CN1696363A - Composite fiber and its mfg. method - Google Patents
Composite fiber and its mfg. method Download PDFInfo
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- CN1696363A CN1696363A CNA2004100500009A CN200410050000A CN1696363A CN 1696363 A CN1696363 A CN 1696363A CN A2004100500009 A CNA2004100500009 A CN A2004100500009A CN 200410050000 A CN200410050000 A CN 200410050000A CN 1696363 A CN1696363 A CN 1696363A
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- 239000000835 fiber Substances 0.000 title claims abstract description 128
- 238000000034 method Methods 0.000 title claims abstract description 36
- 239000002131 composite material Substances 0.000 title claims description 74
- 238000009987 spinning Methods 0.000 claims abstract description 92
- 229920000642 polymer Polymers 0.000 claims abstract description 60
- 238000009826 distribution Methods 0.000 claims abstract description 51
- 238000004519 manufacturing process Methods 0.000 claims abstract description 20
- 230000008859 change Effects 0.000 claims abstract description 18
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- -1 polyethylene terephthalate Polymers 0.000 claims description 42
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 34
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 34
- 238000009998 heat setting Methods 0.000 claims description 29
- 229920002215 polytrimethylene terephthalate Polymers 0.000 claims description 28
- 229920000728 polyester Polymers 0.000 claims description 19
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Classifications
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
- D01F8/14—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D10/00—Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
- D01D10/02—Heat treatment
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/098—Melt spinning methods with simultaneous stretching
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/28—Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
- D01D5/30—Conjugate filaments; Spinnerette packs therefor
- D01D5/32—Side-by-side structure; Spinnerette packs therefor
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- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/02—Yarns or threads characterised by the material or by the materials from which they are made
- D02G3/04—Blended or other yarns or threads containing components made from different materials
- D02G3/045—Blended or other yarns or threads containing components made from different materials all components being made from artificial or synthetic material
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/22—Yarns or threads characterised by constructional features, e.g. blending, filament/fibre
- D02G3/26—Yarns or threads characterised by constructional features, e.g. blending, filament/fibre with characteristics dependent on the amount or direction of twist
-
- D—TEXTILES; PAPER
- D03—WEAVING
- D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
- D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
- D03D15/20—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads
- D03D15/283—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the material of the fibres or filaments constituting the yarns or threads synthetic polymer-based, e.g. polyamide or polyester fibres
-
- D—TEXTILES; PAPER
- D03—WEAVING
- D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
- D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
- D03D15/40—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the structure of the yarns or threads
- D03D15/47—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the structure of the yarns or threads multicomponent, e.g. blended yarns or threads
-
- D—TEXTILES; PAPER
- D03—WEAVING
- D03D—WOVEN FABRICS; METHODS OF WEAVING; LOOMS
- D03D15/00—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used
- D03D15/50—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the properties of the yarns or threads
- D03D15/56—Woven fabrics characterised by the material, structure or properties of the fibres, filaments, yarns, threads or other warp or weft elements used characterised by the properties of the yarns or threads elastic
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2331/00—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
- D10B2331/04—Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyesters, e.g. polyethylene terephthalate [PET]
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/04—Heat-responsive characteristics
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/06—Load-responsive characteristics
- D10B2401/061—Load-responsive characteristics elastic
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/06—Load-responsive characteristics
- D10B2401/062—Load-responsive characteristics stiff, shape retention
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Multicomponent Fibers (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Woven Fabrics (AREA)
Abstract
The present invention provided a conjugate fiber having excellent stretchability and improved heat-set properties; and to provide a method for producing the conjugate fiber. The conjugate fiber having the excellent stretchability and the improved heat-set properties has >=80% heat set properties after no-load boiling water treatment, and <=20% rate of change in each of elastic moduli at 10% elongation and elongations at break before and after the heat set while having a high elasticity of >=50% crimp elongation and >=70% elastic recovery, and is produced by utilizing different fiber-forming polymers having 5,000-50,000 difference between number average molecular weights, and each 1.5-2.5 molecular weight distribution coefficient. The conjugate fiber produced by this fiber is obtained by minimizing the reduction of processability, functionality and physical properties caused by yarn-bending problems at spinning by minimizing the reduction of the molecular weight, properties of a raw yarn and elongation by reducing retention times of the polymers in a spinning pack, and utilizing a method for sticking strands under a spinning cap to form the fiber into a side-by-side shape having <=1.2 curved surface deforming index and 1.3-2.5 modified cross section degree at the spinning.
Description
Technical field
The present invention relates to composite fibre and manufacture method thereof, the retractility excellence of described composite fibre, heat settability are improved, and when being used for following process, goods stability is improved.In more detail, relate to and have high scalability, its curling extensibility more than or equal to 50%, elastic restoration ratio is more than or equal to 70%, elastic modelling quantity when the heat settability after the zero load boiling water treating stretches more than or equal to 80%, 10% simultaneously and the rate of change of fracture degree of drawing before and after heat setting are smaller or equal to 20%, and the goods stability when being used for the goods following process is conjugate fiber excellent and manufacture method thereof extremely.
In addition, the present invention relates to composite fibre and manufacture method thereof, described composite fibre is an operation of utilizing combination under spinning head, the surf deform coefficient of making smaller or equal to 1.2, degree of deformation is 1.3～2.5 parallel composite fibre, like this, compare with the raw yarn of existing eccentric core-sheath-type, operation, decline functional and physical property that the bent silk problem of described composite fibre when spinning causes have subtracted to minimum degree, it has parallel cross section, retractility and heat settability excellence.
Background technology
About the polyesters elastic fibre, in patent documentation 1, the method for having used 2 kinds the polyethylene terephthalate (PET) of limiting viscosity difference is arranged is disclosed.In addition, in patent documentation 2 and patent documentation 3, disclose the combined polymerization polyethylene terephthalate of using general polyethylene terephthalate and highly shrinkable, made the method that polyesters has the fiber of potential crimping property.In addition, in patent documentation 4 and patent documentation 5, disclose in polyethylene terephthalate (PET), used the method for polytrimethylene terephthalate (PTT) or polybutylene terephthalate (PBT) with draftability.
