CN101735608B - Hydroscopic fine denier/superfine denier chinlon master batch, chinlon POY filaments and preparation method thereof - Google Patents
Hydroscopic fine denier/superfine denier chinlon master batch, chinlon POY filaments and preparation method thereof Download PDFInfo
- Publication number
- CN101735608B CN101735608B CN200910311373XA CN200910311373A CN101735608B CN 101735608 B CN101735608 B CN 101735608B CN 200910311373X A CN200910311373X A CN 200910311373XA CN 200910311373 A CN200910311373 A CN 200910311373A CN 101735608 B CN101735608 B CN 101735608B
- Authority
- CN
- China
- Prior art keywords
- nylon
- denier
- spinning
- superfine
- water absorbability
- 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.)
- Expired - Fee Related
Links
Images
Abstract
The invention belongs to the field of spinning materials, and firstly provides a hydroscopic fine denier/superfine denier chinlon master batch which is prepared by adding a hydroscopic modifier, a metallic salt, an antioxidant and other auxiliary agents into nylon 6 chips in proportion to perform melt blending and extrusion, wherein the hydroscopic modifier is PVP; the hydroscopic fine denier/superfine denier chinlon master batch is mixed with the nylon 6 chips to perform melt spinning in proportion, and hydroscopic fine denier/superfine denier chinlon POY filaments are prepared by further performing cooling, oiling bunching and winding on the hydroscopic fine denier/superfine denier chinlon master batch and the nylon 6 chips. The hydroscopic fine denier/superfine denier chinlon POY filaments have the filament number of 0.4 to 0.88 dtex, the breaking strength of 3.3 to 3.8 cN/dtex, the elongation at break of 60 to 120 percent and the fiber hydroscopicity of 4 to 10 percent, so the blank of producing the hydroscopic fine denier/superfine denier chinlon POY filaments by adopting a conventional spinning method at home and abroad is filled up, and simultaneously the improvement on the hydroscopicity of the chinlon POY filaments provides a wider application space for the chinlon POY filaments.
Description
Technical field
The invention belongs to the spinning material field, be specifically related to special-purpose master batch of a kind of water absorbability denier/superfine denier nylon and preparation method thereof and water absorbability denier/superfine denier nylon prepared therefrom.
Background technology
Take synthon at present terylene (polyethylene terephthalate), polyamide fibre (polyamide-based), polypropylene fibre (polypropylene), spandex (urethane), acrylic fibers (polyacrylonitrile) etc. are generally arranged.These fibers have different qualities, thereby different purposes is also arranged.But at present general wearing fabric, because its fiber is thicker, feel is coarse, flexibility is poor, ventilation property is poor, water-absorbent is poor, be easy to pilling.Along with the raising of people's living standard, also more and more higher for the dress requirement of textiles.Address these problems, satisfy people's different requirements, exploitation different sorts, just like a raging fire the carrying out of research novel, functional fiber.
At present, fiber finer dawnization is an important research direction of new fiber development, existing many relevant reports and product.Thin dawn or super fine denier technology such as polyester, polypropylene-base have obtained extensive popularization.But a kind of technical term refers to the 10000m long filament and weighs 1 gram, promptly is called 1dtex.Fiber is thin more, and the dawn number is more little.The thin dawn refers to the fiber of filament number at 3-0.6dtex; Super fine denier refers to the fiber of filament number at 0.2-0.55dtex.
Comfortableness is that clothes are by satisfying the prerequisite performance of Human Physiology health needs, also be the due fundamental propertys of clothes, particularly two season of summer in winter clothes, underwear and children's garment comfortableness is had relatively high expectations, the comfort of summer clothes depends primarily on the water absorbability and the water vapour permeability of material.Water absorbability is meant that dress materials absorb or emit the ability of vapourous water in air.Bibulous lining can in time absorb sweat vapour, the sweat that human body is discharged, and plays heat radiation and regulates the effect of miniclimate humidity between interior table of clothes and body surface, makes human body sensory comfortable.The index of weighing lining water absorbability quality is the percentage that the moisture regain material moisture content accounts for the material dry weight.When there was the relative humidity difference lining both sides, wet steam was called water vapour permeability from the performance that a side saw through, was diffused into opposite side.Human body was whether comfortable when water vapour permeability was directly connected to perspiration.When human body was perspired, there was certain psychrometric difference the lining both sides of clothes, and sweat vapour is transferred to opposite side from pressing close to skin one side.Natural fiber that water vapour permeability is good and regenerated fiber dress material are easy to seeing through of sweat vapour, reduce the humidity in the clothes miniclimate, keep dry and comfortable comfortable.Polyamide fibre has superior physicals, is widely used in fields such as knitted underwear, hosiery, sweat shirt, ski-wear, tights; And compare with polyolefine, trevira, the molecular structure property of polyamide fibre (containing amide group, the analogous protein structure) has good hydrophilic close skin, and toughness is good, rebound resilience good, wear resisting property, also has certain moisture.But compare with traditional natural fiber cotton, hair, silk, its water absorbability, water vapour permeability still exist not enough so cause snugness of fit relatively poor, have also limited it in the directly widespread use of the aspects such as underwear of contact skin.Therefore improve the moisture absorption water vapour permeability of polyamide fibre and improve the very necessity that just seems for its widespread use popularization.The thin dawnization of polyamide fibre can further improve the quality and the value of polyamide fibre on the one hand, can improve the wet thoroughly function of its moisture absorption.Can carry out modification to nylon 6 melt structures on the other hand, thereby improve its water absorbability.
Blend, compound and improve physico-chemical process such as technology is adopted in the production of fine count fiber at present usually, mainly comprises composite algorithm (the island method is peeled off method) and direct method.The use of island method and special-shaped method is to conversion unit, Working environment, and aspects such as manufacturing process require all very harsh, island method complex process particularly, cost increases, the energy consumption height, and bring the potential problem of environmental pollution.A kind of technology of making fine count fiber in addition is on the spinning equipment of existing melt extrusion manufactured conventional fibre, by adjusting polymer property and spinning technology parameter, realizes fiber finer dawnization, belongs to the method for directly spinning.Compare with the island method, this method is a kind of eco-friendly, green high-performance fiber production technology.The equipment of external general using precision, harsh technology is come the fine denier nylon fiber of production filament number more than 0.8dtex, and cost is higher.And at home, compare with polypropylene fibre, terylene, because the characteristic of nylon itself, contain a large amount of hydrogen bonds in the molecular structure, crystallization velocity is fast, and the degree of crystallinity height is difficult for tensile deformation, therefore cause the relatively situation of difficulty of the conventional spinning improved method of present utilization direct production fine-denier polyamide fiber, and just bigger for the difficulty of direct method production super fine denier polyamide fibre.
