CN102517679A - Porous microfine denier polyamide 6 pre-oriented yarn, its preparation method and device - Google Patents
Porous microfine denier polyamide 6 pre-oriented yarn, its preparation method and device Download PDFInfo
- Publication number
- CN102517679A CN102517679A CN2011104326393A CN201110432639A CN102517679A CN 102517679 A CN102517679 A CN 102517679A CN 2011104326393 A CN2011104326393 A CN 2011104326393A CN 201110432639 A CN201110432639 A CN 201110432639A CN 102517679 A CN102517679 A CN 102517679A
- Authority
- CN
- China
- Prior art keywords
- oriented yarn
- porous
- melt
- additive
- denier polyamide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229920002292 Nylon 6 Polymers 0.000 title abstract description 7
- 238000002360 preparation method Methods 0.000 title abstract description 4
- 238000000034 method Methods 0.000 claims abstract description 29
- 239000000654 additive Substances 0.000 claims abstract description 21
- 230000000996 additive effect Effects 0.000 claims abstract description 21
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 claims abstract description 11
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000004804 winding Methods 0.000 claims abstract description 11
- 239000000155 melt Substances 0.000 claims abstract description 7
- 229920005604 random copolymer Polymers 0.000 claims abstract description 6
- 238000001125 extrusion Methods 0.000 claims abstract description 4
- 239000000835 fiber Substances 0.000 claims description 38
- 239000004952 Polyamide Substances 0.000 claims description 33
- 229920002647 polyamide Polymers 0.000 claims description 33
- 238000009987 spinning Methods 0.000 claims description 26
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 25
- 238000001816 cooling Methods 0.000 claims description 19
- 239000003921 oil Substances 0.000 claims description 15
- 238000007664 blowing Methods 0.000 claims description 12
- 238000002425 crystallisation Methods 0.000 claims description 12
- 230000008025 crystallization Effects 0.000 claims description 12
- 238000001035 drying Methods 0.000 claims description 9
- 238000000465 moulding Methods 0.000 claims description 6
- 150000001336 alkenes Chemical class 0.000 claims description 5
- -1 benzene alkene Chemical class 0.000 claims description 5
- 229920006052 Chinlon® Polymers 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000012545 processing Methods 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims description 2
- 208000011580 syndromic disease Diseases 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 11
- 238000005516 engineering process Methods 0.000 abstract description 10
- 238000002074 melt spinning Methods 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 229920000642 polymer Polymers 0.000 abstract description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 abstract 2
- 238000004220 aggregation Methods 0.000 abstract 1
- 230000002776 aggregation Effects 0.000 abstract 1
- 229920001410 Microfiber Polymers 0.000 description 4
- 239000003658 microfiber Substances 0.000 description 4
- 238000013461 design Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002344 fibroplastic effect Effects 0.000 description 2
- 238000007306 functionalization reaction Methods 0.000 description 2
- 238000005098 hot rolling Methods 0.000 description 2
- 230000005764 inhibitory process Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000009877 rendering Methods 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 230000001131 transforming effect Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 238000010409 ironing Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000004243 sweat Anatomy 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
Abstract
The invention, relating to a melt spinning technique of a high-molecular polymer, provides a porous microfine denier polyamide 6 pre-oriented yarn, its preparation method and device. Random copolymer additive of methacrylate, maleic anhydride and styrene are added in the screw melt extrusion step, and the obtained pre-oriented yarn has the breaking tenacity of 3.20-3.70 cN/dex and the breaking elongation of 60-100 %. According to the invention, a routine FDY device and related production technology conditions are improved, the aggregation structure adjustment, high order orientation, and crystalline supramolecular structure in the stretch forming process of a spinneret are effectively controlled, the melt mixing uniformity and pressure stability are further increased, the winding tensile stress and unevenness of the yarn are effectively adjusted and controlled, and the after-stretching performance of the porous microfine denier polyamide 6 pre-oriented yarn is raised. According to the product provided by the invention, the maximum benefits of the enterprise can be achieved.
Description
Technical field
The present invention relates to a kind of melt spinning technology of high molecular polymer, particularly a kind of technology and equipment thereof for preparing the fine denier polyamide fiber 6 pre-oriented yarn of porous.
Background technology
Polyamide fibre 6 pre-oriented yarns of conventional variety can be processed to fullly drawn yarn (FDY), stretch textured yarn and air-textured yarn; Has a series of premium properties; Be widely used in the people's life and socioeconomic various aspects; Its main application can be divided into three big fields, i.e. clothes usefulness, industry usefulness and decoration carpet usefulness.Clothes occupy stable market with mainly being as dress material at aspects such as sweat shirt, swimsuit, gym wear, hosieries, and growing; Industry is with relating to fields such as industrial or agricultural, transportation, fishery; Aspect carpet, be mainly used in fields such as household, hotel, upholstery.
At present; Main both at home and abroad employing technology for high speed spinning approach prepares polyamide fibre 6 pre-oriented yarn conventional varieties; Exist some shortcomings;, antistatic behaviour thick like filament number, dyeability and moisture absorbability and moisture retentivity, ventilative dry and comfortable property are relatively poor, and pleasant softness is also relatively poor etc., has had a strong impact on its snugness of fit.Therefore, but how to utilize existing FDY device fabrication stable performance and the fine denier polyamide fiber 6 POY of the porous flexibility operation is significant for the development chemical fiber factory.
Summary of the invention
The objective of the invention is in order to solve the deficiency that prior art exists; Through transforming FDY device fabrication and adjustment production technology; Provide a kind of and have the superelevation extension property, be prone to dye level dyeing, evenly dye-uptake and high-color rendering, the fine denier polyamide fiber 6 pre-oriented yarn of functionalization porous that pliability is good, and technology and equipment.
In order to achieve the above object, the technical scheme of the present invention's employing is: provide a kind of porous fine denier polyamide fiber 6 pre-oriented yarn, specification is 75dtex/144f～110dtex/144f; It comprises that mass fraction is 0.5～5.0% additive; Described additive is methacrylate, maleic anhydride and the benzene nanometer randomcopolymer of alkene, and by weight percentage, the content of methacrylate is 75～85%; The content of maleic anhydride is 10～12%, and all the other are benzene alkene; The fracture strength of pre-oriented yarn is 3.45 ± 0.25 cN/dex, and elongation at break is 80 ± 20 %.
A kind of equipment for preparing the fine denier polyamide fiber 6 pre-oriented yarn of porous of the present invention; Based on the FDY equipment of producing conventional variety; Comprise preparatory crystallization, drying, screw rod melt extruded device; Spinning manifold, measuring pump, filament spinning component, spinnerets device for spinning, cooling curing device and coiling and forming device; The additive injector is installed on the charging aperture of said screw rod melt extruded device; Described cooling curing device is Xu Lenghe ring blowing cooling; The Xu Leng heater is installed below spinnerets, and the heating region height is 100～120mm; The below installing ring cold wind blower of Xu Leng heater; The boundling oil frame that oils is installed in the below of ring cold wind blower, and the distance of leaving spinnerets is 800 ± 50 mm places; Coiling and forming device comprises first, second godet roller, preparatory Network device and up-coiler, and described preparatory Network device places the centre of first godet roller and second godet roller.
A kind of method for preparing the fine denier polyamide fiber 6 pre-oriented yarn of porous of the present invention comprises that chip drying, melt extruded, melt are extruded, cooling curing, oil nozzle oils and the winding shaping operation, and process conditions are following:
1, in chinlon 6 section, adding mass fraction is 0.5～5.0% additive; Described additive is methacrylate, maleic anhydride and the benzene nanometer randomcopolymer of alkene; By weight percentage; The content of methacrylate is 75～85%, and the content of maleic anhydride is 10～12%, and all the other are benzene alkene;
2, section is adopted 5 grades of screw rod melt extrusion processes with after additive fully mixes in screw rod, and the temperature of 5 grades of screw rods is respectively 248 ± 2 ℃, 258 ± 2 ℃, 260 ± 2 ℃, 259 ± 2 ℃ and 259 ± 2 ℃;
3, melt adopts Xu Lenghe ring blowing process for cooling solidify out into strand after spinnerets is extruded as the melt thread; The heating-up temperature of Xu's device for cooling is 230 ± 2 ℃; The process conditions of ring blowing are: pressure 550Pa, 21 ± 2 ℃ of wind-warm syndrome, humidity 90 ± 5%, wind speed 0.40～0.50 m/s;
4, the tow input speed after nozzle oils boundling is first godet roller of 3945～4455 m/min; Through pressure is after the preparatory Network device of 0.7 ± 0.05 bar carries out preparatory network; Admission velocity is second godet roller of 4050～4565 m/min again, and godet roller is cold roller; Winding speed with 4000～4500 m/mi carries out coiling and molding, and processing specification is the fine denier polyamide fiber 6 pre-oriented yarn of the porous spinning cake of 75dtex/144f～110dtex/144f.
Principle of the present invention is: adopt conventional polyamide 6 (polyamide fibre 6) raw material; In raw material, add additive; It is distributed in polyamide 6 (polyamide fibre 6) melt even and finely; The effect that is produced is: the regularity that molecular structure is arranged in order in the fiber is destroyed in (1), reduces the macromolecular degree of orientation and degree of crystallinity; (2) on polyamide 6 (polyamide fibre 6) strand, orientation and crystallization are formed steric hindrance; Under high speed spinning speed, obtain the supramolecular structure of low crystalline rate and low rate of orientation; Make that the development of fiber orientation and crystallization is effectively suppressed on the high-speed spinning silk thread, can control orientation, the degree of crystallinity of spinning Cheng Yingli and fiber; (3) in fibroplastic process, form micro-fiber structure, make these microfibers partly absorb the unnecessary Cheng Yingli that spins under the high winding speed, thereby make orientation and crystallization under high winding speed obtain inhibition.With this understanding; Adopt suitable spinning and stretch forming process conditions, in fibroplastic process, form microfiber, the microfiber that is added partly absorbs the unnecessary Cheng Yingli that spins under the high winding speed; Simultaneously; Stress in polyamide 6 (polyamide fibre 6) matrix reduces effectively, and therefore, orientation and crystallization under high winding speed have obtained inhibition through additive.In technical scheme of the present invention; Can adjust and control the supramolecular structure of crystallization in the process, orientation according to the addition of additive; Adopt reasonable process conditions, thin dawn of functionalization, micro denier, the ultra-fine denier polyamide fiber 6 series of products of function admirables such as realizing obtaining to have the superelevation extension property, be prone to dye level dyeing, evenly dye-uptake and high-color rendering, pliability be good.
Compared with prior art, the invention has the beneficial effects as follows:
1, the present invention has selected a kind of efficient, polymeric additive at a low price; Adopt and reasonably add speed and optimum addition; Improve device and relevant manufacturing condition, controlled the supramolecular structure of aggregated structure adjustment in the spinneret draft forming process, high order orientation and crystallization effectively; Simultaneously,, further improve melt mixed uniformity and pressure stability, effectively adjust and control the coiling tensile stress and the bar of strand and do inhomogeneous rate, improve the after-drawing performance of the fine denier polyamide fiber 6 POY of porous through transforming the FDY device fabrication.
3, the present invention has rationally utilized existing FDY device resource; Flexibility design and the best process conditions of choose reasonable through the Silk Road adjustment; Produce the 75dtex/144f～fine denier polyamide fiber 6 pre-oriented yarn of 110dtex/144f porous product; Have that production cost is low, output is high, produce control, the characteristics such as good product quality, added value height of being easy to.The product specific area that provides is higher; Its fiber construct has the capillary core sucting action and forms the suction wet guiding function, has the silk of superelevation emulation preferably effect, make that its fabric has that moisture absorption is ventilative, washing shrinkage low, painted strong, folding property is good, rotproofness is strong, the plentiful softness of sense of touch, quick-drying washable, non-ironing, premium properties such as drapability is good, comfortableness is good.
The specific embodiment
Below in conjunction with embodiment technical scheme of the present invention is done further to describe.
Embodiment 1
Present embodiment provides a kind of 75dtex/144f porous fine denier polyamide fiber 6 pre-oriented yarn.It is based on the FDY equipment of producing conventional variety; Comprise preparatory crystallization, drying, screw rod melt extruded device; The additive injector is installed on the charging aperture of screw rod melt extruded device; Spinning manifold, measuring pump, filament spinning component, spinnerets device for spinning are installed the Xu Leng heater below spinnerets, the heating region height is 100～120mm; The below installing ring cold wind blower of Xu Leng heater; The boundling oil frame that oils is installed in the below of ring cold wind blower, and the distance of leaving spinnerets is 800 ± 50 mm places; Coiling and forming device comprises first, second godet roller, preparatory Network device and up-coiler, and described preparatory Network device places the centre of first godet roller and second godet roller.
Production technology and condition are following:
The chinlon 6 section relative viscosity is 2.70～3.10, and relative molecular weight is 16000～18000, cuts into slices 145 ℃ of following preparatory crystallizations about 30 minutes; Delivered to the drying tower inner drying 6～8 hours, baking temperature is 155 ℃, guarantees that the section moisture content is less than 30ppm; Dried polyamide fibre 6 is done section and is got into screw rod, and the adding mass fraction is 0.5% additive in chinlon 6 section, and described additive is methacrylate, maleic anhydride and the benzene nanometer randomcopolymer of alkene; By weight percentage; The content of methacrylate is 75%, and the content of maleic anhydride is 10%, and all the other are benzene alkene; Section is with after additive fully mixes in screw rod; Adopt 5 grades of screw rod melt extrusion processes, heating and melting gets into spinning manifold after mixing, measure, filtering; Be extruded as the melt thread through measuring pump, filament spinning component, spinnerets; Become strand through Xu Leng and at ring blowing cooling air set, be drawn to first godet roller through oil boundling, spinning shaft of nozzle then, carry out then being drawn to second godet roller again behind the preparatory network; Carry out coiling and molding with 4000m/min speed through coiler device, process the fine denier polyamide fiber 6 pre-oriented yarn of 75dtex/144f porous (POY) spinning cake.
The fine denier polyamide fiber 6 pre-oriented yarn of 75dtex/144f porous technological parameter is seen table 1; The fine denier polyamide fiber 6 POY of 75dtex/144f porous performance is seen table 2.
Table 1
Table 2
| Performance | Product index |
| Outward appearance/excellent rate | ≥98% |
| Line density (dtex) | 75~110 |
| The line density coefficient of variation (%) | 1.50~1.90 |
| Fracture strength (cN/dex) | 3.45±0.25 |
| Elongation at break (%) | 80±20 |
| Oil content (%) | 0.57±0.03 |
| Bar evenness | 0.85±0.05 |
In the FDY of routine technological process, polyamide fibre 6 (PA6) section is sent into screw rod fusion, compression and homogenising after crystallization in advance, drying; Get into spinning manifold; Be extruded as the melt thread through measuring pump, filament spinning component, spinnerets, and become strand, after nozzle oils boundling, leave spinning shaft at constant temperature, the constant humidity lateral blowing cooling air set of shock chamber; After Network device carries out preparatory network in advance; Be drawn to the first normal temperature drawing roller roller and the second normal temperature drawing roller roller stretches, carry out HEAT SETTING through the 3rd hot-rolling, input hands over the network nozzle to hand over network again; Carry out coiling and molding with 4200 m/min speed through coiler device then, process the fine denier polyamide fiber 6 fullly drawn yarn (FDY) of 100Den/144f porous.In the present invention; After conventional FDY scrap build, the technological process of producing POY is: the melt thread that spinnerets is extruded, adopt Xu Lenghe ring blowing cooled and solidified to become strand;, nozzle leaves spinning shaft after oiling boundling; Again tow is imported the first cold godet roller, after Network device carries out preparatory network in advance, get into the second cold godet roller; Carry out coiling and molding with 4000m/mi～4500 m/mi winding speeds again, process the fine denier polyamide fiber 6 pre-oriented yarn of 75dtex/144f～110dtex/144f porous (POY) spinning cake.
With conventional FDY apparatus in comparison; The melt thread that the present invention extrudes spinnerets in the former FDY equipment is through constant temperature, the constant humidity lateral blowing process for cooling of shock chamber; Change Xu Lenghe ring blowing cooling into, the location-appropriate ground that melt is solidified moves down, the cooling length of increase strand; Delay, control macromolecular orientation and crystallization, help wire strip forming; Adopt ring blowing process for cooling, improved the uniformity of cooling, overcome tow easy defective that forms skin-core structure in high-speed motion.Simultaneously; The present invention also makes first, second normal temperature drawing roller into the first cold godet roller and the second cold godet roller; And change the preparatory Network device before the first normal temperature drawing roller roller among the FDY and be placed between first, second cold godet roller; Cancel the 3rd hot-rolling, divide roll dies and hand over the network nozzle, and the speed of coiler device is made into to carry out coiling and molding with 4000m/mi～4500 m/mi winding speeds, process the fine denier polyamide fiber 6 pre-oriented yarn of 75dtex/144f～110dtex/144f porous (POY) spinning cake.Utilizing existing FDY production equipment, not only can produce FDY but also can produce the POY product, is the FDY production equipment with product flexibilityization; And through the flexibility design of the Silk Road adjustment and the process conditions of choose reasonable the best; The fine denier polyamide fiber 6 pre-oriented yarn of a kind of novel porous preparation technology is provided, and this production technology is simple, and is with low cost; The fine denier polyamide fiber 6 POY of the porous of being produced product has stable performance; It is good with colouring property that bar is done uniformity, flexible operation, characteristics such as added value height; Produce the fine denier polyamide fiber 6 pre-oriented yarn of 75dtex/144f～110dtex/144f porous by technical scheme provided by the invention, can reach the maximization of company interest.
Claims (3)
1. fine denier polyamide fiber 6 pre-oriented yarn of porous; Specification is 75dtex/144f～110dtex/144f, it is characterized in that: it comprises that mass fraction is 0.5～5.0% additive, and described additive is methacrylate, maleic anhydride and the benzene nanometer randomcopolymer of alkene; By weight percentage; The content of methacrylate is 75～85%, and the content of maleic anhydride is 10～12%, and all the other are benzene alkene; The fracture strength of pre-oriented yarn is 3.45 ± 0.25 cN/dex, and elongation at break is 80 ± 20 %.
2. equipment for preparing the fine denier polyamide fiber 6 pre-oriented yarn of porous as claimed in claim 1; Based on the FDY equipment of producing conventional variety; Comprise preparatory crystallization, drying, screw rod melt extruded device; Spinning manifold, measuring pump, filament spinning component, spinnerets device for spinning, cooling curing device and coiling and forming device is characterized in that:
The additive injector is installed on the charging aperture of said screw rod melt extruded device;
Described cooling curing device is Xu Lenghe ring blowing cooling; The Xu Leng heater is installed below spinnerets, and the heating region height is 100～120mm; The below installing ring cold wind blower of Xu Leng heater;
The boundling oil frame that oils is installed in the below of ring cold wind blower, and the distance of leaving spinnerets is 800 ± 50 mm places;
Coiling and forming device comprises first, second godet roller, preparatory Network device and up-coiler, and described preparatory Network device places the centre of first godet roller and second godet roller.
3. method for preparing the fine denier polyamide fiber 6 pre-oriented yarn of porous as claimed in claim 1 comprises that chip drying, melt extruded, melt are extruded, cooling curing, oil nozzle oils and the winding shaping operation, it is characterized in that process conditions are following:
(1) in chinlon 6 section, adding mass fraction is 0.5～5.0% additive; Described additive is methacrylate, maleic anhydride and the benzene nanometer randomcopolymer of alkene; By weight percentage; The content of methacrylate is 75～85%, and the content of maleic anhydride is 10～12%, and all the other are benzene alkene;
(2) section is adopted 5 grades of screw rod melt extrusion processes with after additive fully mixes in screw rod, and the temperature of 5 grades of screw rods is respectively 248 ± 2 ℃, 258 ± 2 ℃, 260 ± 2 ℃, 259 ± 2 ℃ and 259 ± 2 ℃;
(3) melt adopts Xu Lenghe ring blowing process for cooling solidify out into strand after spinnerets is extruded as the melt thread; The heating-up temperature of Xu's device for cooling is 230 ± 2 ℃; The process conditions of ring blowing are: pressure 550Pa, 21 ± 2 ℃ of wind-warm syndrome, humidity 90 ± 5%, wind speed 0.40～0.50 m/s;
(4) the tow input speed after nozzle oils boundling is first godet roller of 3945～4455 m/min; Through pressure is after the preparatory Network device of 0.7 ± 0.05 bar carries out preparatory network; Admission velocity is second godet roller of 4050～4565 m/min again, and godet roller is cold roller; Winding speed with 4000～4500 m/mi carries out coiling and molding, and processing specification is the fine denier polyamide fiber 6 pre-oriented yarn of the porous spinning cake of 75dtex/144f～110dtex/144f.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110432639.3A CN102517679B (en) | 2011-12-21 | 2011-12-21 | The fine denier polyamide fiber 6 pre-oriented yarn of a kind of porous, preparation method and equipment thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110432639.3A CN102517679B (en) | 2011-12-21 | 2011-12-21 | The fine denier polyamide fiber 6 pre-oriented yarn of a kind of porous, preparation method and equipment thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102517679A true CN102517679A (en) | 2012-06-27 |
| CN102517679B CN102517679B (en) | 2016-01-20 |
Family
ID=46288732
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110432639.3A Expired - Fee Related CN102517679B (en) | 2011-12-21 | 2011-12-21 | The fine denier polyamide fiber 6 pre-oriented yarn of a kind of porous, preparation method and equipment thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102517679B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102995146A (en) * | 2012-11-22 | 2013-03-27 | 浙江亚星纤维有限公司 | Method for manufacturing fine denier porous light interlaced nylon 6 high stretch yarns |
| CN102995147A (en) * | 2012-11-22 | 2013-03-27 | 浙江亚星纤维有限公司 | Manufacture method of ultrathin single-fiber polyamide drawn textured yarn (6DTY) |
| CN105839247A (en) * | 2016-06-07 | 2016-08-10 | 苏州龙杰特种纤维股份有限公司 | FDY (fully drawn yarn) equipment for producing POY (pre-oriented yarn) fibers and POY fiber production method thereof |
| CN106637448A (en) * | 2016-12-13 | 2017-05-10 | 苏州金纬化纤工程技术有限公司 | Chemical fiber polyamide filament FDY (fully drawn yarn) electric control device |
| CN113584633A (en) * | 2021-08-03 | 2021-11-02 | 海阳科技股份有限公司 | Preparation method of fine-denier porous fiber chinlon |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1191906A (en) * | 1997-02-25 | 1998-09-02 | 齐默尔股份公司 | Process for processing polymer blends into filaments |
| CN101014731A (en) * | 2004-05-25 | 2007-08-08 | 圣戈班建筑材料股份有限公司 | Loaded polymer fibre, method for the production thereof, use of the same, and composition comprising such fibres |
| CN101074503A (en) * | 2006-05-16 | 2007-11-21 | 东丽纤维研究所（中国）有限公司 | Polymer-alloy fibre and its production |
| CN102161756A (en) * | 2011-04-14 | 2011-08-24 | 杭州师范大学 | Nylon-6 resin, nylon-6 filament and preparation method thereof |
-
2011
- 2011-12-21 CN CN201110432639.3A patent/CN102517679B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1191906A (en) * | 1997-02-25 | 1998-09-02 | 齐默尔股份公司 | Process for processing polymer blends into filaments |
| CN101014731A (en) * | 2004-05-25 | 2007-08-08 | 圣戈班建筑材料股份有限公司 | Loaded polymer fibre, method for the production thereof, use of the same, and composition comprising such fibres |
| CN101074503A (en) * | 2006-05-16 | 2007-11-21 | 东丽纤维研究所（中国）有限公司 | Polymer-alloy fibre and its production |
| CN102161756A (en) * | 2011-04-14 | 2011-08-24 | 杭州师范大学 | Nylon-6 resin, nylon-6 filament and preparation method thereof |
Non-Patent Citations (1)
| Title |
|---|
| 林飞等: ""锦纶6FDY设备柔性化生产工艺探讨"", 《合成纤维工业》, vol. 25, no. 5, 31 December 2002 (2002-12-31) * |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102995146A (en) * | 2012-11-22 | 2013-03-27 | 浙江亚星纤维有限公司 | Method for manufacturing fine denier porous light interlaced nylon 6 high stretch yarns |
| CN102995147A (en) * | 2012-11-22 | 2013-03-27 | 浙江亚星纤维有限公司 | Manufacture method of ultrathin single-fiber polyamide drawn textured yarn (6DTY) |
| CN102995147B (en) * | 2012-11-22 | 2015-03-11 | 浙江亚星纤维有限公司 | Manufacture method of ultrathin single-fiber polyamide drawn textured yarn (6DTY) |
| CN105839247A (en) * | 2016-06-07 | 2016-08-10 | 苏州龙杰特种纤维股份有限公司 | FDY (fully drawn yarn) equipment for producing POY (pre-oriented yarn) fibers and POY fiber production method thereof |
| CN106637448A (en) * | 2016-12-13 | 2017-05-10 | 苏州金纬化纤工程技术有限公司 | Chemical fiber polyamide filament FDY (fully drawn yarn) electric control device |
| CN106637448B (en) * | 2016-12-13 | 2018-12-11 | 苏州金纬化纤工程技术有限公司 | A kind of chemical fiber nylon long filament FDY electrical control gear |
| CN113584633A (en) * | 2021-08-03 | 2021-11-02 | 海阳科技股份有限公司 | Preparation method of fine-denier porous fiber chinlon |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102517679B (en) | 2016-01-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102493016B (en) | Porous superfine polyamide 6 fully-drawn yarn, preparation method thereof, and equipment thereof | |
| CN102517680B (en) | Multi-hole superfine denier polyamide 6 POY/FDY interlacing composite fiber, its preparation method and its device | |
| CN101338455B (en) | Easy-to-dye terylene BCF and method for preparing same | |
| CN102586939A (en) | Profiled fire-retardant bright terylene FDY (Fully Drawn Yarn) filament and production process thereof | |
| CN102839432B (en) | Preparation method of ultra-high-speed spinning polyester pre-oriented yarn | |
| CN101158056A (en) | Production method and product of polyamide moisture-absorbing and sweat-releasing fiber | |
| CN102517679B (en) | The fine denier polyamide fiber 6 pre-oriented yarn of a kind of porous, preparation method and equipment thereof | |
| CN109371570A (en) | A kind of smooth roll hot rolling elastic non-woven and its manufacturing method | |
| CN102031575A (en) | Method for preparing superfine denier flat terylene drawn yarn | |
| CN102517660A (en) | Manufacture method of super-cotton-feeling super-softness flock fiber of polyester | |
| CN104480556A (en) | Production process of high-speed spinning type potential crinkled polyester filament yarns | |
| CN104480555A (en) | Production process of high-elasticity-feature terylene pre-oriented fibers | |
| CN108728921A (en) | A kind of production method of antimicrobial form polyester industrial yarn | |
| CN104278339A (en) | Production technology of polyester FDY bright trilobal yarn | |
| CN109234820A (en) | A kind of preparation method of polylactic acid short-fiber | |
| CN109023564A (en) | A kind of preparation method of polylactic acid coloured cut staple | |
| CN103114344A (en) | Porous superfine denier polyester pre-oriented yarn and preparation method thereof | |
| CN104278344A (en) | Production technology of semi-dull trilobal FDY polyester fiber | |
| CN104278341A (en) | Production process for fine denier cross-shaped profiled polyester filament yarn | |
| CN102828278A (en) | Polyester fully-drawn slub yarn and preparation method thereof | |
| CN108611692B (en) | Preparation method of high-single-fiber nylon 6 fiber based on high-speed spinning | |
| CN106917150A (en) | A kind of high-strength wearable PLA long filament and its production method | |
| CN104562250B (en) | Porous micro-fine denier nylon 6 triisofiber and preparation method and application thereof | |
| CN107164812B (en) | Special-shaped chinlon 6 fiber and preparation method thereof | |
| CN104451919A (en) | Production technology for orderly dacron bamboo node yarns of identical specification |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder |
Address after: Suzhou City, Jiangsu province 215137 Xiangcheng District Ji Road No. 8 Patentee after: SOOCHOW University Address before: 215123 Suzhou City, Suzhou Province Industrial Park, No. love road, No. 199 Patentee before: Soochow University |
|
| CP02 | Change in the address of a patent holder | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180411 Address after: 215000 Industrial Zone, Zhen Ze town, Wujiang, Suzhou, Jiangsu Patentee after: WUJIANG YATAI CHEMICAL TEXTILE Co.,Ltd. Address before: Suzhou City, Jiangsu province 215137 Xiangcheng District Ji Road No. 8 Patentee before: Soochow University |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160120 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |