CN1763278A - Polyether sulfone fiber and preparation method and application thereof - Google Patents
Polyether sulfone fiber and preparation method and application thereof Download PDFInfo
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- CN1763278A CN1763278A CN 200510115182 CN200510115182A CN1763278A CN 1763278 A CN1763278 A CN 1763278A CN 200510115182 CN200510115182 CN 200510115182 CN 200510115182 A CN200510115182 A CN 200510115182A CN 1763278 A CN1763278 A CN 1763278A
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- 239000004695 Polyether sulfone Substances 0.000 title claims abstract description 77
- 229920006393 polyether sulfone Polymers 0.000 title claims abstract description 77
- 239000000835 fiber Substances 0.000 title claims abstract description 56
- 238000002360 preparation method Methods 0.000 title claims description 12
- 238000009987 spinning Methods 0.000 claims abstract description 31
- 229920005989 resin Polymers 0.000 claims abstract description 20
- 239000011347 resin Substances 0.000 claims abstract description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 5
- 239000001301 oxygen Substances 0.000 claims abstract description 5
- 239000004744 fabric Substances 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 6
- 238000002844 melting Methods 0.000 claims description 6
- 230000008018 melting Effects 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 5
- 238000002074 melt spinning Methods 0.000 claims description 5
- 229920000742 Cotton Polymers 0.000 claims description 3
- 210000000085 cashmere Anatomy 0.000 claims description 3
- 210000004209 hair Anatomy 0.000 claims description 3
- 239000000463 material Substances 0.000 abstract description 12
- 239000000126 substance Substances 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 10
- 238000001816 cooling Methods 0.000 abstract description 7
- 239000004753 textile Substances 0.000 abstract description 5
- 150000001875 compounds Chemical class 0.000 abstract description 2
- 238000012545 processing Methods 0.000 description 7
- 239000003063 flame retardant Substances 0.000 description 5
- 229920006351 engineering plastic Polymers 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000001125 extrusion Methods 0.000 description 4
- 230000004927 fusion Effects 0.000 description 4
- 238000007493 shaping process Methods 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000004804 winding Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000155 melt Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 229920005992 thermoplastic resin Polymers 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000009965 tatting Methods 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- 210000002268 wool Anatomy 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
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- 239000002657 fibrous material Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000010128 melt processing Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 238000007500 overflow downdraw method Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000011176 pooling Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000035882 stress Effects 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000007666 vacuum forming Methods 0.000 description 1
Abstract
The invention discloses a polyethersulfone fiber, making method and appliance in the resin spinning domain, which is characterized by the following: the fineness of signal fiber is between 0.3 and 30 dt, wherein the limited oxygen index equals to and more than 30 when the fineness is between 1.5 and 10 dt; adapting twin-screw extruder to heat and melt the polyethersulfone resin; forming the fiber by cooling and solidifying at the high temperature-resistant spinning component pattern of fondant rill. The invention comprises the following advantages: heat resistance, flame-proof, chemical resistance, good physical mechanical property and so on, which can be used in the textile of flame-proof and or heat resistance or chemical resistance and physical mechanical property need as reinforced material in the compound material.
Description
Technical field
The present invention relates to a kind of fibrous material, say further, relate to a kind of polyether sulfone fiber and its production and application.