But the curling retractility composite fibre that the manufacture method of putting down in writing in the existing described patent is made is not mentioned the variation of heat settability, heat endurance, heat treatment front and back physical property especially.Under the situation of general retractility composite fibre, after the zero load boiling water treating during heat setting, elastic modelling quantity when its shape stability stretches smaller or equal to 70%, 10% and the rate of change of fracture degree of drawing before and after heat setting are more than or equal to 20%, so also serious metamorphosis can take place after subsequent handling or last processing, goods add and are difficult to set its processing conditions man-hour, also produce the problem that is difficult to make dimensionally stable.
Generally, fibre will stand 130～190 ℃ thermal process and the pulling force of 1～2g/d when tentering.At this moment, the heat settability of raw yarn and before and after the heat setting variation of physical property be the key factor of the morphological stability of decision raw yarn and goods thereof.Therefore, in order to make the model deformation minimum of raw yarn and goods thereof, must be in the heat settability that improves existing retractility composite fibre, make the elastic modelling quantity and the rate of change minimum of fracture degree of drawing before and after heat setting of raw yarn, solve the problem that model deformation takes place in the prior art in subsequent handling with this.
The stability that affirmations such as the inventor show heat setting and the morphological stability of raw yarn and goods thereof have confidential relation, and find when the fiber crimp extensibility more than or equal to 50%, elastic restoration ratio is more than or equal to 70%, elastic modelling quantity when the heat settability after the zero load boiling water treating of fiber stretches more than or equal to 80%, 10% simultaneously and the rate of change of fracture degree of drawing before and after heat setting were smaller or equal to 20% o'clock, be used for raw yarn and end article thereof, can make the morphological stability excellence.
In addition, basically only propose to adopt different polyesters macromolecules to make composite spinning about the patent of retractility composite fibre in the past, do not mention of the influence of the molecular weight of the relevant different high molecular polymers that constitute composite fibre itself physical property of composite fibre.In the patent documentation 4, the viscosity of having mentioned PET, the PTT of polyethylene terephthalate (PET), polytrimethylene terephthalate (PTT) and modification changes the change in physical of bringing, but this piece patent is not mentioned the different high molecular molecular weight that constitutes composite fibre yet.Certainly,, can infer molecular weight, still, can not get the information of relevant molecular weight distribution from the relation of viscosity-molecular weight according to mark-Hao sound storehouse equation (Mark-Houwink equation).And the inventor etc. have found to have the molecular weight and the molecular weight distribution of 2 kinds of different polyester polymers of differences in viscosity is the factor that influences fiber retractility and heat settability, and has designed the molecular weight and the molecular weight distribution of 2 kinds of polymer the bests.
Composite fibre constructed in accordance, in spinning process, reduced the time of staying of polymer in filament spinning component, minimum degree is reduced in the reduction of minimizing, its raw yarn physical property and the retractility of molecular weight, utilize spinning head shown in Figure 1, utilization makes it the technology of combination under spinning head, make like that as shown in Figures 2 and 3 the surf deform coefficient smaller or equal to 1.2, degree of deformation be 1.3～2.5 parallel.Like this, compare with the raw yarn of existing eccentric core-sheath-type shown in Figure 4, minimum degree is reduced in manufacturability, decline functional and physical property that composite fibre constructed in accordance bent silk problem during with spinning is brought.In addition, according to different described polymer and operation characteristic, can improve the heat settability of raw yarn, the morphological stability of goods when realizing raw yarn and subsequent handling, and excellences such as the strong extensibility of raw yarn and expansion performance, so composite fibre constructed in accordance can be used for weaven goods, weft knitting, the multiple use through compiling etc.
Patent documentation 1 spy opens flat 10-72732 communique
Patent documentation 2 spies open the 2000-328378 communique
Patent documentation 3 spies open flat 9-41234 communique
No. 3671379 communique of patent documentation 4 United States Patent (USP)s
Patent documentation 5 spies open flat 11-189923 communique
Summary of the invention
The objective of the invention is to, utilization can provide the retractility composite fibre and the manufacture method thereof of goods heat settability and morphological stability excellence at the polyesters macromolecule of the formed fiber of industrial use.
Therefore, the inventor etc. are in order to achieve this end, carried out deep research, found that in can forming the polyesters macromolecule of fiber, the composite fibre that the macromolecule that the difference of utilizing number-average molecular weight is 5000～50000, molecular weight distribution coefficient separately is 1.5～2.5 different formed fiber is made, its retractility excellence; In addition, also find aspect the minimizing deformation when making expansion performance and heat setting, best polymer is made of 2 kinds of compositions, the polyethylene terephthalate family macromolecule that first composition is that number-average molecular weight is 10000～20000, the molecular weight distribution coefficient is 1.5～2.5 formed fiber; The polytrimethylene terephthalate macromolecule that second composition is that number-average molecular weight is 15000～70000, the molecular weight distribution coefficient is 1.5～2.5 formed fiber.The difference of the number-average molecular weight of polymer is smaller or equal to 5000 the time, and the curling extensibility and the elastic restoration ratio of raw yarn are difficult to represent; And more than or equal to 50000 o'clock shortcoming be, because the high temperatureization of spinning temperature further reduces molecular weight, so the effect of polymer can not embody, in addition, during spinning owing to produce bent silk, and be difficult to guarantee manufacturability, and the contractive effect enhancing owing to the molecular weight height, thereby cause heat settability poor.In addition, the molecular weight distribution coefficient being limited to 1.5～2.5, is because if less than 1.5, and molecular weight distribution is too average, and the self-plasticizing action of low molecular weight substance becomes very little, is easy to generate problem on the technology; And the molecular weight distribution coefficient is greater than 2.5, and it is big that molecular weight distribution becomes, and produces several polymer mixed effects, causes heat settability and retractility to reduce.
In addition, the inventor etc. also find, for the high polymer of molecular weight, during spinning, its molecular weight reduces because of thermal decomposition is serious, and molecular weight distribution also broadens, if but polymer melt was minimized in the time of staying of filament spinning component, for example smaller or equal to 5 minutes, just can bring into play physical property that described characteristic brings and functional to the full extent.
In addition, the surf deform coefficient between the polymer in raw yarn cross section surpasses 1.2, and during spinning, the situation that produces bent silk is serious, has problems on manufacturability, and this becomes the reason that retractility descends.This tendency is more serious when cross sectional shape is eccentric core-sheath-type as shown in Figure 4.Therefore, the invention is characterized in, in order to improve manufacturability that the retractility composite fibre makes and functional, use 2 kinds of polyester polymers that can form fiber among the present invention, utilization makes it the technology of combination under spinning head, with parallel (mating type) form throwing shown in Figure 3, and make that the surf deform coefficient between the polymer is smaller or equal to 1.2 on the raw yarn cross section this moment, degree of deformation is 1.3～2.5.
As another aspect of the present invention, for the retractility composite fibre that obtains by melt spinning, the contraction of cloth and silk is serious when subsequent handling, goods add man-hour, be difficult to impose a condition, even also model deformation can take place after the final processing, so be difficult to keep the dimensionally stable of sewings, this is that variation because of raw yarn physical property before and after the heat settability of retractility raw yarn and the heat setting causes.Generally, fibre will stand 130～190 ℃ thermal process and the pulling force of 1～2g/d when tentering, and the heat settability of raw yarn is the key factor of the morphological stability of decision raw yarn and goods thereof.Therefore, elastic modelling quantity when the objective of the invention is stationarity when controlling heat setting after the zero load boiling water treating during fabrication for the model deformation that makes goods is minimum and stretching more than or equal to 80%, 10% and the rate of change of fracture degree of drawing before and after heat setting be smaller or equal to 20%, thereby make the model deformation minimum of subsequent handling.
The invention provides composite fibre, it is made of first composition and second composition, and described first composition is a polyethylene terephthalate, and described second composition is a polytrimethylene terephthalate; Described composite fibre heat settability and retractility excellence, curling extensibility when zero load boiling water treating more than or equal to 50%, elastic restoration ratio more than or equal to 70%, when heat settability stretches more than or equal to 80%, 10% elastic modelling quantity and the rate of change of fracture degree of drawing before and after heat setting smaller or equal to 20%.
In addition, the preferred cross-sections form is parallel form, and the surf deform coefficient is smaller or equal to 1.2, and the degree of deformation in cross section (a/b) is 1.3～2.5.
In addition, a kind of polymer in the preferred described polymer is a polyethylene terephthalate, and its mean molecule quantity is 10000～20000, and the molecular weight distribution coefficient is 1.5～2.5; Another kind of polymer is a polytrimethylene terephthalate, and its number-average molecular weight is 15000～70000, and the molecular weight distribution coefficient is 1.5～2.5; The difference of the number-average molecular weight of these two kinds of polymer is 5000～50000.
In addition, the invention provides by comprising the heat settability that operation (A) and method (B) are made and the manufacture method of retractility conjugate fiber excellent, wherein, operation (A) is for making the operation of two kinds of polyester fusions, wherein a kind of polymer is a polyethylene terephthalate, number-average molecular weight is 10000～20000, the molecular weight distribution coefficient is 1.5～2.5, another kind of polymer is a polytrimethylene terephthalate, number-average molecular weight is 15000～70000, the molecular weight distribution coefficient is 1.5～2.5, and the difference of the number-average molecular weight of two kinds of polymer is 5000～50000; Operation (B) makes described fused mass pass through filament spinning component, its time of staying in filament spinning component was smaller or equal to 5 minutes, then at 2200～4000 meters/minute spinning speed, with parallel form, obtain the surf deform coefficient smaller or equal to 1.2, the degree of deformation (a/b) in cross section is behind 1.3～2.5 the compound silk, stretch and the operation of heat fixation.
In addition, the manufacture method of retractility composite fibre of the present invention preferably adopts partially oriented-stretching/false twisting technology to make.
In addition, described draft temperature is preferably 85～95 ℃, and the heat fixation temperature is preferably 130～200 ℃.
In addition, during described spinning, preferably under spinning head, from bent deformation of filament angle that the right angle orientation of nozzle surface departs from smaller or equal to 20 °.
In addition, the invention provides the twisting count made with described retractility composite fibre (TM: sth. made by twisting/rice) be 150～2000 processing silk.
In addition, the invention provides described retractility composite fibre and degree of drawing more than or equal to 50%, boiling water shrinkage is more than or equal to the blended fiber silk of the raw yarn blending of 15% highly shrinkable.
In addition, the invention provides the cloth and silk that contains described retractility composite fibre.
Retractility composite fibre constructed in accordance, has high scalability, its curling extensibility more than or equal to 50%, elastic restoration ratio is more than or equal to 70%, rate of change before and after elastic modelling quantity when the heat settability after the zero load boiling water treating stretches more than or equal to 80%, 10% simultaneously and the heat setting of fracture degree of drawing is smaller or equal to 20%, so the stability of the goods of raw yarn and following process is extremely excellent.In addition, the composite fibre for being made by the present invention during spinning, has reduced the time of staying in filament spinning component, and minimum degree is reduced in the reduction of minimizing, its raw yarn physical property and the retractility of molecular weight.In addition, compare with existing raw yarn, heat settability improves and minimum degree is reduced in the elastic modelling quantity when making 10% to stretch and the decline of the rate of change of fracture degree of drawing before and after heat setting among the present invention, thereby has realized the morphological stability of subsequent handling goods.In addition, retractility composite fibre constructed in accordance has made section morphology parallel, the surf deform coefficient smaller or equal to 1.2, the section deformation degree is on 1.3～2.5 the level, the decline of bent silk generation and surf deform coefficient is reduced to minimum, outside its manufacturability excellence, powerful degree of drawing, heat settability and the expansion performances etc. of raw yarn are also excellent, thus its go for weaven goods, weft knitting, through multiple uses such as volumes.
Description of drawings
Fig. 1 is the sectional view of the spinning head that uses among the present invention.
Fig. 2 (a)-(c) is the sectional view of retractility and heat settability conjugate fiber excellent constructed in accordance.
Fig. 3 is the surf deform coefficient of expression elastic fibre constructed in accordance and the figure of degree of deformation.
Fig. 4 is the surf deform coefficient of the eccentric core-sheath-type elastic fibre of expression and the figure of degree of deformation.
Fig. 5 is the figure at the bent deformation of filament angle of expression elastic fibre constructed in accordance when making.
The specific embodiment
For the composite fibre of the present invention that the heat settability of making raw yarn and goods thereof is improved, the polyesters macromolecule that the difference of preferably using number-average molecular weight is 5000～50000, molecular weight distribution coefficient separately is 1.5～2.5 different formed fiber.About each high molecular characteristic and analytical method and manufacture method, with conjugated polymer material and utilize the spinning process of polymeric material to carry out following explanation.
(1) high molecular characteristic of polyesters and analytical method thereof that the difference of number-average molecular weight is 5000～50000, molecular weight distribution coefficient separately is 1.5～2.5 different formed fiber.
For 2 kinds of polymer that use among the present invention, for the difference that makes number-average molecular weight is 5000～50000, separately molecular weight distribution coefficient is that the 1.5～2.5, the 1st composition polyethylene terephthalate base polymer must number-average molecular weight be 10000～20000, the molecular weight distribution coefficient is 1.5～2.5; The 2nd composition polytrimethylene terephthalate base polymer must number-average molecular weight be 15000～70000, the molecular weight distribution coefficient is 1.5～2.5.
Among the present invention, as polymer, the polymer of the 1st composition uses that number-average molecular weight is 10000～20000, the molecular weight distribution coefficient is 1.5～2.5 polyethylene terephthalate, and the polymer of the 2nd composition uses that number-average molecular weight is 15000～70000, the molecular weight distribution coefficient is 1.5～2.5 polytrimethylene terephthalate.
Method manufacturings such as the bulk polymerization known to these polymer can be used generally, polymerisation in solution, interfacial polymerization.Among the present invention, purpose polymers can be made with any one method wherein, and especially preferably by the polymer of melt polymerization in the mass polymerization or solid polymerization manufacturing, such polymer is favourable aspect manufacturing cost.
Among the present invention, the minimum of a value of the molecular weight of low molecular weight polyethylene terephthalate polymer is decided to be 10000, and the peak of the molecular weight of high molecular polyethylene terephthalate polymer is decided to be 70000, and it be the reasons are as follows.Make the polymer of molecular weight less than 10000, not so difficult for polymerization itself.But, carry out fibration in order to utilize this polymer, the form that is made into sheet bits (or particle) shape is favourable.And molecular weight less than 10000 is broken too easily when making the sheet bits, so be difficult to make the sheet bits with uniform shapes.Molecular weight surpasses at 70000 o'clock, and polymerization time is long, and is not only unfavorable at economic aspect, and owing to must excessively improve spinning temperature, thermal decomposition causes molecular weight to reduce, so its effect can not embody.
In addition, the molecular weight distribution coefficient is limited to 1.5～2.5.This be because, if the molecular weight distribution coefficient less than 1.5, then molecular weight distribution self-plasticizing action peaceful all, low molecular weight substance is very little, generation problem easily on the technology; The molecular weight distribution coefficient was greater than 2.5 o'clock, and it is big that molecular weight distribution becomes, and shows as a plurality of polymer mixed effects, produced the problem that heat settability and retractility descend.
Among the present invention, number-average molecular weight and molecular weight distribution coefficient are that polymer and the composite fibre of making are dissolved in the hexafluoroisopropanol (HFIP), utilize high temperature GPC equipment (U.S. Waters company), with polystyrene as primary standard substance, measure number-average molecular weight (Mn) and weight average molecular weight (Mw), converse molecular weight distribution coefficient (PDI) from following formula (1).
PDI＝Mw/Mn
(2) manufacturing of composite fibre
When carrying out melt spinning for making composite fibre, the spinning temperature of polymer is set at the temperature higher 20～70 ℃ than each polymer melting temperature, the temperature that the spinning temperature of polymer exceeds than polymer melting temperature is during less than 20 ℃, can cause become too high, operability of pressure in the extruder to reduce because of fusion is inhomogeneous.In addition, be easy to generate problems such as the physical property of the composite fibre of making is inhomogeneous, so be not preferred.In addition, the temperature that the spinning temperature of polymer exceeds than the melt temperature of polymer is during greater than 70 ℃, and the flowability of polymer improves, but problems such as polymer generation thermal decomposition, so be not preferred.
Make each fibrous polymer combination under spinning head that spues, can produce the composite fibre in parallel cross section.The gradient in the hole that spues of the spinning head that the present invention uses, as shown in Figure 1, preferred 10～30 °.The gradient in hole is less than 10 ° if spue, and when utilizing molecular structure two kind polymer spinning different with molecular weight, is difficult to solve the problem that bent silk takes place so; During greater than 30 °, the uneven phenomenon in raw yarn cross section taking place, brings baneful influence for the quality and the manufacturability of raw yarn, so be not preferred.
In addition, the eccentric core-sheath-type composite fibre of combined spinning in filament spinning component, molecular weight during because of spinning and differences in viscosity produce bent silk problem, address this problem and to use spinning head shown in Figure 1, as Fig. 2 and Fig. 3, surf deform coefficient on the control raw yarn cross section between the polymer is smaller or equal to 1.2, and degree of deformation is 1.3～2.5.
In addition, when the inventor finds the high polymer spinning of molecular weight, molecular weight reduces significantly owing to thermal decomposition, molecular weight distribution broadens, and at utmost reduce time of staying of the polymer melt in the filament spinning component, it was decided to be smaller or equal to 5 minutes, can brings into play physical property that described feature brings and functional to the full extent.
For the composite fibre that obtains, can adopt the partially oriented yarn stretching/false twisting technology of utilizing in the common polyester complex fiber manufacturing to carry out fibration.
As the inscape of core technology of the present invention, can enumerate spinning speed is decided to be 2200～4000 meters/minute.This be because, with smaller or equal to 2200 meters/minute speed spinning the time, because of causing the discharge-amount of molten mass, the low speed spinning reduces, this is not only unfavorable in economic aspect, and the draw ratio when stretching increases, and causes percent thermal shrinkage to rise, and is final, the heat settability of raw yarn and goods is descended, and end article is to the impatient poly-decline of the form stable of heat.Generally, the fiber that crystallization is arranged that forms with the high magnification stretching under low spinning speed shows the high shrinkage to heat.In addition, with greater than 4000 meters/minute spinning speed spinning the time, thermal characteristics, physical features between the polymer of 2 kinds of different molecular weights have a great difference, and this causes spinnability to reduce, and then the stability decreases of spinning process, so be not preferred.
Among the present invention, being characterized as of another core technology inscape when adopting partially oriented-stretching/false twisting technology to make, is decided to be 85～95 ℃ with draft temperature, and the heat fixation temperature is decided to be 130～200 ℃.For draft temperature, be difficult to form equably less than 85 ℃ temperature and stretch, and greater than 95 ℃ temperature, heat increases the degree of plasticising, and operation and physical property thereof during spinning become unstable.The heat fixation temperature is during less than 130 ℃, and the percent thermal shrinkage of raw yarn and goods increases, and morphological stability descends, and in addition, the heat fixation temperature is during greater than 200 ℃, and it is big that the plasticising degree becomes, and operation and every physical property descend, so be not preferred.
For existing retractility composite fibre, cloth and silk dwindles generally more than or equal to 10%, because of model deformation takes place the heat settability difference when the postorder operation, so goods add man-hour, be difficult to set the goods processing conditions, in addition, be difficult to keep the problem of sewings dimensionally stable in addition.General fibre is usually when weaving/dyeing processing, heat fixation, stand 130～190 ℃ thermal process and the pulling force of 1～2g/d, the inventor has found that the heat settability of raw yarn and the morphological stability of raw yarn and goods have confidential relation, and then the heat settability of knowing the raw yarn after the zero load boiling water treating is more than or equal to 80%, elastic modelling quantity during 10% stretching and the rate of change of fracture degree of drawing before and after heat setting were smaller or equal to 20% o'clock, and the metamorphosis in the time of can making the postorder operation drops to minimum degree.
Physical property and the functional table 1 that is shown in according to the fiber made of creating conditions of the present invention.
Below, based on following embodiment, illustrating in greater detail the present invention, following embodiment just illustrates the present invention, not delimit the scope of the invention.
Metewand and its assay method of the physical property of mating type composite fibre made according to the method for the present invention at first, are described.
(1) assay method of number-average molecular weight and molecular weight distribution
With polymer dissolution in hexafluoroisopropanol (HFIP), utilize high temperature GPC equipment (U.S. Waters company), mensuration is the number-average molecular weight (Mn) and the weight average molecular weight (Mw) of primary standard substance with the polystyrene, converses molecular weight distribution coefficient (PDI) from following formula (1)
PDI＝Mw/Mn
(2) assay method of curling extensibility and elastic restoration ratio
In order to measure the curling extensibility and the elastic restoration ratio of its physical property of making among the embodiment of conduct that forms curling composite fibre, operate by following.
Zero load down, impregnation of fibers bundle after 30 minutes in boiling water, with the fibre bundle drying at room temperature, application of load 0.1g/d, after 2 minutes, remove weight, placed 10 minutes, will be through the sample of earlier stage, under the 0.002g/d load, place after 2 minutes, measure length (L this moment
1).On described sample, add the 0.1g/d load, measure the length (L after 2 minutes
2).Then, remove 0.1g/d load after, measure the length (L after 2 minutes
3).Calculate curl extensibility and elastic restoration ratio with following formula (2) and formula (3).
Extensibility (%)=[(L curls
2-L
1)/L
2] * 100 ... (2)
Elastic restoration ratio (%)=[(L
2-L
3)/(L
2-L
1)] * 100 ... (3)
(3) assay method of heat settability
Zero load down through 30 minutes boiling water heat treatment, after the air dry, measure the fibre length (T under the deadweight
1).With described tensile fiber 50%, after fixing, measured length (T
2), 130 ℃ of dry heat treatment are 30 minutes then, carry out heat setting.Behind the cool to room temperature, unclamp fixture, measure fibre length (T
3), with the heat settability of following formula (4) calculating fiber.
Heat settability (%)=[(T
3-T
1)/(T
2-T
1)] * 100 ... (4)
The assay method of the rate of change of elastic modelling quantity during (4) 10% stretchings and fracture degree of drawing.
Under zero load, after 30 minutes boiling water heat treatment, utilize Instron 5565 (Instron company), be 65% at 20 ℃, relative humidity, the initial stage load is under the 0.002g/d condition, before and after heat setting, elastic modelling quantity when measuring raw yarn 10% stretching and fracture degree of drawing.Elastic modelling quantity when elastic modelling quantity when heat setting preceding 10% stretches and fracture degree of drawing relatively hot setting back 10% stretch and the rate of change of fracture degree of drawing are represented as shown in the formula (5) and (6) in percentage (%).
The rate of change (%) of elastic modelling quantity before and after the heat setting=[(elastic modelling quantity when 10% elastic modelling quantity-heat setting preceding 10% when stretching stretches after the heat setting)/(elastic modelling quantity during preceding 10% stretching of heat setting)] * 100 ... (5)
Rate of change=[(heat setting after rupture degree of drawing-heat setting before fracture degree of drawing)/(heat setting before fracture degree of drawing)] * 100 of fracture degree of drawing before and after heat setting ... (6)
(5) assay method of bent deformation of filament angle
With angle (°) degree (Fig. 5) that departs from from the right angle orientation of nozzle surface of the silk thread that collaborates under the spinning head of expression.
(6) the surf deform coefficient and the degree of deformation in raw yarn cross section
As Fig. 2, Fig. 3 and shown in Figure 4, with the cross section of scanning electronic microscope (SEM) analysis raw yarn, with following formula (7) and formula (8) expression.
Surf deform coefficient=c/d ... (7)
Degree of deformation=a/b ... (8)
Embodiment 1
Make in the process of retractility composite fibre, setting spinning temperature is 270 ℃, spinning speed is the 2600m/ branch, the time of staying is 4 minutes in the assembly, utilize existing melt composite spinning equipment, with 5: 5 ratio of weight ratio, with number-average molecular weight (Mn) is 12632, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight (Mn) are 19149, molecular weight distribution coefficient (PDI) is 2.4 polytrimethylene terephthalate, with the parallel cross section of Fig. 2-(a), making the surf deform coefficient is 1.10, the section deformation degree is 1.7, monofilament fineness is the polyester complex fiber of 3.4 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, making monofilament fineness is the retractility composite fibre of 2.1 Denier.When implement stretching, draw ratio is 1.70, draft temperature is that 85 ℃, heat fixation temperature are 155 ℃, the results are shown in table 1.Bent deformation of filament angle is little during the spinning of the fiber that obtains, and shows excellent heat settability and expansion performance.
Embodiment 2
Make in the process of retractility composite fibre, setting spinning temperature is 275 ℃, spinning speed is 2600 meters/minute, the time of staying is 4 minutes in the assembly, utilize existing melt composite spinning equipment, with 5: 5 ratio of weight ratio, with number-average molecular weight (Mn) is 12632, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight (Mn) are 33522, the polytrimethylene terephthalate of molecular distribution coefficient (PDI is) 2.1, with the parallel cross section of Fig. 2-(a), making the surf deform coefficient is 1.10, the section deformation degree is 1.9, monofilament fineness is the polyester fiber composite fibre of 3.4 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, making monofilament fineness is the retractility composite fibre of 2.1 Denier.When implement stretching, draw ratio is 1.70, draft temperature is that 90 ℃, heat fixation temperature are 160 ℃, the results are shown in table 1.Bent deformation of filament angle is little during the spinning of the fiber that obtains, and shows excellent heat settability and expansion performance.
Embodiment 3
Make in the process of retractility composite fibre, setting spinning temperature is 280 ℃, spinning speed is 2400 meters/minute, the time of staying is 4 minutes in the assembly, utilize existing melt composite spinning equipment, with 5: 5 ratio of weight ratio, with number-average molecular weight (Mn) is 15385, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight are 45589, molecular weight distribution coefficient (PDI) is 2.2 polytrimethylene terephthalate, with the parallel cross section of Fig. 2-(a), making the surf deform coefficient is 1.10, the section deformation degree is 1.8, monofilament fineness is the polyester complex fiber of 3.4 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, making monofilament fineness is the retractility composite fibre of 2.1 Denier.When implement stretching, draw ratio is 1.70, draft temperature is that 90 ℃, heat fixation temperature are 160 ℃, the results are shown in table 1.Bent deformation of filament angle is little during the spinning of the fiber that obtains, and shows excellent heat settability and expansion performance.
Embodiment 4
Make in the process of retractility composite fibre, setting spinning temperature is 285 ℃, spinning speed is 2200 meters/minute, the time of staying is 4 minutes in the assembly, utilize existing melt composite spinning equipment, with 6: 4 ratio of weight ratio, with number-average molecular weight (Mn) is 15385, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight (Mn) are 63312, molecular weight distribution coefficient (PDI) is 2.0 polytrimethylene terephthalate, with the parallel cross section of Fig. 2-(b), making the surf deform coefficient is 1.15, the section deformation degree is 1.8, monofilament fineness is the polyester complex fiber of 3.4 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, making monofilament fineness is the retractility composite fibre of 2.1 Denier.When implement stretching, draw ratio is 1.62, draft temperature is that 90 ℃, heat fixation temperature are 180 ℃, the results are shown in table 1.Bent deformation of filament angle is little during the spinning of the fiber that obtains, and shows excellent heat settability and expansion performance.
Comparative example 1
Make in the process of retractility composite fibre, setting spinning temperature is 270 ℃, spinning speed is 2600 meters/minute, the time of staying is 4 minutes in the assembly, utilize existing melt composite spinning equipment, with 5: 5 ratio of weight ratio, with number-average molecular weight (Mn) is 12632, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight (Mn) are 16950, molecular weight distribution coefficient (PDI) is 2.4 polytrimethylene terephthalate, with the parallel cross section of Fig. 2-(a), making the surf deform coefficient is 1.10, the section deformation degree is 1.6, monofilament fineness is the polyester complex fiber of 3.4 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, and making monofilament fineness is the retractility composite fibre of 2.1 Denier, when implementing to stretch, draw ratio is 1.70, draft temperature is that 85 ℃, heat fixation temperature are 145 ℃, the results are shown in table 1.Bent deformation of filament angle is little during the spinning of the fiber that obtains, but shows that heat settability and retractility are low.
Comparative example 2
Make in the process of retractility composite fibre, setting spinning temperature is 270 ℃, spinning speed is 2600 meters/minute, the time of staying is 8 minutes in the assembly, utilize existing melt composite spinning equipment, with 5: 5 ratio of weight ratio, with number-average molecular weight (Mn) is 12632, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight (Mn) are 24411, molecular weight distribution coefficient (PDI) is 2.7 polytrimethylene terephthalate, with the eccentric core-sheath-type cross section of Fig. 4, making the surf deform coefficient is 1.55, the section deformation degree is 1.0, monofilament fineness is the polyester complex fiber of 3.4 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, making monofilament fineness is the retractility composite fibre of 2.1 Denier.When implement stretching, draw ratio is 1.70, draft temperature is that 85 ℃, heat fixation temperature are 140 ℃, the results are shown in table 1.Bent deformation of filament angle is big during the spinning of the fiber that obtains, and shows that heat settability and expansion performance are low.
Comparative example 3
Make in the process of retractility composite fibre, setting spinning temperature is 275 ℃, spinning speed is 1400 meters/minute, the time of staying is 8 minutes in the assembly, utilize existing melt composite spinning equipment, with 5: 5 ratio of weight ratio, with number-average molecular weight (Mn) is 12632, molecular weight distribution coefficient (PDI) is that 2.2 polyethylene terephthalate and number-average molecular weight (Mn) are 31290, molecular weight distribution coefficient (PDI) is 2.8 polytrimethylene terephthalate, with the parallel cross section of Fig. 2-(a), making the surf deform coefficient is 1.20, the section deformation degree is 1.7, monofilament fineness is the polyester complex fiber of 6.0 Denier.Utilize other stretching device, the composite fibre that obtains through described spinning/batch is stretched, making fineness is the retractility composite fibre of 2.1 Denier.When implement stretching, draw ratio is 2.90, draft temperature is that 75 ℃, heat fixation temperature are 145 ℃, the results are shown in table 1.Bent deformation of filament angle is little during the spinning of the fiber that obtains, but shows that heat settability and expansion performance are low.
Table 1
| Embodiment 1 | Embodiment 2 | Embodiment 3 | Embodiment 4 | Comparative example 1 | Comparative example 2 | Comparative example 3 | ||
| Polymer A (Mn) | ????PET ????(12632) | ????PET ????(12632) | ????PET ????(15385) | ????PET ????(15385) | ????PET ????(12632) | ????PET ????(12632) | ????PET ????(12632) | |
| Polymer B (Mn) | ????PTT ????(19149) | ????PTT ????(33522) | ????PTT ????(45589) | ????PTT ????(63312) | ????PTT ????(16950) | ????PTT ????(24411) | ????PTT ????(31290) | |
| ??PDI(A/B) | ????2.2/2.4 | ?????2.2/2.1 | ????2.2/2.2 | ????2.2/2.0 | ????2.2/2.4 | ????2.2/2.7 | ????2.2/2.8 | |
| The time of staying in the assembly (minute) | ????4 | ????4 | ????4 | ????4 | ????4 | ????8 | ????8 | |
| Spinning temperature (℃) | ????270 | ????275 | ????280 | ????285 | ????270 | ????270 | ????275 | |
| Spinning speed (rice/minute) | ????2600 | ????2600 | ????2400 | ????2200 | ????2600 | ????2600 | ????1400 | |
| Bent deformation of filament angle (°) | ????5 | ????7 | ????10 | ????15 | ????5 | ????35 | ????10 | |
| Section morphology 1) | ????S/S | ????S/S | ????S/S | ????S/S | ????S/S | ????S/C | ????S/S | |
| Surf deform coefficient (c/d) | ????1.10 | ????1.10 | ????1.10 | ????1.15 | ????1.10 | ????1.55 | ????1.20 | |
| Degree of deformation (a/b) | ????1.7 | ????1.9 | ????1.8 | ????1.8 | ????1.6 | ????1.0 | ????1.7 | |
| Draw ratio | ????1.70 | ????1.70 | ????1.70 | ????1.62 | ????1.70 | ????1.70 | ????2.90 | |
| Draft temperature (℃) | ????85 | ????90 | ????90 | ????90 | ????85 | ????85 | ????75 | |
| The heat fixation temperature (℃) | ????155 | ????160 | ????160 | ????180 | ????145 | ????140 | ????145 | |
| Curling extensibility (%) | ????59 | ????63 | ????58 | ????57 | ????28 | ????37 | ????41 | |
| Elastic restoration ratio (%) | ????79 | ????80 | ????82 | ????81 | ????69 | ????70 | ????69 | |
| Heat settability | ????82 | ????86 | ????85 | ????88 | ????80 | ????75 | ????77 | |
| Rate of change (%) before and after the heat setting 2) | Modulus during 10% stretching | ????10 | ????13 | ????12 | ????14 | ????16 | ????23 | ????30 |
| The fracture degree of drawing | ????-12 | ????-15 | ????-14 | ????-16 | ????-1?8 | ????-20 | ????-25 | |
1) S/S: parallel, S/C: eccentric core-sheath-type
2) after the zero load boiling water treating, elastic modelling quantity during 10% stretching and the rate of change (%) of fracture degree of drawing before and after heat setting
Claims (10)
1, heat settability and retractility conjugate fiber excellent is characterized by, and described fiber is made of two kinds of compositions, and first composition is a polyethylene terephthalate, and second composition is a polytrimethylene terephthalate; Curling extensibility during boiling water treating that it is zero load is more than or equal to 50%, and elastic restoration ratio is more than or equal to 70%, and elastic modelling quantity when heat settability stretches more than or equal to 80%, 10% and the rate of change of fracture degree of drawing before and after heat setting are smaller or equal to 20%.
2, heat settability as claimed in claim 1 and retractility conjugate fiber excellent is characterized by, and its section morphology is parallel form, and the surf deform coefficient is smaller or equal to 1.2, and the degree of deformation a/b in cross section is 1.3～2.5.
3, heat settability as claimed in claim 1 and retractility conjugate fiber excellent is characterized by, and a kind of polymer is a polyethylene terephthalate, and its number-average molecular weight is 10000～20000, and the molecular weight distribution coefficient is 1.5～2.5; Another kind of polymer is a polytrimethylene terephthalate, and its number-average molecular weight is 15000～70000, and the molecular weight distribution coefficient is 1.5～2.5; The difference of the number-average molecular weight of these two kinds of polymer is 5000～50000.
4, the manufacture method of heat settability and retractility conjugate fiber excellent, it is characterized by, it comprises following operation: the operation that (A) makes two kinds of polyester fusions, a kind of polymer is a polyethylene terephthalate, and number-average molecular weight is 10000～20000, and the molecular weight distribution coefficient is 1.5～2.5, another kind of polymer is a polytrimethylene terephthalate, number-average molecular weight is 15000～70000, and the molecular weight distribution coefficient is 1.5～2.5, and the difference of the number-average molecular weight of two kinds of polymer is 5000～50000; (B) make described fused mass pass through filament spinning component, its time of staying in filament spinning component was smaller or equal to 5 minutes, then at 2200～4000 meters/minute spinning speed, with parallel form, obtain the surf deform coefficient smaller or equal to 1.2, the degree of deformation a/b in cross section is behind 1.3～2.5 the compound silk, stretch and the operation of heat fixation.
5, the manufacture method of heat settability as claimed in claim 4 and retractility conjugate fiber excellent is characterized by, and described stretching process adopts partially oriented-stretching/false twisting technology to make.
6, the manufacture method of heat settability as claimed in claim 4 and retractility conjugate fiber excellent is characterized by, and described draft temperature is 85～95 ℃, and the heat fixation temperature is 130～200 ℃.
7, the manufacture method of heat settability as claimed in claim 4 and retractility conjugate fiber excellent is characterized by, when spinning, under the spinning head from bent deformation of filament angle that the right angle orientation on spinning head surface departs from smaller or equal to 20 °.
8, the processing silk is characterized by, and it is made by the described retractility composite fibre of claim 1, and twisting count TM is 150～2000.
9, the blended fiber silk is characterized by, its be by the described retractility composite fibre of claim 1 and extensibility more than or equal to 50%, boiling water shrinkage forms more than or equal to the raw yarn blending of 15% high shrinkage character.
10, cloth and silk is characterized by, and it contains described heat settability of claim 1 and retractility conjugate fiber excellent.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR0033921/2004 | 2004-05-13 | ||
| KR10-2004-0033921A KR100531618B1 (en) | 2004-05-13 | 2004-05-13 | Conjugated fiber and manufacturing thereof |
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| Publication Number | Publication Date |
|---|---|
| CN1696363A true CN1696363A (en) | 2005-11-16 |
| CN100334272C CN100334272C (en) | 2007-08-29 |
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|---|---|---|---|
| CNB2004100500009A Expired - Lifetime CN100334272C (en) | 2004-05-13 | 2004-06-24 | Composite fiber and its mfg. method |
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|---|---|
| JP (1) | JP3953052B2 (en) |
| KR (1) | KR100531618B1 (en) |
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| TW (1) | TW200536970A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102864510A (en) * | 2012-09-11 | 2013-01-09 | 浙江恒逸高新材料有限公司 | Preparation method of special-shaped easy-to-dye modified polyester composite elastic yarn |
| CN103866422A (en) * | 2012-12-13 | 2014-06-18 | 罗莱家纺股份有限公司 | Polymer fiber with high heat shrinkage and preparation method thereof |
| WO2016124027A1 (en) * | 2015-02-06 | 2016-08-11 | 欧阳文咸 | Production method for ptt-pet parallel composite flexible short fiber without mechanical crimping |
| CN112996956A (en) * | 2018-11-06 | 2021-06-18 | 东丽株式会社 | Stretch yarn, fiber product, composite spinneret, and method for producing composite fiber |
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| KR100700796B1 (en) * | 2005-11-07 | 2007-03-28 | 주식회사 휴비스 | Spontaneous high-crimp polyester multiple staple fiber, and spun yarn and nonwaven fabric containing the same |
| KR101273357B1 (en) | 2006-12-28 | 2013-06-12 | 주식회사 효성 | Polyethyleneterephthalate yarn with good thermal performance and high tenacity for industrial use |
| KR100808567B1 (en) * | 2007-04-30 | 2008-02-29 | 성안합섬주식회사 | High-volume yarns and their textiles using alkali-soluble polyester resins and methods for producing the same |
| CN103924344A (en) * | 2014-05-04 | 2014-07-16 | 苏州市叶绣工艺厂 | Rayon embroidery thread for embroidery |
| CN113913991A (en) * | 2021-10-11 | 2022-01-11 | 江苏箭鹿毛纺股份有限公司 | Piece-dyed elastic wool fabric of functional modified polyester composite filament and preparation method thereof |
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| EP1280947B1 (en) * | 2000-05-11 | 2008-08-06 | E.I. Du Pont De Nemours And Company | Meltblown web |
| JP2002054029A (en) * | 2000-05-29 | 2002-02-19 | Toray Ind Inc | Highly crimped polyester-based conjugate fiber |
| JP4720014B2 (en) * | 2001-05-17 | 2011-07-13 | 東レ株式会社 | Polyester composite yarn having latent crimp expression, method for producing the same, and package |
| US6656586B2 (en) * | 2001-08-30 | 2003-12-02 | E. I. Du Pont De Nemours And Company | Bicomponent fibers with high wicking rate |
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2004
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- 2004-06-07 JP JP2004168244A patent/JP3953052B2/en not_active Expired - Lifetime
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102864510A (en) * | 2012-09-11 | 2013-01-09 | 浙江恒逸高新材料有限公司 | Preparation method of special-shaped easy-to-dye modified polyester composite elastic yarn |
| CN103866422A (en) * | 2012-12-13 | 2014-06-18 | 罗莱家纺股份有限公司 | Polymer fiber with high heat shrinkage and preparation method thereof |
| WO2016124027A1 (en) * | 2015-02-06 | 2016-08-11 | 欧阳文咸 | Production method for ptt-pet parallel composite flexible short fiber without mechanical crimping |
| CN112996956A (en) * | 2018-11-06 | 2021-06-18 | 东丽株式会社 | Stretch yarn, fiber product, composite spinneret, and method for producing composite fiber |
| CN112996956B (en) * | 2018-11-06 | 2023-10-03 | 东丽株式会社 | Telescopic processing yarn, fiber product, composite spinneret and manufacturing method of composite fiber |
Also Published As
| Publication number | Publication date |
|---|---|
| KR100531618B1 (en) | 2005-11-29 |
| JP3953052B2 (en) | 2007-08-01 |
| CN100334272C (en) | 2007-08-29 |
| JP2005325495A (en) | 2005-11-24 |
| TW200536970A (en) | 2005-11-16 |
| KR20050109316A (en) | 2005-11-21 |
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Assignee: Hyosung chemical (Jiaxing) Co.,Ltd. Assignor: Hyosung Corp. Contract record no.: 2010990000255 Denomination of invention: Hot melting complex fiber and preparation method Granted publication date: 20070829 License type: Exclusive License Open date: 20051116 Record date: 20100507 |
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