ° C
浸泡液 03 HCI ¾S04 HNO; NaOH NaOH NaCIO NaCIO H202 H202 lOppm (2%) (2%) (2%) (2%) (5%) (1%) (5%) (1%) (5%)Soaking solution 0 3 HCI ¾S0 4 HNO; NaOH NaOH NaCIO NaCIO H 2 0 2 H 2 0 2 lOppm (2%) (2%) (2%) (2%) (5%) (1%) (5%) (1%) (5%)
PPESPPES
PPEK 膜的外观、 质量、 厚度、 强度均无变化 No change in appearance, quality, thickness, and strength of PPEK film
PPESK 本发明所采用的溶剂包括 N， N—二甲基乙酰胺（DMAc)、 Ν,Ν-二甲基甲酰胺 (DMF)、 N—甲基吡咯烷酮 （NMP)、 氯仿 （CHC13)、 二氯甲垸 （CH2C12)或者 其中两者的混合物， 优选使用 DMAc或 MP。 PPESK Solvents used in the present invention include N, N-dimethylacetamide (DMAc), Ν, Ν-dimethylformamide (DMF), N-methylpyrrolidone (NMP), chloroform (CHC1 3 ), two For chloroformamidine (CH 2 C1 2 ) or a mixture of the two, DMAc or MP is preferably used.
根据 PPESK、 PPES和 PPEK三种材料制膜液的可纺性及膜强度等综合因素， 本发明的中空纤维超滤膜制膜液中高聚物的百分比浓度均大于 14% , 不同于已有 文献中所用的高聚物浓度（10〜14% )。 According to the comprehensive factors such as the spinnability and membrane strength of PPESK, PPES, and PPEK film-forming solutions, the percentage concentration of polymers in the hollow-fiber ultrafiltration membrane-forming solution is greater than 14%, which is different from existing literatures. High polymer concentration (10 ~ 14%).
本发明所采用的添加剂包括吐温、 聚乙二醇、 聚乙烯吡咯垸酮、 乙醇、 异丙 醇、 丙三醇、 丙酮、 乙二醇、 一缩二乙二醇， 甲基丙烯酸羟乙酯， 氯化锂， 硝酸 锂， C2〜C5有机酸等， 优选吐温 （T-60、 Τ-40、 Τ-20)、 聚乙二醇 （分子量 400, 600， 1000, 2000)和草酸。 本发明的添加剂对改进膜通量有重要的作用。 Additives used in the present invention include Tween, polyethylene glycol, polyvinylpyrrolidone, ethanol, isopropanol, glycerol, acetone, ethylene glycol, diethylene glycol, and hydroxyethyl methacrylate , Lithium chloride, lithium nitrate, C 2 ~ C 5 organic acids, etc., preferably Tween (T-60, T-40, T-20), polyethylene glycol (molecular weight 400, 600, 1000, 2000) and oxalic acid . The additives of the present invention have an important effect on improving membrane flux.
本发明所采用的填充剂包括纳米二氧化钛和纳米二氧化硅， 优选颗粒的直径 为 10〜50nm。 由于高分子材料多孔膜在高温下会产生一定程度的收缩变形， 加入 一定量的无机纳米材料作为填充剂， 可以改善膜结构的稳定性， 减少其在高温条 件下的收縮变形。 The filler used in the present invention includes nano titanium dioxide and nano silicon dioxide, and the diameter of the particles is preferably 10 to 50 nm. Since the porous membrane of polymer materials will have a certain degree of shrinkage and deformation at high temperatures, adding a certain amount of inorganic nanomaterials as fillers can improve the stability of the membrane structure and reduce its shrinkage and deformation under high temperature conditions.
本发明采用干湿法纺丝， 浸渍凝胶相转换化法制备中空纤维超滤膜。 按照本 发明的方法制备的中空纤维超滤膜的外径为 0.5〜2ir皿， 壁厚为 0.1〜0.4mm。 In the present invention, a dry-wet spinning method and a dipping gel phase inversion method are used to prepare a hollow fiber ultrafiltration membrane. The hollow fiber ultrafiltration membrane prepared according to the method of the present invention has an outer diameter of 0.5 to 2 ir and a wall thickness of 0.1 to 0.4 mm.
本发明对制出的中空纤维膜的纯水通量及截留率进行了测定。 测定使用 25V 下的去离子水， 操作压力为 O.lMPa, 牛血清蛋白的分子量为 67000， Y球蛋白的 分子量为 150000。 在 100'C水中热处理 30min， 测定膜的水通量变化情况。 The present invention measures the pure water flux and rejection rate of the produced hollow fiber membrane. The measurement was performed using deionized water at 25 V, the operating pressure was 0.1 MPa, the molecular weight of bovine serum protein was 67,000, and the molecular weight of Y globulin was 150,000. Heat treatment in 100'C water for 30min to determine the water flux change of the membrane.
本发明制备的中空纤维超滤膜能耐高温、 耐溶剂腐蚀， 有好的抗氧化、 耐酸
碱性及耐氯性。为了考察膜结构的稳定性，在 100Ό的水中处理 30min后， 测得其 水通量结果比未经处理的膜下降仅 1〜5%。 The hollow fiber ultrafiltration membrane prepared by the present invention can withstand high temperature and solvent corrosion, and has good oxidation resistance and acid resistance. Alkali and chlorine resistance. In order to examine the stability of the membrane structure, the water flux measured after treatment in 100 Ό of water for 30 minutes was only 1 to 5% lower than that of the untreated membrane.
下面以实施例的方式进一步描述本发明， 但是这些实施例不是对本发明的范 围的限制。 The present invention is further described below by way of examples, but these examples do not limit the scope of the present invention.
本发明以草酸为添加剂制备的 PPESK中空纤维超滤膜具有优异的综合性能， 不但有好的耐高温、 耐氧化、 耐溶剂性能， 而且具有大的通量。 这种大通量的超 滤膜具有海绵状结构， 中空纤维的内表面孔属于超滤， 外表面孔属于微滤。 实施例 1 The PPESK hollow fiber ultrafiltration membrane prepared by using the oxalic acid as an additive in the present invention has excellent comprehensive performance, not only has good high temperature resistance, oxidation resistance, solvent resistance performance, but also has a large flux. This large-throughput ultrafiltration membrane has a sponge-like structure. The inner surface pores of the hollow fiber belong to ultrafiltration, and the outer surface pores belong to microfiltration. Example 1
取膜原料平均分子量为 240， 000的 PPES(P) 65g, 溶剂 DMAc (SI) 135g和 NMP (S2) 200g, 添加剂吐温 60 (A) 40g, 颗粒直径为 10〜30nm的纳米 Ti023g， 配制成 443g制膜液。 在 90Ό温度下搅拌 15小时， 制成均匀的制膜液。 经过滤、 脱气后， 按上文所述的制备方法步骤 5.1-5.4制备中空纤维膜， 其中紡丝釜压力 O.lMPa, 纺丝原液温度（釜温）为 30°C， 牵伸速度 25m/min， 芯液为 60°C的超滤 水， 空气间隙为 0， 第一凝胶浴和第二凝胶浴均为 60Ό的超滤水。 65 g of PPES (P) with an average molecular weight of 240, 000, 135 g of solvent DMAc (SI) and 200 g of NMP (S2), 40 g of additive Tween 60 (A), and 3 g of nano Ti0 2 with a particle diameter of 10-30 nm, Formulated into 443g film-forming solution. Stir at 90 ° F for 15 hours to prepare a uniform film-forming solution. After filtration and degassing, hollow fiber membranes were prepared according to steps 5.1-5.4 of the preparation method described above, wherein the spinning kettle pressure was 0.1 MPa, the spinning dope temperature (pot temperature) was 30 ° C, and the draft speed was 25 m / min, ultrafiltration water with a core fluid of 60 ° C and an air gap of 0, and the first gel bath and the second gel bath are both 60Ό ultrafiltration water.
在 25°C的水中浸泡 24小时后， 测试所得中空超滤膜的性能。 在操作压力为 O.lMPa,温度为 25°C的条件下膜的纯水通量为 650L/m2.h，膜对牛血清蛋白的截留 率为 80%， 对 γ球蛋白的截留率为 91 %。 After immersion in water at 25 ° C for 24 hours, the performance of the obtained hollow ultrafiltration membrane was tested. Under the conditions of operating pressure of 0.1 MPa and temperature of 25 ° C, the pure water flux of the membrane was 650 L / m 2 .h, and the rejection rate of the membrane to bovine serum protein was 80%, and the rejection rate to gamma globulin was 91%.
该中空超滤膜在 100'C的水中处理 30min后， 测得其水通量比未热处理时下降 5.0% 实施例 2— 10 After the hollow ultrafiltration membrane was treated in water at 100 ° C for 30 minutes, it was measured that its water flux was 5.0% lower than that when it was not heat treated. Example 2-10
以下表 3中所示的不同原料组成和制备条件分别制备实施例 2— 10的中空纤 维超滤膜， 膜的测试性能同时列于表 3。 实施例 11 ' The hollow fiber ultrafiltration membranes of Examples 2 to 10 were prepared with different raw material compositions and preparation conditions shown in Table 3 below. The test performances of the membranes are also listed in Table 3. Example 11 '
取膜材料平均分子量为 220， 000的 PPESK (P) 125g, 溶剂 DMAc (S^ 175g 和 NMP (S2) 200g， 添加剂聚乙二醇（PEG400) lOOg, 配制 600g制膜液。在 100 °C温度下搅拌 15小时， 制成均勾的制膜液。 经过滤、 脱气后， 按本发明的制备方 法步骤 5.1-5.4制备中空纤维膜， 其中纺丝釜压 0.4Mpa， 纺丝原液温度（釜温） 60 V， 牵引速度 30m/min，'芯液温度为 60°C， 水流量为 3L/h， 空气间隙 1500mm， 第一凝胶浴为硬度为 3 mol/L的软化水， 温度为 60°C， 第二凝胶浴为 60°C的超滤 水。 Take an average molecular weight of membrane material 220, 000 PPESK (P) 125g, solvent DMAc (S ^ 175g and NMP (S 2) 200g, the additive, polyethylene glycol (PEG400) lOOg, 600g film was prepared in 100 ° C Stir for 15 hours at a temperature to make a uniform film-forming solution. After filtering and degassing, hollow fiber membranes are prepared according to steps 5.1-5.4 of the preparation method of the present invention, wherein the spinning kettle pressure is 0.4 MPa, and the spinning dope temperature ( Kettle temperature) 60 V, traction speed 30m / min, 'core fluid temperature is 60 ° C, water flow is 3L / h, air gap is 1500mm, the first gel bath is demineralized water with a hardness of 3 mol / L, the temperature is 60 ° C, the second gel bath is 60 ° C ultrafiltration water.
在 25°C的水中浸泡 24小时后， 测试膜的性能。 在操作压力为 O.lMpa, 温度 25Ό的条件下， 膜的纯水通量为 250L/m2.h， 对 Y球蛋白的截留率为 99.7%。 该超
滤膜具有海绵状结构， 中空纤维的内表面孔属于超滤、 外表面孔属于微滤。 实施例 12— 18 _ After immersion in water at 25 ° C for 24 hours, the performance of the film was tested. Under the operating pressure of 0.1 Mpa and a temperature of 25 ° C, the pure water flux of the membrane was 250 L / m 2 .h, and the retention rate of Y globulin was 99.7%. The super The filter membrane has a sponge-like structure. The inner surface pores of the hollow fiber belong to ultrafiltration, and the outer surface pores belong to microfiltration. Example 12-18 _
以下表 4中所示的不同原料组成和制备条件分别制备实施例 12— 18的中空纤 维超滤滤膜， 膜的测试性能同时列于表 4。 实施例 19一 24 The hollow fiber ultrafiltration membranes of Examples 12 to 18 were prepared with different raw material compositions and preparation conditions shown in Table 4 below. The test performances of the membranes are listed in Table 4 at the same time. Examples 19 to 24
以下表 5中所示的不同原料组成和制备条件分别制备实施例 19一 26的中空纤 维超滤滤膜， 膜的测试性能同时列于表 5。
The hollow fiber ultrafiltration membranes of Examples 19 to 26 were prepared by using different raw material compositions and preparation conditions shown in Table 5 below.
表 3.实施例 2〜10的制备条件及膜性能列表 (1，2) Table 3. List of preparation conditions and membrane properties of Examples 2 to 10 (1 , 2)
1. [ ]内数量为制膜原料的质量（g); 1. The number in [] is the mass of the raw material for film making (g);
2.纳米 Ti02的颗粒直径为 10〜30纳米， 纳米 Si02的颗粒直径为 30〜50纳米 t
2. Ti0 2 nanoparticle diameter of 10~30 nm, particle diameter of the nano Si0 2 is 30 ~ 50 nanometers t
表 4. 实施例 12〜18的制备条件及膜性能列表 (1) Table 4. Preparation conditions and membrane properties of Examples 12 to 18 (1)
注： 1. [ ]内数量为制膜原料的质量 (g); Note: 1. The quantity in [] is the mass of the raw material for film making (g);
2. PPESK的平均分子量为 220,000; 2. The average molecular weight of PPESK is 220,000;
3.测试条件： 操作压力 O.lMpa, 操作温度 25Ό.
3. Test conditions: operating pressure O.lMpa, operating temperature 25Ό.
表 5.实施例 19~24的制备条件及膜性能列表 (1) Table 5. List of preparation conditions and membrane properties of Examples 19-24 (1)
1. [ ]内数量为制膜原料的质量 (g); 1. The number in [] is the mass of the raw material for film making (g);
2. PPES的平均分子量为 200,000, PPEK的平均分子量为 160,000; 2. The average molecular weight of PPES is 200,000, and the average molecular weight of PPEK is 160,000;
3.测试条件： 操作压力 O.lMpa, 操作温度 25°C.
3. Test conditions: operating pressure O.lMpa, operating temperature 25 ° C.
Claims
1、 二氮杂萘-聚醚砜、 -聚醚酮或-聚醚砜酮类中空纤维超滤膜， 含有： 聚合物 P,其选自含二氮杂萘结构的聚醚砜 PPES、含二氮杂萘结构的聚醚酮1. Diazanaphthalene-polyethersulfone, -polyetherketone or -polyethersulfoneketone hollow fiber ultrafiltration membrane, containing: polymer P, which is selected from polyethersulfone PPES containing a diazanaphthalene structure, containing Polyether ketone
PPEK和含二氮杂萘结构的聚醚砜酮 PPESK, 其中所述的含二氮杂萘结构的聚醚 砜 PPES由式 （I)表示： PPEK and a diazanaphthalene-containing polyethersulfone ketone PPESK, wherein the diazanaphthalene-containing polyethersulfone PPES is represented by formula (I):
(Π) 其中 n=400— 600， 其玻璃化温度分别为 253-263 °C ; 以及 含二氮杂萘结构的聚醚砜酮 PPESK由式 （ΙΠ)表示: (Π) where n = 400-600, and their glass transition temperatures are 253-263 ° C, respectively; and the polyethersulfone ketone PPESK containing a diazanaphthalene structure is represented by formula (ΙΠ):
(m) 其中 m=200— 600, n= 100— 500， 其玻璃化转变温度为 264-284 °C； 和任选存在的填充剂 F， 其选自纳米二氧化钛和纳米二氧化硅，
其中： F/P的重量比为 0-1/20。 (m) where m = 200-600, n = 100-500, and its glass transition temperature is 264-284 ° C; and optional filler F, which is selected from nano titanium dioxide and nano silica, Among them: The weight ratio of F / P is 0-120.
2、·如权利要求 1所述的二氮杂萘-聚醚砜、 -聚醚酮和-聚醚砜酮类中空纤维超 滤膜的制备方法， 其包括以下步骤： 2. The method for preparing a diazanaphthalene-polyethersulfone, -polyetherketone and -polyethersulfone-ketone hollow fiber ultrafiltration membrane according to claim 1, comprising the following steps:
( 1 )在溶料釜中配制具有下列组成的制膜液： (1) A film-forming liquid having the following composition is prepared in a melting pot:
聚合物 P, 其选自式（I)所示的含二氮杂萘结构的聚醚砜 PPES、 式（II)所 示的含二氮杂萘结构的聚醚酮 PPEK和式 （ΠΙ)所示的含二氮杂萘结构的聚醚砜 酮 PPESK, A polymer P, which is selected from the group consisting of a diazanaphthalene-containing polyethersulfone PPES represented by formula (I), a diazanaphthalene-containing polyetherketone PPEK represented by formula (II), and The polyethersulfone ketone PPESK containing the diazanaphthalene structure shown,
溶剂 S, 其选自 Ν,Ν—二甲基乙酰胺、 Ν—甲基吡咯烷酮、 Ν，Ν—二甲基甲酰 胺、 氯仿、 二氯甲垸以及其中任意两者的混合物， A solvent S, which is selected from the group consisting of N, N-dimethylacetamide, N-methylpyrrolidone, N, N-dimethylformamide, chloroform, dichloromethane, and a mixture of any two of them,
添加剂 Α， 其选自吐温、 聚乙二醇、 聚乙烯吡咯垸酮、 乙醇、 异丙醇、 丙三 醇、 丙酮、 乙二醇、 一缩二乙二醇， 甲基丙烯酸羟乙酯， 氯化锂， 硝酸锂和 C2〜 C5有机酸， 以及 Additive A, which is selected from the group consisting of Tween, polyethylene glycol, polyvinylpyrrolidone, ethanol, isopropanol, glycerol, acetone, ethylene glycol, diethylene glycol, hydroxyethyl methacrylate, Lithium chloride, lithium nitrate and C 2 ~ C 5 organic acids, and
任选存在的填充剂 F， 其选自纳米二氧化钛和纳米二氧化硅； Optional filler F, selected from nano titanium dioxide and nano silicon dioxide;
其中： P/(P+S)的重量比为 15-25% ， Wherein: the weight ratio of P / (P + S) is 15-25%,
A/P的重量比为 0.01-1/1 A / P weight ratio is 0.01-1 / 1
F/P的重量比为 0-1/20; F / P weight ratio is 0-1 / 2;
(2)溶解 (2) Dissolved
把所配制的制膜液在 80〜100Ό的温度下搅拌 15〜24小时，形成均匀的制膜 液， ' Stir the prepared film-forming solution at a temperature of 80 to 100 ° C for 15 to 24 hours to form a uniform film-forming solution.
(3)过滤 (3) Filtration
在热状态下过滤溶解均匀的制膜液以除去不溶杂质， Filter and dissolve the uniform film-forming solution under hot conditions to remove insoluble impurities
(4)脱气 (4) Degassing
在 25〜35°C条件下 ¾行真空脱气， ¾ line vacuum degassing at 25 ~ 35 ° C,
(5)成型 (5) Forming
在下述工艺条件下成型， 制出具有所需壁厚的中空纤维膜： Molding under the following process conditions to produce a hollow fiber membrane with the required wall thickness:
纺丝釜压力： 0.1〜0.4MPa， Spinning kettle pressure: 0.1 ~ 0.4MPa,
紡丝原液的温度： 30〜60°C， Temperature of spinning dope: 30 ~ 60 ° C,
牵引速度： 10〜40m/min， Traction speed: 10 ~ 40m / min,
芯液： 超滤水，或含有 1〜50重量％上述溶剂的水溶液，温度为 5〜60°C， Core liquid: ultrafiltration water, or an aqueous solution containing 1 to 50% by weight of the above solvent, the temperature is 5 to 60 ° C,
流量 0.3〜3.0L/h， Flow 0.3 ~ 3.0L / h,
空气间隙： 0~1500mm， 蒸发气氛空气温度为室温， Air gap: 0 ~ 1500mm, evaporation temperature is room temperature,
第一凝胶浴： 超滤水或硬度为 2~3μιηο1/ΐ;的软化水， 或含有 1一 10重量％ 上述溶剂的水溶液， 其中任选含有 0〜1重量％的表面活性 剂，' '温度 0〜60°C，
第二凝胶浴： 超滤水， 温度 30〜60°C。 First gel bath: ultrafiltration water or demineralized water with a hardness of 2 ~ 3μιηο1 / ΐ; or an aqueous solution containing 1 to 10% by weight of the above solvent, which optionally contains 0 to 1% by weight of a surfactant, '' Temperature 0 ~ 60 ° C, Second gel bath: ultrafiltration water, temperature 30 ~ 60 ° C.
3、如权利要求 2所述的制备方法，其中所述的溶剂为 Ν,Ν—二甲基乙酰胺或 Ν—甲基吡咯烧酮。 3. The preparation method according to claim 2, wherein the solvent is N, N-dimethylacetamide or N-methylpyrrolidone.
4、 如权利要求 2所述的制备方法， 其中所述的添加剂选自吐温、 聚乙二醇、 异丙醇、 氯化锂、 硝酸锂、 冰醋酸和草酸中的至少之一。 4. The method according to claim 2, wherein the additive is at least one selected from the group consisting of Tween, polyethylene glycol, isopropyl alcohol, lithium chloride, lithium nitrate, glacial acetic acid, and oxalic acid.
5、 如权利要求 4所述的制备方法， 其中所述的添加剂选自吐温 Τ-60、 吐温 Τ-40、 吐温 Τ-20、 分子量分别为 400、 600、 1000和 2000的聚乙二醇以及草酸中 的至少之一。
5. The preparation method according to claim 4, wherein the additive is selected from the group consisting of Tween T-60, Tween T-40, Tween T-20, and polyethylene with molecular weights of 400, 600, 1000, and 2000, respectively. At least one of glycol and oxalic acid.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN03124222.7 | 2003-05-01 | ||
| CN 03124222 CN1251793C (en) | 2003-05-01 | 2003-05-01 | Hollow fibre ultrafiltration membrane of phenodiazine polyether-sulphone-ketone material and preparing process thereof |
| CNB2003101155444A CN100506365C (en) | 2003-11-28 | 2003-11-28 | Dinitrogen phenodiazine polyethersulfone ketone hollow fiber ultra filtration membrane and fabrication method thereof |
| CN200310115544.4 | 2003-11-28 |
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| WO2004096418A1 true WO2004096418A1 (en) | 2004-11-11 |
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| PCT/CN2004/000295 WO2004096418A1 (en) | 2003-05-01 | 2004-03-31 | Hollow fiber ultrafilter membrane with poly(phthalazinone ether fulfone), poly(phthalazinone ether ketone) or poly(phthalazinone ether sulfone ketone) and preparation thereof |
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| WO2012106583A3 (en) * | 2011-02-04 | 2013-03-21 | Fresenius Medical Care Holdings, Inc. | Performance enhancing additives for fiber formation and polysulfone fibers |
| CN111701459A (en) * | 2020-07-01 | 2020-09-25 | 浙江工业大学 | Nitrogen-heterocycle-containing polyaryletherketone/sulfone ultra/micro-filtration membrane and structure regulation method thereof |
| CN112221360A (en) * | 2020-09-15 | 2021-01-15 | 大连理工大学 | Copolymerized ether sulfone hemodialysis membrane containing phthalazinone structure and preparation method thereof |
| CN112221361A (en) * | 2020-09-15 | 2021-01-15 | 大连理工大学 | Polyether sulfone/copolyether sulfone blended hollow fiber hemodialysis membrane with phthalazinone structure and preparation method thereof |
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| WO2009077553A1 (en) | 2007-12-18 | 2009-06-25 | Solvay Advanced Polymers, L.L.C. | Polyphenyl sulfone ketone copolymers |
| USRE48703E1 (en) | 2011-02-04 | 2021-08-24 | Fresenius Medical Care Holdings, Inc. | Performance enhancing additives for fiber formation and polysulfone fibers |
| US9617421B2 (en) | 2011-02-04 | 2017-04-11 | Fresenius Medical Care Holdings, Inc. | Performance enhancing additives for fiber formation and polysulfone fibers |
| WO2012106583A3 (en) * | 2011-02-04 | 2013-03-21 | Fresenius Medical Care Holdings, Inc. | Performance enhancing additives for fiber formation and polysulfone fibers |
| CN112295415A (en) * | 2019-08-02 | 2021-02-02 | 北京新源国能科技集团股份有限公司 | Preparation method and device of hollow fiber nanofiltration membrane |
| CN113530464A (en) * | 2020-04-17 | 2021-10-22 | 中国石油化工股份有限公司 | Oil well pipe and method for manufacturing same |
| CN111701459A (en) * | 2020-07-01 | 2020-09-25 | 浙江工业大学 | Nitrogen-heterocycle-containing polyaryletherketone/sulfone ultra/micro-filtration membrane and structure regulation method thereof |
| CN112221360A (en) * | 2020-09-15 | 2021-01-15 | 大连理工大学 | Copolymerized ether sulfone hemodialysis membrane containing phthalazinone structure and preparation method thereof |
| CN112221361A (en) * | 2020-09-15 | 2021-01-15 | 大连理工大学 | Polyether sulfone/copolyether sulfone blended hollow fiber hemodialysis membrane with phthalazinone structure and preparation method thereof |
| CN113024925A (en) * | 2021-03-15 | 2021-06-25 | 四川汇利实业有限公司 | Modified PE film capable of improving self-repairing performance and preparation method thereof |
| CN115369517A (en) * | 2022-08-30 | 2022-11-22 | 烟台民士达特种纸业股份有限公司 | Preparation method and application of polyether-ether-ketone nanofiber membrane |
| CN115369517B (en) * | 2022-08-30 | 2023-09-01 | 烟台民士达特种纸业股份有限公司 | Preparation method and application of polyether-ether-ketone nanofiber membrane |
| CN117771983A (en) * | 2023-04-04 | 2024-03-29 | 赛普(杭州)过滤科技有限公司 | Polyether sulfone ultrafiltration membrane, preparation method and application thereof, and ultrafiltration equipment |
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