Background technology
(polyether sulfone is amorphism, amber, transparent homopolymers PES) to polyethersulfone resin, has comprehensive excellent properties.The construction unit of polyether sulfone is:
The PES resin is a kind of heat resistance speciality polymer material with excellent flame retardancy.Its heat resistance is outstanding, and heat distortion temperature is 200～220 ℃, can use at 180～200 ℃ long-term.Creep-resistant property is good under the high temperature, and under 150 ℃, the stress effect of 19.99MPa, its strain has only 2.55%, and its creep resistance is the most excellent a kind of in the thermoplastic resin in the temperature range below 180 ℃.In temperature environment jumpy, still can keep outstanding advantages such as stable performance.Goods are transparent, dimensionally stable, hot water or steam that can be anti-150～160 ℃, its modulus 100～200 ℃ almost constant, especially all better more than 100 ℃ than any thermoplastic resin.Ageing-resistant performance is also excellent, can reach 20 years 180 ℃ of service lifes.PES resin limited oxygen index is 38, has self-extinguishment, and not adding any fire retardant promptly has excellent flame.Its chemical resistance is good, except that can anti-dilute sulfuric acid, the rare nitric acid, dense, watery hydrochloric acid, also can anti-50%NaOH, 50%KOH, inorganic acid alkali such as liquefied ammonia and ammoniacal liquor, the ability of anti-organic reagent also is better than the common engineering plastics, as can anti-various alkane, petroleum product, alcohols, benzene, acetate, chloroform and carbon tetrachloride etc.Anti-steam and superheated water (150～160 ℃) performance is also fabulous, can be through repeatedly moise-heat sterilization.But chemical nickel plating and copper facing.The x radiation x of anti-r performance might as well.But the UV resistant performance is poor.Aspect sanitary standard, approved by U.S. FDA, also meet the requirement of No. the 434th, Japanese health ministry and No. 178 bulletins.Mechanical property and electrical property are good, its typical physical and chemical performance is: relative density 1.37, TENSILE STRENGTH 84MPa, bending strength 12.4MPa, cantilever beam impact strength (breach) 85.3J/m, Rockwell hardness M88, water absorption rate (24h) 0.43%, 203 ℃ of heat distortion temperatures (1.82MPa), relative dielectric constant 3.5, specific insulation 10
17～10
18Ω cm
3
The special engineering plastics polyether sulfone all is very superior at aspects such as heat resistance, chemical proofing and mechanical performances, and it is thermoplastic resin, and processing and forming is good, so the demand in the field that high-performance, high reliability request are arranged is in continuous growth.The main application fields of PES has electrical equipment, electronics, mechanical field, automotive field, hot water field, medical apparatus, food processing machinery field, film separation field.
The goods of PES resin only limit to special type (heat resistant type) engineering plastics, coating and filter membrane at present.Its engineering plastics can with inject, extrude, method processing such as mold pressing, vacuum forming, the processing of coating and filter membrane then needs wiring solution-forming.The hollow PES fiber that the kind of like fibrous has only ultrafiltration still at the experimental stage to use, it is the diameter (about 1mm) made by the solution spinning wet moulding filtering material much larger than general fibre (diameter is 10～30 μ m), and its processing technology and performance requirement and general fibre are also incomplete same.Abroad the report about the polyether sulfone melt-spun has only one piece [1], has wherein studied the incompatible additive that adds in PES less than 1%, and PES just can stablize spinning, and the gained fibre strength is 2.1CN/dtex.Domestic research report about the polyether sulfone melt spinning is also few, has only Tianjin to spin institute and made experimental study on fusion index instrument.(" polyether sulfone fiber development ", Yu Jianming etc., Tianjin Textile Industry College institute newspaper, 1996,15 2.: 14～17)
The difficulty of fusion method spinning polyether sulfone fiber mainly is at present:
1, polyethersulfone resin processing temperature height.And the single screw extrusion machine that the spinning of using is at present used and the serviceability temperature of supporting filament spinning component are limited in below 350 ℃, and the processing temperature of PES is 330～370 ℃, and spinning temperature is then higher, need at 340～380 ℃.
2, melt viscosity is big.Behind the PES heating and melting, viscosity is bigger, and the melt fracture tendency is arranged, and spinnability is poor.And by improve spinning temperature reduce melt viscosity method since the existence of thermal decomposition be difficult to realize.
3. difficult feed in commonly used fusion apparatus one single screw extrusion machine of spinning technique.PES is unformed macromolecular material, and no fusing point takes place softening in a wider temperature range.Therefore reaching the easy loops resistance material that takes place under the condition of abundant fusion.
Summary of the invention
At above problems of the prior art, the present invention is intended to obtain a kind of polyether sulfone fiber that has good heat resistance, chemical-resistant resistance and mechanical performance when having the good flame-retardance energy.
Therefore, the purpose of this invention is to provide a kind of high-performance polyethersulfone fiber.Plurality of advantages such as that this fiber has is heat-resisting, fire-retardant, chemical-resistant resistance, physical and mechanical properties are good.
Another object of the present invention provides the equipment that is different from existing melt spinning of described polyether sulfone fiber and the preparation method of technology.
A further object of the present invention provides the application in preparation textiles and field of compound material of described polyether sulfone fiber.
A kind of polyether sulfone fiber of the present invention, its filamentary fineness is 0.3～30dt, is preferably 1.5～10dt.Fibre fineness is a fiber number herein, and standard unit is dt (dtex), is the gram number of this fiber of ten thousand metres.
Above-described polyether sulfone fiber, it, is preferably more than and equals 36 more than or equal to 30 by the limited oxygen index (LOI) of pure polyether sulfone fabric of preparation.
Traditional resin fibre melt spinning method is the resin single screw extrusion machine heating and melting that moisture content is reached spinning requirement, flow out through the form of filament spinning component (comprising filtration, metering, distributor and spinnerets) with the melt thread, through cooling curing, form fiber again.
In the present invention, in order to make the PES resin can be spun into fiber smoothly, need moisture content is reached the PES resin double screw extruder heating and melting of common spinning technique requirement, flow out through the form of resistant to elevated temperatures filament spinning component again with the melt thread, through cooling curing, form fiber.
The preparation method of polyether sulfone fiber of the present invention specifically may further comprise the steps:
1. with the polyethersulfone resin drying;
2. with above polyethersulfone resin with double screw extruder 330～390 ℃, be preferably heating and melting under 350～370 ℃ the temperature, be at least 400 ℃ filament spinning component melt spinning again through temperature tolerance, spinning temperature is 340～400 ℃, is preferably 350～370 ℃.
With above-mentioned spun silk according to a conventional method behind the cooling curing, through common up-coiler winding shaping; Balance was carried out drawing-off with the parallel drafting machine and is made final polyether sulfone fiber of the present invention after a period of time.
The polyether sulfone fiber of the present invention's preparation is pure polyethersulfone resin preparation, promptly contains the 100%wt polyethersulfone resin.
The preparation method of above-mentioned polyether sulfone fiber selects for use double screw extruder to be because melt extrude and can provide bigger melt pressure to resin with double screw extruder, produce bigger shear rate, thereby reduce the PES melt viscosity to a certain extent, improve its spinnability.In addition, the dual-screw-stem machine extruder is different from single screw extrusion machine, and it has automatic cleaning action, is positive feed, the loops resistance material can not take place, thereby has solved the problem of this unformed macromolecular material of PES difficult feed in fusion apparatus.Used in the present invention double screw extruder can be selected various double screw extruders used in the prior art for use.
The preparation method of above-mentioned polyether sulfone fiber, the temperature that melt extrudes with spinning is to decide according to the melt processing temperature scope of polyethersulfone resin.Wherein the structure of filament spinning component is general modular construction, generally comprises measuring pump, screen pack, spinnerets etc.The filament spinning component material of selecting for use the heatproof temperature to be at least 400 ℃ is made in the present invention.Adoptable material comprises heatproof metal material, heatproof nonmetallic materials etc., and scope is very extensive.Consider that the factors such as complexity that cost and material obtain generally can be made by stainless steel (1Gr18Ni9Ti), also can make by high-strength steel (40Gr).
The polyether sulfone fiber of the invention described above can with the doubling of pooling capital of a kind of yarn in cotton, hair, silk, fiber crops, the cashmere, make the yarn goods.Can have anti-flammability, improve heat resistance and intensity, improve DIMENSIONAL STABILITY.
The polyether sulfone fiber of the invention described above can interweave and make fabric with other natural fabric or synthetic fiber or above-mentioned polyether sulfone yarn, can have anti-flammability, improves heat resistance and intensity, improves DIMENSIONAL STABILITY.
Plurality of advantages such as that polyether sulfone fiber of the present invention has is heat-resisting, fire-retardant, chemical-resistant resistance, physical and mechanical properties are good, can be used for having the textiles (as the carpet of fire-entry suit, public place, decoration etc.) of fire-retardant requirement, also can be used for the textiles (as labour protection clothes, industrial cloth etc.) that on chemical proofing and physical and mechanical properties, has higher requirements, also can in the composite that heat-resisting and/or fire-retardant requirement is arranged or on chemical proofing and physical and mechanical properties, have higher requirements, make reinforcing material.
The preparation method of polyether sulfone fiber of the present invention has solved the problem that polyethersulfone resin in the prior art is difficult to prepare fiber, successfully prepare the polyether sulfone fiber of function admirable, and technology is simple, and easy operating is fit to promote.
The specific embodiment
Further describe the present invention below in conjunction with embodiment.Scope of the present invention is not subjected to the restriction of these embodiment, and scope of the present invention proposes in claims.
Embodiment 1
The polyether sulfone of producing with German BASF (BASF) company (E1010) is raw material (moisture content＜100ppm) after the vacuum desiccator drying, adopt parallel dual-screw extruding machine group (the SHJ-18 type that Jie Ente company in Nanjing produces) to melt extrude, melt extrude temperature at 330-360 ℃ (one section 330 ℃, two sections 340 ℃, three sections 340 ℃, four sections 340 ℃, five sections 360 ℃); Afterwards through filament spinning component 360 ℃ of spinning, cooling curing after up-coiler with 500 meters/minute speed winding shaping; Carry out drawing-off with the parallel drafting machine then, drafting multiple is 2.0.Described filament spinning component comprises that measuring pump, screen pack, spinnerets etc. are made by stainless steel (1Gr18Ni9Ti).
The filament number that makes polyether sulfone fiber through above method is 5dtex, and intensity is 2.7cN/dtex, and extension at break is 11%.Record by standard GB 9997.
Embodiment 2
The polyether sulfone of producing with German BASF (BASF) company (E1010) is raw material (moisture content＜100ppm) after the vacuum desiccator drying, adopt parallel dual-screw extruding machine group (the SHJ-18 type that Jie Ente company in Nanjing produces) to melt extrude, melt extrude temperature at 330-350 ℃ (one section 330 ℃, two sections 340 ℃, three sections 340 ℃, four sections 340 ℃, five sections 350 ℃); Afterwards through filament spinning component 350 ℃ of spinning, cooling curing after up-coiler with 300 meters/minute speed winding shaping; Carry out drawing-off with the parallel drafting machine then, drafting multiple is 1.5.Described filament spinning component comprises that measuring pump, screen pack, spinnerets etc. are made by stainless steel (1Gr18Ni9Ti).
Make polyether sulfone fiber through the same standard test through above method, filament number is 20dtex, and intensity is 2.1cN/dtex, and extension at break is 20%.
Embodiment 3
The polyether sulfone of producing with German BASF (BASF) company (E2010) is raw material (moisture content＜50ppm) after the vacuum desiccator drying, adopt parallel dual-screw extruding machine group (the SHJ-18 type that Jie Ente company in Nanjing produces) to melt extrude, melt extrude temperature at 330-370 ℃ (one section 330 ℃, two sections 340 ℃, three sections 340 ℃, four sections 350 ℃, five sections 370 ℃); Afterwards through filament spinning component 370 ℃ of spinning, cooling curing after up-coiler with 600 meters/minute speed winding shaping; Carry out drawing-off with the parallel drafting machine then, drafting multiple is 2.4.Described filament spinning component comprises that measuring pump, screen pack, spinnerets etc. are made by stainless steel (1Gr18Ni9Ti).
The filament number that makes polyether sulfone fiber through above method is 1.Sdtex, and intensity is 2.9cN/dtex, and extension at break is 10%.
Embodiment 4
To be twisted into fineness be that 40Ne/1, the twist are the single thread of 377 sth. made by twisting/m through adding with embodiment 1 gained polyether sulfone fiber, on the full-automatic tatting proof press of SL7900 (Taiwan Ben Meng), be made into plain cloth (one on the other), through close 260/10m, 230/10m of filling density, fabric width 50cm.The LOI that records this fabric according to GB GB/T5454-1997 is 37.
Embodiment 5
Embodiment 3 gained polyether sulfone fibers and pure wool yarn are spun into cladded yarn on ring spinner, polyether sulfone fiber is coated on the pure wool yarn, the content of polyether sulfone fiber in cladded yarn is 60%, spins to such an extent that the cladded yarn twist is 880 sth. made by twisting/m, and the resultant yarn fiber number is 16.5tex.On the full-automatic tatting proof press of SL7900 (Taiwan Ben Meng), be made into plain cloth (one on the other), through close 160/10m, 140/10m of filling density, fabric width 50cm, fabrication processes is smooth.
Claims (8)
1. polyether sulfone fiber, its filamentary fineness is 0.3～30dt.
2. polyether sulfone fiber according to claim 1, its filamentary fineness is 1.5～10dt.
3. polyether sulfone fiber according to claim 1, the polyether sulfone that contains prepared therefrom is that the limited oxygen index of 100% fabric is more than or equal to 30.
4. polyether sulfone fiber according to claim 3, the limited oxygen index of described fabric is more than or equal to 36.
5. according to the preparation method of the described polyether sulfone fiber of one of claim 1～4, may further comprise the steps:
1. with the polyethersulfone resin drying;
2. with above polyethersulfone resin double screw extruder heating and melting under 330～390 ℃ temperature, reach 400 ℃ filament spinning component melt spinning more at least through the heatproof temperature, spinning temperature is 340～400 ℃.
6. the preparation method of polyether sulfone fiber according to claim 5, wherein the heating and melting temperature of double screw extruder is 350 ℃～370 ℃; Spinning temperature is 350～370 ℃.
7. polyether sulfone yarn is to adopt one of claim 1～4 described polyether sulfone fiber and one or more yarns in cotton, hair, silk, fiber crops, the cashmere to pool capital doubling and get.
8. polyether sulfone fabric is to adopt one of claim 1～4 described polyether sulfone fiber or the described polyether sulfone yarn of claim 7 and one or more yarns in cotton, hair, silk, fiber crops, the cashmere to interweave and get.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101151828A CN1313658C (en) | 2005-11-15 | 2005-11-15 | Polyether sulfone fiber and preparation method and application thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005101151828A CN1313658C (en) | 2005-11-15 | 2005-11-15 | Polyether sulfone fiber and preparation method and application thereof |
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| Publication Number | Publication Date |
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| CN1763278A true CN1763278A (en) | 2006-04-26 |
| CN1313658C CN1313658C (en) | 2007-05-02 |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103088446A (en) * | 2011-11-01 | 2013-05-08 | 北京中纺优丝特种纤维科技有限公司 | Preparation method of polyether sulfone fiber |
| CN103088439A (en) * | 2011-11-01 | 2013-05-08 | 北京中纺优丝特种纤维科技有限公司 | Melt spinning method for polyether sulfone fibers by using single-screw extruder |
| CN103361748A (en) * | 2013-07-25 | 2013-10-23 | 绍兴文理学院 | Method for producing high-temperature-resistant PES (polyether sulfone) fibers by melting method |
| US8637583B2 (en) | 2008-10-17 | 2014-01-28 | Solvay Advanced Polymers, L.L.C. | Fiber or foil from polymers with high Tg and process for their manufacture |
| CN103572500A (en) * | 2013-11-13 | 2014-02-12 | 泰安鲁普耐特塑料有限公司 | Polyether sulfone fiber compound rope and preparation method thereof |
| CN105926110A (en) * | 2016-06-21 | 2016-09-07 | 澳帕曼织带（昆山）有限公司 | Wiring harness protecting woven tape |
| CN106218151A (en) * | 2016-08-31 | 2016-12-14 | 宁波市阳光汽车配件有限公司 | A kind of automobile-used PP PES knitted composite fabric and preparation method |
| CN108004617A (en) * | 2017-12-15 | 2018-05-08 | 常州创赢新材料科技有限公司 | A kind of polyether-ether-ketone/polyether sulfone composite fibre and preparation method thereof |
| CN111495037A (en) * | 2020-04-29 | 2020-08-07 | 廖国庆 | Polyether sulfone fiber non-woven fabric composite filter material and preparation method thereof |
| CN113425146A (en) * | 2021-06-18 | 2021-09-24 | 金华洁灵家居用品有限公司 | Production process of chenille looped pile floor mat and chenille looped pile floor mat |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1631501A (en) * | 2004-11-11 | 2005-06-29 | 东华大学 | Hollow cellulous dialyzing and ultra filtrating membrane of cross blend polyethersulfone, its manufacturing method and usage |
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2005
- 2005-11-15 CN CNB2005101151828A patent/CN1313658C/en not_active Expired - Fee Related
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8637583B2 (en) | 2008-10-17 | 2014-01-28 | Solvay Advanced Polymers, L.L.C. | Fiber or foil from polymers with high Tg and process for their manufacture |
| CN103088446B (en) * | 2011-11-01 | 2015-10-28 | 北京中纺优丝特种纤维科技有限公司 | Preparation method of polyether sulfone fiber |
| CN103088439A (en) * | 2011-11-01 | 2013-05-08 | 北京中纺优丝特种纤维科技有限公司 | Melt spinning method for polyether sulfone fibers by using single-screw extruder |
| CN103088446A (en) * | 2011-11-01 | 2013-05-08 | 北京中纺优丝特种纤维科技有限公司 | Preparation method of polyether sulfone fiber |
| CN103088439B (en) * | 2011-11-01 | 2016-02-24 | 北京中纺优丝特种纤维科技有限公司 | Melt spinning method for polyether sulfone fibers by using single-screw extruder |
| CN103361748A (en) * | 2013-07-25 | 2013-10-23 | 绍兴文理学院 | Method for producing high-temperature-resistant PES (polyether sulfone) fibers by melting method |
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