The method of improving the nylon fibre hygroscopic property at present has: 1. with blend such as a small amount of hydrophilic component such as Polyvinylpyrolidone (PVP)s; 2. hydrophilic component and hexanolactam copolymerization; 3. be copolymerized into hydrophilic polyamide earlier, again with the nylon 6 slice co-blended spinning; 4. carboxyl grafting, amido, cyano group, hydroxyl isopolarity group on nylon 6 molecular backbone chains; 5. by changing the fibre section shape, make fiber heteromorphosis, super-refinement, surface roughening or make fiber form micropore increasing surface-area, thereby improve water absorbability; 6. with hydrophilic agent polyamide fibre or its fabric are carried out the post-treatment processing.In above various method of modifying, copolymerization and grafting method complex process, the implementation cost height is difficult to produce in batches.The physically modified method needs special profile spinneret, such as, application number provides a kind of production method and product of polyamide moisture-absorption perspiration fibre for the Chinese patent application of CN200710028788.7, it mainly is to pass through special production equipment, transform production technique and produce the improvement that the fiber of profiled-cross-section is realized polyamide moisture-absorption, in addition, its production is not fine-denier polyamide fiber; Application number provides a kind of moisture absorption polyamide 6 fibre for the Chinese patent application of CN200610155359.1, and it also is a water absorbability of improving daiamid-6 fiber by the fiber that production has a special cross-section.The fiber water absorbability that post treatment method obtains is difficult to lastingly.Blending method is because technology is simple, and modified effect obviously has been subjected to people's extensive attention.
In the hydrophilic polymer of various suitability for industrialized production, Polyvinylpyrolidone (PVP) has better heat-resisting, water absorbability, hypotoxicity and good physiological compatibility, is the moisture-absorption modified raw material of a kind of comparatively ideal nylon fibre.The patent No. of toray Co., Ltd. application is that the Chinese invention patent of ZL97109686.4 discloses the refining Polyvinylpyrolidone (PVP) (residual monomer content is less than 0.1%) of a kind of employing, with nylon 6 slice melt blending and spinning, make the nylon fibre that water absorbability obviously improves.But owing to be subjected to the restriction of the wettability power of Polyvinylpyrolidone (PVP) own, have only when the Polyvinylpyrolidone (PVP) mass content surpasses 15%, the standard moisture absorption rate score of modification nylon fibre just can reach the level of textile fiber.And after the Polyvinylpyrolidone (PVP) mass content surpassed 15%, modification polyamide fibre toughness sensation contact very uncomfortablely, and the while spinnability is also bad, can not stably carry out spinning.
The patent No. provides a kind of moisture-absorption modifier that is used for polyamide fibre for the Chinese invention patent of ZL200510037289.5: make PVP alkaline hydrolysis ring-opening reaction at normal temperatures and pressures with nanometer cupric ion catalyzer, to obtain moisture-absorption modifier.During application, this moisture-absorption modifier and Nylon 6 co-blended spinning are made nylon fibre on a small quantity.But this invented technology complexity easily causes environmental pollution, and the moisture-absorption modifier consumption is big, and the cost height is difficult for actually operating.In addition, this patent is not pointed out the specification of nylon fibre, and conventional fibre exists obviously different with fine count fiber.
Summary of the invention
The present invention is directed to the shortcoming and defect of prior art,,, make high-hygroscopicity denier/superfine denier nylon POY long filament by using the denier/superfine denier nylon master granule of development voluntarily from preparation denier/superfine denier water absorbability, high added value chinlon POY filaments purpose.Described technology simple possible is saved cost, and spinning process is stable; Simultaneously, the denier/superfine denier water absorbability chinlon POY filaments of making belongs to the high-performance high value added product, can bring considerable economic and social benefit.
The contriver by add water absorbability properties-correcting agent in chinlon master batch, changes nylon 6 melt structures from the chinlon master batch angle, can obviously improve the moisture absorption water vapour permeability of polyamide fibre; Add the metallic salt material in addition, when improving the nylon melt structure, the tensile strength of Reinforced Nylon melt reduces the crystallization rate of nylon melt, thereby a kind of denier/superfine denier nylon POY long filament with excellent moisture absorption property of can producing on common high-speed spinning equipment is provided.The present invention combines the advantage of PVP water absorbability and ultra-fine fibre water absorbability two aspects, thereby makes described denier/superfine denier nylon POY long filament, and its rate of moisture absorption can reach 4-10% (20 ℃, 65%RH); The filament number of described moisture absorption polyamide fibre is 0.4-0.88dtex.
The objective of the invention is to be implemented by the following technical programs:
The contriver at first provides a kind of water absorbability denier/superfine denier nylon master granule, it is to be extruded by moisture-absorption modifier, metallic salt material, antioxidant, dispersion agent and nylon 6 slice melt blending to make, wherein, in the master batch by nylon 6 slice weight, contain moisture-absorption modifier 0.1-10%, metallic salt material 0.5-10%, antioxidant 0.1-1%, dispersion agent 0.1-1%, described moisture-absorption modifier is polyvinylpyrrolidone (PVP).
Why the present invention selects polyvinylpyrrolidone (PVP), based on three aspect reasons: the one, it is the lactan structure, can take place obviously to interact with nylon matrix, changes the nylon melt structure, makes it to be beneficial to spin the denier/superfine denier fiber; The 2nd, the hygroscopic property of PVP own is good, can improve the water absorbability of nylon fiber after compound with nylon; The 3rd, itself is active high, is easy to react with multiple dyestuff, can not influence the dyeing of nylon fiber, even can improve the nylon fiber dyeing behavior, and it is easier to make it dyeing, and it is more lasting to paint.Antioxidant of the present invention can guarantee nylon 6 slice not oxidative degradation in the high-temperature fusion process, nondiscoloration; Tangible chelating coordination can take place with the nylon molecule in the metallic salt material, changes nylon 6 melt structures, increases nylon melt tensile strength, and thin dawn spinning is played an important role; In addition, useful effect also can take place with moisture-absorption modifier PVP in the metallic salt material, plays important synergy in the thin dawn spinning process of water absorbability nylon.The adding of dispersion agent can obviously improve the mixed performance between nylon and metal-salt and the PVP, makes the effective constituent can homodisperse, to make the good and stable water absorbability fine-denier polyamide fiber POY long filament of performance.Moisture-absorption modifier, metallic salt material, antioxidant, dispersion agent and nylon 6 slice are made the water absorbability master batch under suitable proportioning, suitable conditions such as temperature, and then can on conventional spinning equipment, spin out the good denier/superfine denier nylon POY long filament of hygroscopic property.
As preferred version, according to water absorbability denier/superfine denier nylon master granule of the present invention, wherein, it is at least a in the plurality of specifications such as 1000-100000 that described polyvinylpyrrolidone is selected from molecular weight.Such as selecting PVP1000, PVP10000, PVP20000 or the like for use.
As preferred version, according to water absorbability denier/superfine denier nylon master granule of the present invention, wherein, described metallic salt material is selected from the compound of first, second main group and transition metal, comprise one or more combinations in muriate, Sulfates material, the metal carboxylate material, content is the 0.5%-10% of nylon matrix weight.Muriate such as LaCl
3, Sulfates material such as MgSO
4, metal carboxylate material such as Zn (Ac)
2Or the like.
As preferred version, according to water absorbability denier/superfine denier nylon master granule of the present invention, wherein, described antioxidant is selected from one or more in Hinered phenols, triazole species, amine, phosphorous acid esters or the thioesters class antioxidant.Wherein, described hindered phenol anti-oxidants is selected from antioxidant 1010 etc.; The triazole species antioxidant is selected from antioxidant BHT etc.; Amine antioxidants is selected from oxidation inhibitor 5057 etc.; The phosphorous acid esters antioxidant is selected from oxidation inhibitor 168 etc.; The sulfuric acid ester antioxidant is selected from anti-oxidant DLTP etc.
As preferred scheme, the antioxidant among the present invention is from Hinered phenols antioxidant 1010 and phosphite ester kind antioxidant 168.Antioxidant 1010 is a kind of well behaved antioxidant, and stable performance and most polymers have good consistency, and the good discoloration that light and heat causes that prevents can be arranged; Oxidation inhibitor 168 is antioxidants that a kind of resistance to hydrolysis can be good, and stable performance is widely used.The two collaborative use, antioxidant effect can be better.PVP is a kind of amphipathic organic polymer, can be dissolved in most of organic solvents (as ester class, alcohols, amine and acid etc.), can have an effect with above-mentioned antioxidant, strengthens the synergy ability.
As preferably, according to water absorbability denier/superfine denier nylon master granule of the present invention, wherein, described dispersion agent mainly is selected from paraffin, the low-molecular weight polymer at least a.Described lower molecular weight is meant the polymkeric substance of molecular weight at 200-2000, described polymkeric substance comprises polyoxyethylene glycol (PEG), polyvinyl alcohol (PVA), polycaprolactone (PCL) etc., is that 600 and 10000 polyoxyethylene glycol, molecular weight are PVA (polyvinyl alcohol) of 10000 etc. as molecular weight.These dispersion agents have good synergy, can have an effect with nylon matrix, also has good water absorbability, can well dissolve PVP again, guarantee that PVP reached molecular level and disperses before mixing with nylon matrix, enable fully and nylon interacts homodisperse, and then guarantee the carrying out that the thin dawn spinning process of nylon can steady and continuous, reach the purpose of production water absorbability denier/superfine denier nylon.
The present invention also provides the preparation method of above-mentioned water absorbability denier/superfine denier nylon master granule, described preparation method comprises: with moisture-absorption modifier, metallic salt material, antioxidant, dispersion agent and nylon 6 slice mixed melting, through the twin-screw extruder granulation, wherein, nylon 6 melt temperatures are that 190-270 ℃, screw speed are that 10-30r/min, die temperature are 190-250 ℃.
As preferred version, according to the preparation method of water absorbability denier/superfine denier nylon master granule of the present invention, wherein, described nylon 6 slice water ratio is below 600ppm; The moisture-absorption modifier water ratio is below 1000ppm; The metallic salt material is before use in the inherent 150-250 ℃ of dry 6-12h of vacuum drying oven.Thin dawn spinning has significant effects to water ratio to nylon: the water ratio height, easily cause the oxidative degradation of nylon melt, and molecular weight reduces, melt viscosity reduces, and causes tensile strength to reduce, and the spinning lousiness increases, end breakage rate increases, and has a strong impact on spinning production of thin dawn of nylon and fibrous quality thereof.Described nylon 6 slice and moisture-absorption modifier can be dry as follows: the vacuum drum drying, and drying temperature 85-95 ℃, time of drying, the section water ratio promptly can be controlled in the 600ppm at 18-24 hour; The water ratio of moisture-absorption modifier PVP is controlled at below the 1000ppm, and 100-110 ℃ of dry 12-24h gets final product in vacuum drying oven.
The water absorbability denier/superfine denier nylon master granule that the present invention obtains, its melt flow index is 1-10g/10min, melting range is 100-200 ℃.
The present invention also provides a kind of water absorbability denier/superfine denier nylon POY long filament, it is to add above-mentioned water absorbability denier/superfine denier nylon master granule by nylon 6 slice to make through direct high-speed spinning method, the filament number of gained nylon fibre is 0.4-0.88dtex, wherein, the content of additive master batch accounts for the 1-10% of nylon 6 slice weight.Described master batch addition causes in the fine denier nylon spinning process after a little while, and fiber easily breaks end, lousiness, causes cost to raise; When described master batch addition is too high, can cause that fibre strength descends, be unfavorable for that follow-up dyeing and finishing processing weaves.
As preferred version, according to water absorbability denier/superfine denier nylon of the present invention, wherein, the content of additive master batch accounts for the 3-5% of nylon 6 slice weight.The described master batch of preferred version adds scope when realizing that the object of the invention promptly provides the good denier/superfine denier nylon of water absorbability, also can make the production cost optimization.
As preferred version, according to water absorbability denier/superfine denier nylon POY long filament of the present invention, wherein, the breaking tenacity of described water absorbability denier/superfine denier nylon is 3.3-4.0cN/dtex, and elongation at break is 60-120%, and the rate of moisture absorption of fiber is 4-10%.The hygroscopic property of this kind fiber reaches the real silk level, near cotton fine.Simultaneously, the fiber number of polyamide fibre is low among the present invention, near or reach the super fine denier level, belong to the differential fibre category, soft, specific surface area is big and have unique wicking, the moisture absorption performance of having a good sweat greatly improves, thereby dress is more comfortable, can be used for making various high-grade fabrics.
The present invention also provides the preparation method of above-mentioned water absorbability denier/superfine denier nylon POY long filament, and described preparation method comprises the steps: successively
(1) mixed melting spinning: nylon 6 slice adds above-mentioned master batch and carries out the mixed melting spinning, and wherein, the screw pressure during fusion is 90-120kg/cm
2, screw speed is 15-30r/min, spinning temperature is 230-290 ℃; Its diameter of orifice that adopts is that 0.15-0.35mm, length-to-diameter ratio are 2.5-4.0,
(2) cross air blow cooling: the blowing of spinning nozzle ring, wind-warm syndrome 28-40 ℃, humidity 40-60%, wind speed 0.3-0.5m/s,
(3) oil, boundling: through the oil thrower boundling that oils, used finish is the polyamide fibre finish second distillation water miscible liquid of 8-12wt% through the cross air blow cooled fibers; The rate of oiling is 0.8-1.8%
(4) reel: the tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 3500-4500m/min, promptly gets water absorbability denier/superfine denier nylon POY long filament.
Polyamide fibre finish second distillation water miscible liquid of the present invention is about to the polyamide fibre finish adds in proportion in the redistilled water to stir and makes emulsion and get final product, and consumption accounts for polyamide fibre finish and redistilled water total weight by it.The polyamide fibre finish selects for use the general reagent in this area to get final product, and as the chinlon filament HOY that uses among the embodiment, the trade mark is DELION HO-7.
As preferred version, according to the preparation method of water absorbability denier/superfine denier nylon POY long filament of the present invention, wherein, described nylon 6 slice water ratio is below 600ppm; The master batch water ratio is at (more preferably below the 900ppm) below the 1200ppm.The water ratio height easily causes the oxidative degradation of nylon melt, and molecular weight reduces, and melt viscosity reduces, and causes tensile strength to reduce, and the spinning lousiness increases, and end breakage rate increases, and has a strong impact on spinning production of thin dawn of nylon and fibrous quality thereof.Described nylon 6 slice and master batch can be dry as follows: the vacuum drum drying, and drying temperature 85-95 ℃, time of drying, the section water ratio promptly can be controlled in the 600ppm at 18-24 hour; 100-110 ℃ of dry 12-24h in vacuum drying oven, promptly may command master batch water ratio is below 1200ppm.
Water absorbability denier/superfine denier nylon master granule of the present invention is a kind of special-purpose master batch that is exclusively used in production water absorbability denier/superfine denier nylon POY long filament, it utilizes moisture absorption improving agent and nylon 6 slice and other auxiliary agents (comprising antioxidant, dispersion agent) melt blending extruding pelletization, and moisture-absorption modified agent content is the 0.1-10% of nylon 6 slice weight.Use described master batch and nylon 6 slice direct fabrics behind mixed melting in the screw rod then, the master batch addition is the 1-10% (preferred 3-5%) of nylon 6 slice weight, master batch and nylon molecule interact, can change the molecular structure of nylon melt, thereby may ultimately reach the purpose of production water absorbability denier/superfine denier nylon on conventional spinning-drawing machine.The filament number of gained fiber is 0.4-0.88dtex, and fibre breakage intensity is 3.3-4.0cN/dtex, and elongation at break is 60-120%, and the water absorbability of fiber is 4-10%.Water absorbability denier/superfine denier nylon POY continuous yarn product steady quality provided by the invention, water absorbability are good, and Color is better.
Water absorbability denier/superfine denier nylon master granule of the present invention is preparation as follows generally:
(1) gets the raw materials ready:, take by weighing the metallic salt of PVP, the 0.5-10% of its weight 0.1-10%, the antioxidant of 0.1-1%, the dispersion agent of 0.1-1% in nylon 6 slice weight.
(2) preparation method: the nylon 6 slice that vacuum-drying is good mixes in agitator with PVP, and then adding metallic salt material, antioxidant, dispersion agent stir in agitator, mix.Then mixture is poured in the hopper of twin screw extruder (containing static state, dynamic mixer), the mixture melt blending is extruded check rod, wherein nylon 6 melt temperatures are that 190-270 ℃, screw speed are that 10-30r/min, extrusion mould-outlet temperature are 190-250 ℃, extrude product pelletizing behind metal track cooling check rod, master batch throughput is 10-20kg/h.The melt flow index of gained master batch is 1-10g/10min, and melting range is 100-200 ℃.
Water absorbability denier/superfine denier nylon POY long filament of the present invention is preparation as follows generally:
Nylon 6 slice after the vacuum-drying and water absorbability denier/superfine denier nylon master granule are transported in the twin screw high-speed spinning machine, the nylon chips pump is 50-100g/min for amount, the master batch pump is 0.5-10g/min for flow, is that 230-290 ℃, screw speed are that 15-30r/min and screw pressure are 90-120kg/cm at spinning temperature
2Down fused mixture melt is pushed through screw rod (containing static state, dynamic mixer), pump into spinning pack, after extra large sand filters, extrude through orifice (orifice is characterized as: diameter 0.15-0.35mm, length-to-diameter ratio 2.5-4.0) again through metering.In spinning nozzle ring blowing device, be that 28-40 ℃, humidity are that 40-60% and wind speed are cross air blow cooling under the 0.3-0.5m/s then in the wind-warm syndrome that blows out.Then oil through the oil thrower boundling through the cross air blow cooled fibers, the rate of oiling is 0.8-1.8wt%, and used finish is that concentration is the polyamide fibre finish second distillation water miscible liquid of 8-12wt%.The tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 3500-4500m/min.The filament number of gained water absorbability denier/superfine denier nylon POY long filament is 0.4-0.88dtex, and breaking tenacity is 3.3-4.0cN/dtex, and elongation at break is 60-120%, and the fiber rate of moisture absorption is 4-10%.
What the present invention used is the conventional high-speed spinning machine of twin screw, adopts the master batch volume pump accurately to control the master batch adding proportion, utilizes specific spinning pack: orifice footpath 0.15-0.35mm, length-to-diameter ratio 2.5-4.0; Assembly inland sea sand filtering material is the 40-80 order.Screw rod respectively distinguishes temperature and spin manifold temperature is controlled automatically, and screw rod, volume pump rotating speed and melt pressure frequency conversion are controlled automatically.
The water absorbability denier/superfine denier nylon POY long filament finished silk performance of gained of the present invention is as follows:
1. filament number: 0.4-0.88dtex;
2. breaking tenacity: 3.3-4.0cN/dtex;
3. elongation at break is 60-120%;
4. oil length: 0.8-1.8%;
5. the rate of moisture absorption 4-10% of fiber.
Compared with prior art, the present patent application has the following advantages:
1. the present invention adopts the interpolation moisture-absorption modifier, changes the nylon melt structure, thereby can obviously improve the moisture absorption water vapour permeability of polyamide fibre, for the widespread use of fine-denier polyamide fiber provides technical support.
2. add the metallic salt material, when improving the nylon melt structure, the tensile strength of Reinforced Nylon melt reduces the crystallization rate of nylon melt, thereby a kind of denier/superfine denier nylon POY long filament with excellent moisture absorption property of can producing on common high-speed spinning equipment is provided.
3. the present invention combines the advantage of PVP water absorbability and ultra-fine fibre water absorbability two aspects, thereby makes described denier/superfine denier nylon POY long filament, and its rate of moisture absorption can reach 4-10% (20 ℃, 65%RH); The filament number of described moisture absorption polyamide fibre is 0.4-0.88dtex.
4. the present invention adopts the method for the special-purpose master batch of water absorbability denier/superfine denier nylon that interpolation develops voluntarily, on conventional high-speed spinning machine, produce denier/superfine denier nylon POY long filament, with the island method, peel off composite spinning methods such as method and compare, technology is simple, is a kind of eco-friendly high-performance fiber production technology.
5. the present invention adopts conventional high speed spinning method to produce, and cost declines to a great extent, and the gained fibre property is stable, easy dyeing.
6. production method of the present invention is easy, has filled up the blank that domestic and international water absorbability denier/superfine denier nylon POY long filament adopts conventional high speed spinning method to produce, and has promoted the scientific and technological content and the added value of polyamide fibre product.
Description of drawings
Fig. 1 is the technological process of production synoptic diagram of water absorbability denier/superfine denier nylon master granule of the present invention.
Fig. 2 is the technological process of production synoptic diagram of water absorbability denier/superfine denier nylon POY long filament of the present invention.
Embodiment
Below in conjunction with embodiment, be described more specifically content of the present invention.Should be appreciated that enforcement of the present invention is not limited to the following examples, all will fall into protection domain of the present invention any pro forma accommodation and/or the change that the present invention made.
In the present invention, if not refer in particular to, all part, per-cents are weight unit, and all equipment and raw material etc. all can be buied from market or the industry is commonly used.
Main raw material, instrument and equipment:
Nylon 6 slice: relative viscosity 2.47 ± 0.02, density 1.14g/cm
3, fusing point is 215-222 ℃, water ratio is less than 600ppm.
Finish: be polyamide fibre finish second distillation water miscible liquid, wherein said polyamide fibre finish is the chinlon filament HOY that Suzhou this grease of bamboo company limited produces, and the trade mark is DELION HQ-7.
Agitator: high-speed mixing stirrer (good machinery is created in the Zhangjiagang)
Twin screw extruder: twin screw extruder (power chemical industry SHJ-35 is gathered in Nanjing)
Master batch volume pump: Masterbatch volume pump (the new more chemical fiber machinery DKTJ-1 of factory of Wuxi City)
High-speed spinning spinning trier: (Dalian Synthetic Fibres Inst.)
Volume pump: specification: 0.6mL/rep (0.6 milliliter of revolution), its rotating speed is according to calculating such as finished silk fiber number, proportioning raw materials, spinning speeds.
Embodiment 1:
(1) gets the raw materials ready:, take by weighing the PVP (PVP10000 and PVP24000 mass ratio are 2: 1 mixture) of its weight 1.0%, 0.8% MgSO in nylon 6 slice weight
4, 0.2% antioxidant (antioxidant 1010 and oxidation inhibitor 168, the two proportioning are 1: 1), 0.2% dispersion agent (whiteruss and PEG600, the two mass ratio are 1: 1).
(2) preparation method: the nylon 6 slice that vacuum-drying is good (water ratio 600ppm) mixes in agitator with PVP, and then adding metallic salt material, antioxidant, dispersion agent stir in agitator, mix.Then mixture is poured in the hopper of twin screw extruder (containing static state, dynamic mixer), the mixture melt blending is extruded check rod, wherein nylon 6 melt temperatures are that 245 ℃, screw speed are that 20r/min, extrusion mould-outlet temperature are 240 ℃, extrude product pelletizing behind metal track cooling check rod, master batch throughput is 10kg/h.The melt flow index of gained master batch is 6.0g/10min, and melting range is 185-200 ℃.This enforcement gained master batch is used for embodiment 2.
Embodiment 2
Nylon 6 slice after the vacuum-drying (water ratio 580ppm) and water absorbability denier/superfine denier nylon master granule (water ratio 850ppm) are transported in the twin screw high-speed spinning machine, the nylon chips pump is 86.4g/min for amount, the master batch pump is 1.32g/min for flow, is that 281 ℃, screw speed are that 25r/min and screw pressure are 90-110kg/cm at spinning temperature
2Down fused mixture melt is pushed through screw rod (containing static state, dynamic mixer), pump into spinning pack, after extra large sand filters, extrude through orifice (orifice is characterized as: diameter 0.3mm, length-to-diameter ratio 2.7) again through metering.Then in spinning nozzle ring blowing device in the wind-warm syndrome that blows out be 36 ℃, humidity be 50% and wind speed be cross air blow cooling under the 0.3m/s.Then oil through the oil thrower boundling through the cross air blow cooled fibers, the rate of oiling is 0.9wt%, and used finish is that concentration is the polyamide fibre finish second distillation water miscible liquid of 12wt%.The tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 3600m/min.The filament number of gained water absorbability denier/superfine denier nylon POY long filament is 0.8dtex, and breaking tenacity is 3.4cN/dtex, and elongation at break is 90%, and the fiber rate of moisture absorption is 5.5%, oil length 0.8%.
Embodiment 3
(1) gets the raw materials ready:, take by weighing the PVP (PVP10000 and PVP24000 mass ratio are 2: 1 mixture) of its weight 2.4%, 3% Zn (Ac) in nylon 6 slice weight
2, 0.5% antioxidant (antioxidant 1010 and oxidation inhibitor 168, the two proportioning are 1: 1), 0.4% dispersion agent (whiteruss and PEG600, the two mass ratio are 1: 1).
(2) preparation method: the nylon 6 slice that vacuum-drying is good (water ratio 580ppm) mixes in agitator with PVP, and then adding metallic salt material, antioxidant, dispersion agent stir in agitator, mix.Then mixture is poured in the hopper of twin screw extruder (containing static state, dynamic mixer), the mixture melt blending is extruded check rod, wherein nylon 6 melt temperatures are that 246 ℃, screw speed are that 20r/min, extrusion mould-outlet temperature are 240 ℃, extrude product pelletizing behind metal track cooling check rod, master batch throughput is 10kg/h.The melt flow index of gained master batch is 3.9g/10min, and melting range is 180-200 ℃.This enforcement gained master batch is used for embodiment 4.
Embodiment 4
Nylon 6 slice after the vacuum-drying (water ratio 600ppm) and water absorbability denier/superfine denier nylon master granule (water ratio 900ppm) are transported in the twin screw high-speed spinning machine, the nylon chips pump is 86.4g/min for amount, the master batch pump is 2.1g/min for flow, is that 282 ℃, screw speed are that 25r/min and screw pressure are 90-105kg/cm at spinning temperature
2Down fused mixture melt is pushed through screw rod (containing static state, dynamic mixer), pump into spinning pack, after extra large sand filters, extrude through orifice (orifice is characterized as: diameter 0.25mm, length-to-diameter ratio 3) again through metering.Then in spinning nozzle ring blowing device in the wind-warm syndrome that blows out be 35 ℃, humidity be 52% and wind speed be cross air blow cooling under the 0.3m/s.Then oil through the oil thrower boundling through the cross air blow cooled fibers, the rate of oiling is 1.0wt%, and used finish is that concentration is the polyamide fibre finish second distillation water miscible liquid of 12wt%.The tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 3900m/min.The filament number of gained water absorbability denier/superfine denier nylon POY long filament is 0.7dtex, and breaking tenacity is 3.6cN/dtex, and elongation at break is 78%, and the fiber rate of moisture absorption is 6.5%, oil length 0.9%.
Embodiment 5
(1) gets the raw materials ready:, take by weighing the PVP (PVP10000 and PVP24000 mass ratio are 2: 1 mixture) of its weight 4.5%, 5% CaCl in nylon 6 slice weight
2, 0.8% antioxidant (antioxidant BHT and anti-oxidant DLTP, part by weight 1: 1), 0.6% dispersion agent (whiteruss and PCL, the two mass ratio are 1: 1).
(2) preparation method: the nylon 6 slice that vacuum-drying is good (water ratio 600ppm) mixes in agitator with PVP, and then adding metallic salt material, antioxidant, dispersion agent stir in agitator, mix.Then mixture is poured in the hopper of twin screw extruder (containing static state, dynamic mixer), the mixture melt blending is extruded check rod, wherein nylon 6 melt temperatures are that 248 ℃, screw speed are that 22r/min, extrusion mould-outlet temperature are 243 ℃, extrude product pelletizing behind metal track cooling check rod, master batch throughput is 11kg/h.The melt flow index of gained master batch is 2.6g/10min, and melting range is 170-190 ℃.This enforcement gained master batch is used for embodiment 6.
Embodiment 6
Nylon 6 slice after the vacuum-drying (water ratio 600ppm) and water absorbability denier/superfine denier nylon master granule (water ratio 950ppm) are transported in the twin screw high-speed spinning machine, the nylon chips pump is 86.4g/min for amount, the master batch pump is 3.2g/min for flow, is that 283 ℃, screw speed are that 25r/min and screw pressure are 90-105kg/cm at spinning temperature
2Down fused mixture melt is pushed through screw rod (containing static state, dynamic mixer), pump into spinning pack, after extra large sand filters, extrude through orifice (orifice is characterized as: diameter 0.25mm, length-to-diameter ratio 3) again through metering.Then in spinning nozzle ring blowing device in the wind-warm syndrome that blows out be 36 ℃, humidity be 50% and wind speed be cross air blow cooling under the 0.4m/s.Then oil through the oil thrower boundling through the cross air blow cooled fibers, the rate of oiling is 1.2wt%, and used finish is that concentration is the polyamide fibre finish second distillation water miscible liquid of 12wt%.The tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 4050m/min.The filament number of gained water absorbability denier/superfine denier nylon POY long filament is 0.6dtex, and breaking tenacity is 3.7cN/dtex, and elongation at break is 72%, and the fiber rate of moisture absorption is 7.0%, oil length 1.1%.
Embodiment 7
(1) gets the raw materials ready:, take by weighing the PVP (PVP10000 and PVP24000 mass ratio are 2: 1 mixture) of its weight 6%, 8% LaCl in nylon 6 slice weight
3, 0.8% antioxidant (antioxidant BHT and anti-oxidant DLTP, part by weight 1: 1), 0.8% dispersion agent (whiteruss and PVA, the two mass ratio are 1: 1).
(2) preparation method: the nylon 6 slice that vacuum-drying is good (water ratio 600ppm) mixes in agitator with PVP, and then adding metallic salt material, antioxidant, dispersion agent stir in agitator, mix.Then mixture is poured in the hopper of twin screw extruder (containing static state, dynamic mixer), the mixture melt blending is extruded check rod, wherein nylon 6 melt temperatures are that 248 ℃, screw speed are that 22r/min, extrusion mould-outlet temperature are 243 ℃, extrude product pelletizing behind metal track cooling check rod, master batch throughput is 11kg/h.The melt flow index of gained master batch is 1.9g/10min, and melting range is 160-180 ℃.This enforcement gained master batch is used for embodiment 8.
Embodiment 8
Nylon 6 slice after the vacuum-drying (water ratio 600ppm) and water absorbability denier/superfine denier nylon master granule (water ratio 1000ppm) are transported in the twin screw high-speed spinning machine, the nylon chips pump is 86.4g/min for amount, the master batch pump is 4.3g/min for flow, is that 283 ℃, screw speed are that 25r/min and screw pressure are 90-105kg/cm at spinning temperature
2Down fused mixture melt is pushed through screw rod (containing static state, dynamic mixer), pump into spinning pack, after extra large sand filters, extrude through orifice (orifice is characterized as: diameter 0.2mm, length-to-diameter ratio 3.4) again through metering.Then in spinning nozzle ring blowing device in the wind-warm syndrome that blows out be 36 ℃, humidity be 50% and wind speed be cross air blow cooling under the 0.4m/s.Then oil through the oil thrower boundling through the cross air blow cooled fibers, the rate of oiling is 1.3wt%, and used finish is that concentration is the polyamide fibre finish second distillation water miscible liquid of 12wt%.The tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 4150m/min.The filament number of gained water absorbability denier/superfine denier nylon POY long filament is 0.53dtex, and breaking tenacity is 3.83cN/dtex, and elongation at break is 65%, and the fiber rate of moisture absorption is 8%, oil length 1.2%.
Embodiment 9
(1) gets the raw materials ready:, take by weighing the PVP (PVP10000 and PVP24000 mass ratio are 2: 1 mixture) of its weight 8%, 10% LaCl in nylon 6 slice weight
3, 1% antioxidant (antioxidant 1010 and oxidation inhibitor 168, part by weight 1: 1), 1% dispersion agent (whiteruss and PEG600, the two mass ratio are 1: 1).
(2) preparation method: the nylon 6 slice that vacuum-drying is good (water ratio 600ppm) mixes in agitator with PVP, and then adding metallic salt material, antioxidant, dispersion agent stir in agitator, mix.Then mixture is poured in the hopper of twin screw extruder (containing static state, dynamic mixer), the mixture melt blending is extruded check rod, wherein nylon 6 melt temperatures are that 249 ℃, screw speed are that 22r/min, extrusion mould-outlet temperature are 245 ℃, extrude product pelletizing behind metal track cooling check rod, master batch throughput is 11kg/h.The melt flow index of gained master batch is 1.1g/10min, and melting range is 155-170 ℃.This enforcement gained master batch is used for embodiment 10.
Embodiment 10
Nylon 6 slice after the vacuum-drying (water ratio 600ppm) and water absorbability denier/superfine denier nylon master granule (water ratio 1050ppm) are transported in the twin screw high-speed spinning machine, the nylon chips pump is 80.4g/min for amount, the master batch pump is 6.5g/min for flow, is that 285 ℃, screw speed are that 22.5r/min and screw pressure are 90-105kg/cm at spinning temperature
2Down fused mixture melt is pushed through screw rod (containing static state, dynamic mixer), pump into spinning pack, after extra large sand filters, extrude through orifice (orifice is characterized as: diameter 0.18mm, length-to-diameter ratio 3.8) again through metering.Then in spinning nozzle ring blowing device in the wind-warm syndrome that blows out be 35 ℃, humidity be 50% and wind speed be cross air blow cooling under the 0.4m/s.Then oil through the oil thrower boundling through the cross air blow cooled fibers, the rate of oiling is 1.4wt%, and used finish is that concentration is the polyamide fibre finish second distillation water miscible liquid of 12wt%.The tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 4300m/min.The filament number of gained water absorbability denier/superfine denier nylon POY long filament is 0.45dtex, and breaking tenacity is 3.96cN/dtex, and elongation at break is 60%, and the fiber rate of moisture absorption is 9.0%, oil length 1.3%.
Although the contriver has done comparatively detailed elaboration to technical scheme of the present invention and has enumerated, be to be understood that, for the those skilled in the art in this area, according to disclosed content, the foregoing description is modified and/or flexible or to adopt the replacement scheme that is equal to be obvious, the essence that all can not break away from spirit of the present invention, the term that occurs among the present invention are used for can not being construed as limiting the invention the elaboration of technical solution of the present invention and understanding.
Claims (9)
1. water absorbability denier/superfine denier nylon master granule, it is characterized in that, it is to be extruded by moisture-absorption modifier, metallic salt material, antioxidant, dispersion agent and nylon 6 slice melt blending to make, wherein, in the master batch by nylon chips weight, contain moisture-absorption modifier 0.1-10%, metallic salt material 0.5-10%, antioxidant 0. 1-1%, dispersion agent 0. 1-1%, described moisture-absorption modifier is a polyvinylpyrrolidone, and wherein said metallic salt material is selected from MgSO
4, Zn(Ac)
2, CaCl
2Or LaCl
3
2. water absorbability denier/superfine denier nylon master granule as claimed in claim 1 is characterized in that, it is among the 1000-100000 one or more that described polyvinylpyrrolidone is selected from molecular weight.
3. water absorbability denier/superfine denier nylon master granule as claimed in claim 1, it is characterized in that described metallic salt is the compound that is selected from first, second main group and transition metal, comprise one or more combinations in muriate, Sulfates, the metal carboxylate material, be selected from MgSO
4, Zn(Ac)
2, CaCl
2Or LaCl
3Antioxidant is selected from one or more in Hinered phenols, triazole species, amine, phosphorous acid esters or the thioesters class antioxidant; Dispersion agent is selected from paraffin, the low-molecular weight polymer at least a, and described lower molecular weight is meant the polymkeric substance of molecular weight at 200-2000, and described polymkeric substance comprises polyoxyethylene glycol, polyvinyl alcohol, polycaprolactone.
4. the preparation method of the described water absorbability denier/superfine denier nylon master granule of one of claim 1-3, it is characterized in that, described preparation method comprises: with moisture-absorption modifier, metallic salt material, antioxidant, dispersion agent and nylon 6 slice mixed melting, through the twin-screw extruder granulation, wherein, nylon 6 melt temperatures are that 190-270 ℃, screw speed are that 10-30r/min, die temperature are 190-250 ℃.
5. the preparation method of water absorbability denier/superfine denier nylon master granule as claimed in claim 4 is characterized in that, described nylon 6 slice water ratio is below 600ppm; The moisture-absorption modifier water ratio is below 1000ppm.
6. water absorbability denier/superfine denier nylon POY long filament, it is characterized in that, it is to add one of the claim 1-3 direct high speed spinning method of described water absorbability denier/superfine denier nylon master granule by nylon 6 slice to make, the filament number of gained fiber is 0.4-0.88dtex, wherein, the described master batch addition 1-10% that is nylon 6 slice weight.
7. water absorbability denier/superfine denier nylon POY long filament as claimed in claim 6 is characterized in that, described water absorbability denier/superfine denier nylon POY filament breakage intensity is 3.3-4.0 cN/dtex, and elongation at break is 60-120%, and the rate of moisture absorption of fiber is 4-10%.
8. the preparation method of claim 6 or 7 described water absorbability denier/superfine denier nylon POY long filaments is characterized in that described preparation method comprises the steps: successively
(1) melting high-speed spinning: nylon 6 slice adds master batch and carries out melting high-speed spinning, and wherein, the screw pressure during fusion is 90-120kg/cm
2, screw speed is 15-30 r/min, spinning temperature is 230-290 ℃; Its diameter of orifice that adopts is that 0.15-0.35mm, length-to-diameter ratio are 2.5-4.0,
(2) cross air blow cooling: the blowing of spinning nozzle ring, wind-warm syndrome 28-40 ℃, humidity 40-60%, wind speed 0.3-0.5m/s,
(3) oil, boundling: through the oil thrower boundling that oils, used finish is the polyamide fibre finish second distillation water miscible liquid of 8-12wt% through the cross air blow cooled fibers, and the rate of oiling is 0.8-1.8%,
(4) reel: the tow that oils enters winding head through bottom tumbler, top tumbler, rabbit silk head, begins the spinning of reeling, and spinning speed is 3500-4500m/min, promptly gets water absorbability denier/superfine denier nylon POY long filament.
9. the preparation method of water absorbability denier/superfine denier nylon POY long filament as claimed in claim 8 is characterized in that described nylon 6 slice water ratio is below 600ppm; The master batch water ratio is below 1200ppm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910311373XA CN101735608B (en) | 2009-12-14 | 2009-12-14 | Hydroscopic fine denier/superfine denier chinlon master batch, chinlon POY filaments and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200910311373XA CN101735608B (en) | 2009-12-14 | 2009-12-14 | Hydroscopic fine denier/superfine denier chinlon master batch, chinlon POY filaments and preparation method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101735608A CN101735608A (en) | 2010-06-16 |
| CN101735608B true CN101735608B (en) | 2011-07-20 |
Family
ID=42459662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200910311373XA Expired - Fee Related CN101735608B (en) | 2009-12-14 | 2009-12-14 | Hydroscopic fine denier/superfine denier chinlon master batch, chinlon POY filaments and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101735608B (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101935889B (en) * | 2010-09-17 | 2011-07-20 | 北京三联虹普新合纤技术服务股份有限公司 | Production process of fine denier nylon 66 pre-oriented fiber |
| CN103122494B (en) * | 2011-11-18 | 2016-04-20 | 东丽纤维研究所（中国）有限公司 | A kind of moisture absorption type polyester fiber and preparation method thereof |
| CN103696034B (en) * | 2013-09-18 | 2016-01-06 | 杭州师范大学 | The production method of a kind of full-dull thin dawn or super fine denier nylon 6FDY long filament |
| CN104153033B (en) * | 2014-08-13 | 2016-05-04 | 浙江华峰氨纶股份有限公司 | A kind of preparation method of porous easy dyeing spandex |
| CN104562275A (en) * | 2014-11-27 | 2015-04-29 | 杭州师范大学 | Porous micro-fine denier nylon 6 POY filament yarns and preparation method thereof |
| CN105088386A (en) * | 2015-09-02 | 2015-11-25 | 太仓市宏亿化纤有限公司 | Hygroscopic polyamide fiber processing technology |
| CN105544056A (en) * | 2016-01-20 | 2016-05-04 | 段宏伟 | Functional fabric capable of achieving super water absorption, quick-drying, super softness and natural touch feeling and preparation method thereof |
| CN106637492B (en) * | 2016-09-23 | 2019-04-16 | 江西师范大学 | Electrospinning nylon 56/PVA/ boric acid composite nano fiber and preparation method thereof |
| CN108532027B (en) * | 2018-04-24 | 2020-10-02 | 山东科贝尔非织造材料科技有限公司 | PA/PVA sea-island fiber with water-soluble sea phase and production process thereof |
| CN113354843B (en) * | 2020-12-23 | 2023-01-20 | 上海瞬吾商务咨询中心 | Preparation method and application of high-molecular degradable master batch |
| CN113122953B (en) * | 2021-03-16 | 2022-09-16 | 浙江恒逸石化研究院有限公司 | Preparation method of high-shrinkage antistatic polyamide fiber |
| CN115341299A (en) * | 2021-11-11 | 2022-11-15 | 创姿服饰(上海)有限公司 | Safe and environment-friendly composite fiber and preparation method thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10309966A1 (en) * | 2002-03-27 | 2003-10-09 | Barmag Barmer Maschf | Melt spinning assembly control reduces the speed of the spinning pump drive and filament treatment stages during splicing and joining, to allow for bobbin changes and filament break repairs with minimum wastage |
| JP2007521422A (en) * | 2004-01-06 | 2007-08-02 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | Method for producing poly (trimethylene terephthalate) fiber |
| CN101122053A (en) * | 2007-07-13 | 2008-02-13 | 杭州师范大学 | Fine denier or ultra-fine denier nylon fibre and producing method thereof |
| CN101139750A (en) * | 2007-07-13 | 2008-03-12 | 杭州师范大学 | Fine denier or ultra-fine denier nylon fibre and production method thereof |
-
2009
- 2009-12-14 CN CN200910311373XA patent/CN101735608B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10309966A1 (en) * | 2002-03-27 | 2003-10-09 | Barmag Barmer Maschf | Melt spinning assembly control reduces the speed of the spinning pump drive and filament treatment stages during splicing and joining, to allow for bobbin changes and filament break repairs with minimum wastage |
| JP2007521422A (en) * | 2004-01-06 | 2007-08-02 | イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー | Method for producing poly (trimethylene terephthalate) fiber |
| CN101122053A (en) * | 2007-07-13 | 2008-02-13 | 杭州师范大学 | Fine denier or ultra-fine denier nylon fibre and producing method thereof |
| CN101139750A (en) * | 2007-07-13 | 2008-03-12 | 杭州师范大学 | Fine denier or ultra-fine denier nylon fibre and production method thereof |
Non-Patent Citations (3)
| Title |
|---|
| A.F. Xie et al.The coordination and phase separation in nylon–copper chloride system.《Journal of Molecular Structure》.2002,第613卷67-71. * |
| Huizhen Li et al.A New Facile Method for Preparation of Nylon-6 with High.《Macromolecules》.2009,第42卷(第4期),1175-1179. * |
| JP特开2007521422A 2007.08.02 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101735608A (en) | 2010-06-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101735608B (en) | Hydroscopic fine denier/superfine denier chinlon master batch, chinlon POY filaments and preparation method thereof | |
| CN101747624B (en) | Hygroscopic fine denier/superfine denier nylon masterbatch, nylon and preparation method thereof | |
| CN101724265B (en) | Denier/superfine denier nylon master granule, preoriented yarn (POY) and draw textured yarn (DTY) stretch yarn and preparation method thereof | |
| CN103590139B (en) | A kind of powerful three-dimensional crimp memory fiber and manufacture method thereof | |
| CN101792578B (en) | Polyester fiber with functions of wetting, moisture transmitting and quick drying and fabric thereof | |
| CN110644073B (en) | Preparation method of polyester-nylon parallel composite elastic fiber | |
| CN105200550B (en) | A kind of low melting point antibacterial special polyester monofilament and its processing method | |
| US20150147569A1 (en) | Thermo-regulated fiber and preparation method thereof | |
| CN101857981B (en) | Process for producing nanometer bamboo carbon fiber by adopting polylactic acid group | |
| CN103225125A (en) | Modified polylactic acid fiber and preparation method thereof | |
| CN107313128A (en) | A kind of PBT fiber fabrication process | |
| CN1908259A (en) | Preparation method of hollow multi-micropore polyester filament yarn | |
| CN101302666A (en) | Processing process of melt-spun antibiotic spandex filament | |
| CN101158057A (en) | Core-skin type composite fiber and production method thereof | |
| CN101195934A (en) | Moisture absorption polyamide 6 fibre and production method thereof | |
| CN101158054A (en) | Chromatic high-wet conductivity anti-bacterial fiber and spinning method thereof | |
| JP6523454B2 (en) | Process for producing functional yarn having deodorizing property and sweat-absorbing quick-drying property | |
| CN111020727A (en) | Chitosan antibacterial fabric and preparation method and product thereof | |
| CN103726129B (en) | Preparation method of anti-static chinlon/terylene compounded hybrid fiber | |
| CN102877155B (en) | High-simulated-cotton porous superfine-denier polyester fiber and preparation method thereof and preparation equipment | |
| CN103122500B (en) | A kind of Splittable conjugate fiber and obtained Superfine Fibre Fabric thereof | |
| CN101463505A (en) | Negative ion polypropylene hollow air deformation fibre, preparation and use thereof | |
| CN104294396B (en) | Fused mass directly spinning adds the preparation method of antibacterial polyester skin-core structure fiber online | |
| CN101139750B (en) | Fine denier or ultra-fine denier nylon fibre and production method thereof | |
| CN101928999A (en) | PBT (Poly Butylenes Terephthalate) bamboo-charcoal elastic fiber |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110720 Termination date: 20181214 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |