CN1048765C - Polyester mixed yarns with fine filaments - Google Patents

Polyester mixed yarns with fine filaments Download PDF

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Publication number
CN1048765C
CN1048765C CN93117656A CN93117656A CN1048765C CN 1048765 C CN1048765 C CN 1048765C CN 93117656 A CN93117656 A CN 93117656A CN 93117656 A CN93117656 A CN 93117656A CN 1048765 C CN1048765 C CN 1048765C
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filament
yarn
long filament
value
stretching
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CN93117656A
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CN1092483A (en
Inventor
H·R·E·弗兰克波特
B·H·克诺斯
G·A·派
小·E·E·莫斯特
S·B·约翰逊
小·J·F·伦敦
R·J·科林斯
D·G·宾尼
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Invista Technologies Sarl
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EI Du Pont de Nemours and Co
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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
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • 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
    • D01D5/082—Melt spinning methods of mixed yarn
    • 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
    • D02G1/00—Producing crimped or curled fibres, filaments, yarns, or threads, giving them latent characteristics
    • D02G1/18—Producing crimped or curled fibres, filaments, yarns, or threads, giving them latent characteristics by combining fibres, filaments, or yarns, having different shrinkage characteristics
    • 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
    • D—TEXTILES; PAPER
    • D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
    • D02J1/00—Modifying the structure or properties resulting from a particular structure; Modifying, retaining, or restoring the physical form or cross-sectional shape, e.g. by use of dies or squeeze rollers
    • D02J1/22—Stretching or tensioning, shrinking or relaxing, e.g. by use of overfeed and underfeed apparatus, or preventing stretch

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Artificial Filaments (AREA)

Abstract

Polyester mixed fine filament yarns having excellent mechanical quality and uniformity, and preferably with a balance of good dyeability and shrinkage, are prepared by a simplified direct spin-orientation process by selection of polymer and spinning conditions.

Description

The method for making of non-stretching mixed filament polyester spray silk orientated yarns reaches by its yarn that makes
What the present invention relates to is polyester (continuously) combined filament yarn (comprising fine filament) and the improvement thereof in different filament deniers and/or cross section, and preferably relates to this class yarn that the polyester combined filament yarn of various different performances can be provided from same materials; The present invention also comprises improved method for making and the new product that obtains thus.
In history, the synthetic fiber (comprising polyester fiber) that will be used for clothes are supplied in textile industry and more or less duplicate natural fabric and/or improve on natural fabric to make fabric and clothes, its objective is.For many years, dawn number (dpf) scope of every threads of commodity synthetic textile filament (for example be clothes manufacturing and use) and common natural fabric (i.e. cotton and mao) is similar.Yet the dpf scope of recently commercially available polyester filament is similar in appearance to (being the rank of 1dpf) of real silk, or even inferior dawn number (promptly less than about 1dpf), although its cost is higher.Recently, to the low for example about 1dpf of dpf or even the commercial interest of counting fiber of lower dawn produced owing to a variety of causes.Quoting as a reference we here is referred to as " female application " WO92/13119 and relates to novel direct melt-out spinning/winding manufactured fine filament, as a comparison, existing method for making is to be sprayed into thicker long filament earlier, the latter's further processing in the operation (comprising stretching) of uniting or separating then is with the required long filament that obtains low dawn number but have the fabric property of being applicable to.The long filament of " female application " is " a spray silk-orientation "; That is, be the long filament of " not stretching ".Its importance has carried out discussing and will discussing later on technically.
We have found that, (all yarns have identical cross-section and identical dawn number to yarn to the consumer to fine filament weaving (flat or distortion), and particularly the dawn number of this long filament less than about 1 dawn) reaction tended to their application limitations on selected textiles, " body " of fabric and " drapability " have become inessential in such fabric, or " body " and " drapability " that provide fabric by the structure that makes the twisting of many filament yarns and/or change fabric costliness too for special final use, and/or this change has adverse effect and makes that this kind fabric is not desirable other character (for example outward appearance and feel).People expectation needn't make the fine filament yarn twisting and/or changes fabric construction and directly make the finespun fabric with required " body " and " drapability " by elongated gauze.People also expect, a kind of elongated gauze that silk one orientation does not stretch that sprays can be provided, comprehensive according to its performance, it can be as directly using yarn or stretching feeding yarn (for example generating stretch flat yarn or distortion " varicosity " yarn), these yarns can provide fabric " body " or " drapability " and needn't carry out for example expensive yarn twisting, also needn't change fabric construction and sacrifice its outward appearance and fabric feeling.
Keep uniformity and various spray silk oriented yarn from start to finish and be important by the uniformity between the elongate filaments of its gained.The shortage uniformity often shows as on final DYED FABRICS dyeing defect, thereby does not expect.
For the purpose of weaving, " textile strand " must have some performance, for example sufficiently high modulus and yield point, and enough low contraction, this just makes common textile strand be different from common " feeding yarn ", and it serves as to make fabric and use required performance subsequently to produce MIN that the latter needs further processing.Usually, we claim non-modified continuous filament yarn for " flat yarn " here, and the prolate gauze that claims not stretch is " feeding " or " stretch and feed " yarn, here not needing to stretch and/or heat treatment and the filament yarn that can be used as textile strand is called " directly using yarn " again.
Important is to will be appreciated that the comprehensive of all properties of special yarn (or clothes) is important to any special final use, and this yarn is the yarn itself in the processing sometimes, but also is with final fabric or the clothes of this yarn as its composition sometimes.Is easy by processed to reduce contraction, but this modification is accompanied by other variations usually, and therefore, this comprehensive or balance of any just clothes (or staple fibre) performance is important.People also understand, according to the present invention, can supply and/or process this long filament with the form of yarn or endless tow, and this endless tow needn't have the very cohesion of " yarn ".A lot of long filaments can be called " yarn " or " bundle ", and do not attempt to limit especially by this term but for convenience.People will recognize that this method for making also can be used for the polyester filament of other forms under suitable occasion, tow for example, and this tow can be transformed into staple fibre then, and is used according to the balance of its performance.As described below, this balance be the expectation and also can obtain.
Be used to prepare spray silk-orientation of the present invention identical that the polyester polymers of combined filament yarn can be with " mother applies for " that do not stretch.
The preparation polyester does not stretch, and in fact (this is described in " background that mother applies for " with " spray silk-orientation " method of " female application " for the spray silk-method for alignment of thin mixed filament feeding yarn, and at Fig. 4 A, discuss among B and the C) identical, this feeding yarn is made up of the cross section difference and/or the different long filament of dawn number of two or more types, and the dawn number of wherein at least a long filament component is less than about 1; Preferably when being stretched to 30% when elongation average yarn filament denier wherein less than about 1; And particularly, the average yarn filament denier of thin combined filament yarn wherein is less than about 1.But the selection and the discharging mode hole shape of the spinneret capillary size (L and D) in these two kinds of method for makings are different, so that can spray two or more different long filament compositions altogether; And if desired, a spray silk hardware configuration has been modified, so that interweaving and different long filament components are being carried out quenching and conflux before winding enters packing material.
From before spraying the polyester filament mixture of higher dpf altogether, and under the low speed of prior art, spray the polyester filament mixture altogether, with the effort of the undrawn filament that makes low orientation, we can carry out common spray and also have this fact of uniformity and feel very surprised the mixture of a kind of like this dawn number and cross section from a spinnerets.This mother that can create surprised effect applies for that processing method has some unique thing.
As what will be appreciated that, useful especially mixed filament stretching feeding yarn has two types of long filaments, and a kind of dpf is less than about 1, and is called " (dpf) 1", and another kind of during as the stretching feeding yarn its dpf not only greater than 1, and even be stretched to required degree for example be stretched to required residual stretch than the dpf of (RDR) back gained also greater than 1.
People wish that usually the RDR value of two types elongate filaments is all in the scope of about 1.2X to 1.4X.People wish that also the stretching feeding yarn can be stretched and not produce long filament or " thin neck stretches " defective.The difference of RDR of certainly also wishing two class long filaments is less than about 40%, so the difference of the RDR of elongate filaments type is about 20% or littler.The long filament of higher dpf that (non-circle) cross section that has abnormity is provided is to obtaining a kind of very effective technology of needed object.
The combined filament yarn (it is " flat ") of the different dpf of varying cross-section (a kind of greater than 1, a kind of less than 1) is desirable with regard to sense of touch and aesthetic feeling.Equally, wherein all long filaments all are that low shrink direct also is useful with this class combined filament yarn of yarn.In this, non-circle cross-section wishes to provide useful means to obtain required object concerning the long filament of higher dpf.
The yarn that makes with the inventive method can be used as: 1) the stretching feeding yarn is (for example in method for making that separate or associating, in daraf(reciprocal of farad), in stretching air jet texturing method, twist with the fingers in the deformation method stretching in stretching gear crimping method and the curling method of stretching stuffing box at the stretching false add); 2) can be used as direct usefulness " fabric " combined filament yarn and do not need the non-stretching thin combined filament yarn that stretches again and/or heat; 3) need not stretch (for example in air jet texturing, the stretching in stuffer box crimping and the gear crimping) and can be used as non-stretching direct usefulness " fabric " yarn of feeding yarn; 4) with or need not heat and with or can partially or completely stretch without after-baking and to become carefully combined filament yarn of the non-stretching direct usefulness " fabric " of even thin combined filament yarn.
Aforementioned spray silk-directed method provides a kind of spray silk one directed polyester non-stretching combined filament yarn, and polyester polymers wherein is characterised in that the scope of relative viscosity (LRV) is about 13 to about 23, zero to shear fusing point (T M°) scope be about 240 ℃ to about 265 ℃, the scope of glass transition temperature (Tg) is about 40 ℃ to about 80 ℃; Wherein form combined filament yarn by two or more long filament components, these long filaments are inequality aspect cross section and/or dawn number, and the filament denier of wherein at least a long filament component is less than about 1 (for example average stretch yarn filament denier (dpf) of preferably average yarn filament denier (dpf) s DLess than about 1, wherein (dpf) DBe defined as (dpf) sX[(1.3)/(1+Eb/100) s]; And particularly non-stretching yarn average filament dawn number (dpf) s is less than about 1), wherein for combined filament yarn, high denier filament (2) is about 2 to being about 6 to the ratio of low denier filament (1); And it is characterized in that: maximum dry thermal contraction tension force ST MaximumAt xeothermic peak contraction tension force temperature T (ST Maximum) when being higher than about 5 ℃ to about 30 ℃ of glass transition temperature of polymer Tg for less than about 0.2g/d; (1-S/Sm) value is at least about 1 (preferably being at least about 0.25) so that the ageing stability contraction to be provided; Elongation at break (E B) about 40% to about 160% (the stretching feeding yarn is preferably about 90% to about 120%, and in particular for about 40% to about 90%, and (1-S/Sm) value is at least 0.85 so that as the non-stretching direct yarn of using); The strength range in 7% when elongation is about 0.5 to about 1.75g/d and (the stretching feeding yarn is preferably about scope of 0.5 to about 1g/d (7% intensity T when extending particularly 7Intensity T when being less than 20% elongation 20, with the stability that improve to stretch), to as directly with yarn then particularly in the scope of about 1～1.75g/d); And fracture strength (T B) n, be normalized to 20.8 polymer RLV, be at least about 5g/dl and preferably be at least about 6g/d): and preferred difference in shrinkage (DHS-S) is less than+2%.
Non-stretching combined filament yarn of the present invention provides stretch flat yarn or air jet texturing combined filament yarn, their long filament difference in shrinkage is at least 5%, non-stretching combined filament yarn is made being stretched to the scope of main crystallization start temperature (Tc °) by glass transition temperature of polymer (Tg), it is characterized in that remaining extension at break (E B) be that about 15% intensity to about 45%, 7% when elongation is at least about 1g/d; And directly carry out by cold stretch but do not carry out the flat yarn of special stretching mixed filament that the back heat setting makes and the difference in shrinkage of air jet texturing yarn is at least 5% non-stretching with combined filament yarn, above and cold drawn different combined filament yarns described here be further characterized in that residue extension at break (E B) be about 15%～55%, and the intensity during 7% elongation is at least about 1g/d.
Flat yarn of uniform stretched polyester provided by the invention and the thin combined filament yarn of distortion make extension at break (E by above-mentioned of the present invention non-stretching thin mixed filament feeding yarn B) be about 15～45%, the intensity (T when (1-S/Sm) value is at least about 0.85,7% elongation 7) being at least 1g/d, preferred back flexion modulus (Mpy) is about 5～25g/d; And the flat thin combined filament yarn that preferably stretches be further characterized in that use along filament denier disperse that (DS) record along the monofilament uniformity less than about 3% (particularly less than about 2%).
Other general pictures of the present invention and will seeing below concrete the enforcement.
Figure 1A is the representational enlarged photograph of filament cross, and condensing behind this long filament is incomplete (be called here " open wide ") and this is considered to novel, and is useful with creative; Figure 1B is according to the round long filament that has a dense longitudinal void (hole) of the present invention (this requirement) the representational enlarged photograph of cross section; And Fig. 1 c also is the representational enlarged photograph of hollow filament yarn according to a modification of this invention, shows that almost completely decay in the space when the stretching false add is twisted with the fingers distortion.
Figure 1B marks (dpf) of cospinning circle long filament 1 and 2 2/ (dpf) 1To (L 1D 2/ L 2D 1) n(D 2/ D 1) 3Relation, and (L 1D 2/ L 2D 1) n(D 2/ D 1) 3Be the shower plate capillary (1) of length (L) and diameter (D) and (2) [(L/D) nD 3] 1/ [(L/D) n/ D 3] 2Reduced representation, concerning Newtonian liquid, the value of " n " is 1; With regard to the scope of polymer RLV and the processing conditions that is adopted here, the economic value of " n " is about 1.1, and in other words, n=1 is useful actual approximation).
Fig. 2 A is that destarch is shunk (S) for extension at break (E B) representative diagram, it is 0.85,0.7,0.5,0.25 that its center line 1,2,3,4,5 and 6 is represented (1-S/Sm) value respectively, 0.1 and 0 o'clock line; And the contraction of a series of yarns that curve 7 representatives are generated and the typical relation between the extension at break, for example raising is sprayed silk speed and is kept transformable other processes constant.Other processes that change can be handed over (for example dpf or polymer viscosity) then generate one " family " similar curves, and they are in fact parallel to each other.Based on ageing stability, vertical dotted line is represented about EB value scope of the preferred long filament of the present invention, i.e. yarn is directly used in 40%～90% representative, and 90%～120% represent to draw and stretch feeding yarn, and 160% be about upper limit.Suitable be suitable for the preferred long filament of the present invention who makes the stretching feeding yarn with " wide spacing " region representation, its E BValue is for about 90%～120%, and (1-S/Sm) ratio is at least about 0.25 (being lower than line 4), be suitable for the preferred long filament of the present invention who makes textile strand with " thin space " the zone represent its E BValue is 40%～90%, and ratio (1-S/Sm) is at least about 0.85 (being lower than line 1).
Fig. 2 B is that the destarch of spray directed " solid-state " long filament of silk (not being according to of the present invention) is shunk (S) to volume percent crystallinity (X v) representative diagram, the extension at break E of this long filament wherein BBe the broad range of about 160%-40%, adopt the processing conditions (for example filament denier and cross section spray silk speed, polymer LRV, quenching, capillary size (LXD) and polymer temperature) of broad range to spray silk, and X vRecord with unsteady density, and correction is % pigment.Supported a kind of like this viewpoint by the S of the yarn gained of the different Eb values of this class and the single-relation between the density (tolerance of the crystallization SIC degree that the amorphous region stress causes when being melt-out spinning): at the E of the degree of mensuration S BIn this scope of value, the degree of SIC is first fabric event, and the orientation that the amorphous region stress causes during melt-out spinning (SIO) then is second fabric event, concerning the stretching feeding yarn, corresponding to X vThe scope of value was by about 10% to 20% o'clock, and then the scope of S value is line (a-b) by about 50% to about 10%, and this is the preferred levels of SIC, and concerning directly with textile strand, corresponding to X vGreater than about 20%, then the shrinkage value scope is less than about 10%, promptly line (b-c) this be the preferred levels of SIC.
Fig. 3 A then is that Tcc is to the birefringent representative diagram in amorphous region, Tcc is the peak temperature of " cold crystallization ", record with differential scanning calorimetry (DSC) down for 20 ℃ at the programming rate per minute, and birefringence is the tolerance (represented as Frankfort and Knox) of amorphous orientation, measure its birefringent long filament for difficulty, the Tcc value is a kind of useful metrics of amorphous orientation.The Tcc value of long filament of the present invention is between 90 ℃ to 110 ℃.
Fig. 3 B is that back surrender secant modulus (Tan β) (i.e. " Mpy ") is to birefringent representative diagram.The Mpy here is by (1.20T 20-1.07T 7)/0.13 calculates, T in the formula 20Intensity when being 20% elongation, T 7Intensity when being 7% elongation.As can be seen, during greater than 2g/d, back surrender modulus (Mpy) provides birefringent a kind of useful metrics of the directed long filament of spray silk, elongate filaments and modified continuous filament.The Mpy value of preferred elongate filaments of the present invention is about 5～25g/d.
Fig. 4 A be spray silk thread speed (V) to graphic representation from the distance (X) of spinning plate surface, final (batching) speed of increasing to after the drawing-down fully of the speed (Vo) of spray silk speed when extruding (typically records at the conflux point in the downstream, Vc) here; Wherein, in apparent spray silk thread stress with the spray silk thread speed that is proportional to the necking point place (promptly approximately be proportional to ratio LRV (Tm °/Tp) 6, temperature is degree centigrade in the formula) with the product of the velocity gradient (dv/dx) at necking point place, find that here dv/dx approximately is proportional to V 2/ dpf, particularly when spray silk speed is about 2～4 kilometers/minute, and when promptly about 4～6 kilometers/minute scopes of higher spray silk speed, be proportional to pact
Figure C9311765600181
Spray silk thread temperature also to the spray silk thread apart from mapping, and find that it is along with distance evenly reduces.As a comparison, increase rapidly in constriction place spray silk thread speed.Select processing conditions to make that spray silk thread stress has development in about 0.45～0.105g/d scope apparent when drawing-down, making spray silk-oriented yarn, particularly suitable do stretching feeding yarn (DFY) is characterized in that 7% intensity (T when extending 7) value is the scope of 0.5～1g/d; And make that apparent interior spray silk thread stress is about 1.05～0.195g/d scope, to make the directed long filament of spray silk, particularly be applicable to the direct yarn (DUY) of using, the intensity (T when it is characterized in that 7% elongation 7) be the scope of about 1～1.75g/d; Spray silk thread stress is here represented with the empirical analysis expression formula in wherein apparent:
k(LRV/LRV 20.8)(T R/T P) 6(V 2/dpf)(A o/ #C) 0.7
In the formula, be about 1.345～1.385g/cm to density 3, i.e. 1.36g/cm 3, long filament, then the k value is the approximation of (0.01/SOC), SOC be polyester polymers " stress optical coefficient " (for example for the 2GT homopolymers it for about 0.7 (g/d) -1); TR is for being defined as (T M°+40 ℃) the polymer reference temperature, T in the formula M° be zero to shear (DSC) melting point polymer; Tp is a polymer melt spray silk temperature, ℃: V be expressed as kilometer/minute coiling speed; #C is the given long filament number (being capillary) of extruding area; A 0Be expressed as #C/cm 2LRV is tested polymer (lab) viscosity; And LRV 20.8For having identical zero polyester polymers corresponding of shearing " newton " melt viscosity with reference to LRV value (definition of LRV is here seen below) at 295 ℃, just as the LRV value of 2GT homopolymers be 20.8 (for example, the melt viscosity of having found 15LRV cationic-dyeable look polyester is as the capillary pressure reduction is pointed, be within the scope of about 20LRV 2GT homopolymers, therefore polymer-modified preferred of this class is about 15.5 with reference to LRV, and tests with the capillary pressure reduction determination method of standard and to record.)
Fig. 4 B is the graphic representation of the birefringence of the directed long filament of spray silk to spray silk thread stress in apparent, and its slope is called " stress optical coefficient (SOC) ", and line 1,2 should be 0.75,0.71 and 0.645 (g/d) mutually with 3 SOC value -1, and be the typical relation of the 2GT polymer found in the list of references.Therefore the mean value of SOC is about 0.7.
Intensity when Fig. 4 C is 7% elongation of spraying the directed long filament of silk is to the graphic representation of spray silk thread stress in apparent.Birefringence and T 7The relation of the intimate linearity between (they each again with respect to spray silk thread stress in apparent) makes available T 7Practicality tolerance as long filament mean molecule orientation.For its dawn number less than 1, particularly special-shaped cross section (comprising hollow fibre), birefringence is structural parameters of be difficult to measuring.
Fig. 5 is the extension at break (E of spray silk directed non-stretching nylon (I) and polyester (II) B) to spraying the representative diagram of silk speed.Between about 3.5 kilometers/minute to 6.5 kilometers/minute (with the ABCD region representation), particularly between about 4 to 6 kilometers/minute, the elongation of non-stretching polyester and Tynex is at the same order of magnitude.Raising polymer RV can increase the elongation of non-stretching nylon and (see the United States Patent (USP) 4,583,357 and 4 of Chamberlin, 646,514), use chain branching agent also can (see the United States Patent (USP) 4 of Nunning, 721,650), or use copolyamide and higher RV also can (see the EP of Knox through selecting A10411774).The elongation of non-stretching polyester can be adopted low inherent viscosity and use copolyester to improve and (see the United States Patent (USP) 4,156,071 of Knox, the United States Patent (USP) 4 of Frankfort and Knox, 134,882 and 4,195,051), also can adopt a small amount of chain branching agent of adding (to see the United States Patent (USP) 4,092,229 of MacLean, the United States Patent (USP) 4 of Knox, 156,051, and the United States Patent (USP) 4,883 of Reese, 032,4,996,740,5,034,174).The elongation of polyester filament is responsive especially to the dawn number and the shape of long filament, increases the ratio (promptly with the dawn number that reduce long filament and non-circular shape the two or the two one of all relevant) of the area of long filament to volume, and elongation is reduced.
Fig. 6 represents to relax/the remaining extensibility (RDR) of heat-set temperature TR (degree centigrade ℃) and nylon 66 stretch yarns DBetween relation, with [1000/TR+273)] to (RDR) DMapping, as people such as Boles at United States Patent (USP) 5,219, the same described in 503.Select the processing conditions among area I (ABCD) and the II (ADEF), can make the final non-stretching long filament that uses of the conduct that is suitable for strict dyeing.If stretch and the degree of heat setting press 1000/ (TR+273)＞/=[4.95-1.75 (RDR) D] this relational expression is balance, then can obtain acceptable dyeing uniformity along monofilament.This lax temperature with (RDR) DCorrelation also to can be used for the common stretching and the heat of combined filament yarn lax, or the heat of the combined filament yarn of drawn and co-blended is lax, the combined filament yarn that for example stretches altogether, for example the heat of nylon/polyester filament yarn is lax.
Method for making according to " female application " can generate non-stretching thin combined filament yarn of the present invention, and different is to make change, and feasible long filament that can two or more are dissimilar carries out common spray silk, quenching, and convergence becomes thin mixed filament bundle.For example, before interweaving and twining, but preferably before boundling and arrangement, will merge, and can generate the mixing dawn to count filament yarn from the different filament deniers of identical or different spinning head assembly and/or the endless tow of cross section ejecta.If desired, according to the present invention, by the non-stretching feeding yarn of having handled with the caustic alkali in the spinning oil, can advantageously make yarn (as Grindstaff and Reese at United States Patent (USP) 5, say described in 069,844), with hydrophily that improves them and hygroscopicity and the comfort that provides.
In fusion drawing-down process, give (amorphous) that stress caused orientation (SIO) degree of these non-stretching long filaments, reduced the peak temperature (Tcc) of cold crystallization, here, for the non-oriented yarn of non-setting, the Tcc value typically is about 135 ℃, the stress that reduces noncrystalline (amorphous) polymer chain causes orientation (SIO), and Tcc is reduced to less than 100 ℃.This peak temperature Tcc with cold crystallization in Fig. 3 A has done explanation to amorphous birefringence (defined as Frankfort and Knox) mapping.Known that nothing opens birefringence surely and increase with the increase of spray silk speed, therefore, amorphous birefringence is along with the extension at break (E of non-stretching long filament B) reduction and increase.To its elongation (E B) be 40 to about 120% scope, the Tcc value that records is at the preferred non-stretching spray silk oriented yarn of about 90 ℃～110 ℃ scope, this is considered to make even also begins the reason of further crystallization under gentle stretching condition, this also partly thought in addition also to generate the thin combined filament yarn of even stretched polyester when the cold stretch be important.
It is the result of amorphous region SIO degree that stress causes the degree of crystallization (SIC), and the density with polymeric material defines usually.Because the huge lip-deep air trap of air trap between the fine filament and fine filament is so it is difficult to measuring concerning elongated gauze; Therefore having used a kind of stress to cause the relative measurement method of crystallization, this method here is with to a given yarn extension at break (E B) the destarch degree of shrinking (S) be the basis, for given fibre-forming polymer degree of crystallinity, wish destarch contraction (S) along with the expansion of molecule (promptly along with extension at break E BReduction) and increase; Therefore, the crystallization that stress causes (SIC) defines with following formula: (1-S/Sm), Sm is when not having crystallization in the formula, and given molecule enlarges (E B) the desired maximum collapse of long filament of degree; Here Sm is defined as: Sm (%)=([(E B) Maximum-E B]/[(E B) Maximum+ 100]) 100%, (E in the formula B) MaximumBe completely without the desired maximum extension at break (E of setting " isotropism " long filament B).Concerning being about 0.56 to the polyester filament ejecta of the polymer gained of about 0.68 (is about 16 to about 23 corresponding to LRV) by its typical textiles inherent viscosity, (E B) MaximumNormal value be found to be about 550% through experiment, if maximum remaining extensibility is 6.5 words (" high speed fibre spinning ", A.Ziabicki and H.Kawaj compile, Wiley Interscience publishing house (1985), p.409), like this, here, the available skeleton symbol of Sm (%) is defined as follows: Sm, %=[(550-E B)/650] * 100% (graphic representation is in Fig. 2 A).Long filament of the present invention is described to (1-S/Sm) value greater than about 0.1 (being preferably greater than about 0.25 so that provide enough SIC for ageing stability) and elongation (E B) be about 40 to 160%.
The directed combined filament yarn of spray silk of the present invention be characterised in that occur in than polymer Tg high 5 ℃～30 ℃ shrink tension peak temperature T (ST Maximum) maximum collapse tension force (ST when (for example, be about 65 ℃ homopolymers 2GT to polymer Tg, this temperature is 70-100 ℃) Maximum) less than about 0.2g/d; And preferred non-stretching thin mixed filament feeding yarn is further characterized in that extension at break (E B) scope about 90% to about 120%, the intensity (T when 7% elongation 7) in about scope of 0.5 to about 1g/d; And (1-S/S Maximum) value is at least about 0.25; Be suitable as direct particularly preferred non-stretching filament yarn and be further characterized in that extension at break (E with yarn B) scope about 40% to about 90%, the intensity (T when 7% elongation 7) in about scope of 1 to 1.75g/d, and (1-S/Sm) value is at least about 0.85.
The dawn number of the long filament of every combined filament yarn that is obtained by identical spinnerets is capillary mass velocity W=(Vs * dpf)/9000 record with by spinneret capillary the time.It (is to be proportional to (L/D) approximately here that the W value is inversely proportional to that capillary pressure falls n/ D 3), in the formula, for Newtonian liquid, its n value is 1, and L is a capillary pipe length, and D is a capillary diameter, concerning the non-circle cross-section capillary of common short length, (L/D) n//D 3Value is taken from the metering capillary, and the latter feeds polymer and makes it to become the shape that is determined by outlet opening; Like this, (dpf) 1* [(L/D) n/ D 3] 1=(dpf) 2* [(L/D) nD 3] 2, thereby ratio (dpf) 2/ (dpf) 1]=(L/D) n/ D 3] 2For example, be about 1 and concerning the processing window that is adopted here, use to have 15 * 72 mils and 8 * 32 mils and measure spinnerets capillaceous and carry out common spray, will generate the long filament that mixes dpf, ratio (dpf) for the n value 2/ (dpf) 1Be about 476.7mm 3/ 86.5mm 2(=5.5).If spin the cross section difference but the identical long filament of dpf, it is different a little (promptly [(L/D) to need to measure diameter capillaceous n/ D 3] value is different), fall to overcome any little but different pressures of far reaching shaping outlet opening.Yet, if for example spray different long filament components from the spinning head sub-assembly that separates, and they are merged become simple mixed filament bundle, then depend on the pressure and the spray filament size of sub-assembly by the dpf of given spinning head sub-assembly gained long filament, it is simply provided by following formula: dpf=9000w/ (Vs#F), W is total spinning head sub-assembly mass flow speed (g/ minute) in the formula, and #F is long filament (F) number (#) of each spinneret assembly, and Vs is the coiling speed with rice/minute expression.
Specifically, the present invention includes but be not limited to following method for making (and by its product that makes):
(1) a spray of the present invention alignment method generates the non-stretching combined filament yarn of class spray silk oriented polyester, and wherein polyester polymers is characterised in that its relative viscosity (LRV) is about 13～about 23, zero shearing fusing point (T M°) be about 240 ℃～about 265 ℃, and glass transition temperature (Tg) is about 40 ℃～about 80 ℃; And the combined filament yarn of forming by two or more long filament components of varying cross-section and/or dawn number, the filament denier of its at least a long filament component (preferably has an average yarn spun filament dawn number (dpf) less than 1 s, like this, average stretch yarn filament denier (dpf) DLess than about 1, (dpf) DWith { (dpf) s* [(1.3)/(1+Eb/100) s) definition; Particularly, at this, non-stretching yarn average filament dawn number (dpf) sLess than 1, thereby to mixing the dawn yarn, its high denier filament (2) is about 2 to about 6 to long filament dawn ratio low but long filament (1); And it is further characterized in that: than high about 5 ℃～30 ℃ xeothermic shrink tension peak temperature T (ST of polymer glass temperature (Tg) Maximum) under, its maximum dry thermal contraction tension force ST MaximumLess than about 0.2g/d; Its (1-S/ST Maximum) value is at least about 0.1 (being preferably at least about 0.25) and shrinks to produce ageing stability; Its extension at break (E B) be about 40%～160% (the stretching feeding yarn is preferably about 90%～120%, therein, pore volume does not have actual loss during stretching), particularly (1-S/Sm) value is at least 0.85, and E BFor about 40%～90% with as the stretching feeding yarn or as the non-stretching yarn of directly using); Intensity (T during 7% elongation 7) be about 0.5～1.75g/d (the stretching feeding yarn is preferably about 0.5～1g/d, and to as directly with yarn particularly about 1～1.75); And the fracture strength (T when being normalized to 20.8LRV B) nBe at least 5g/d (preferably being at least 6g/d); Difference (DHS-S) is preferably less than+2%.
Spray silk alignment method is characterised in that:
(i) select polyester polymers so that its relative viscosity is about 13～23, zero shearing fusing point (T M°) be about 240 ℃～265 ℃, and glass transition temperature (Tg) is 40 ℃～80 ℃: make this mixture melt and be heated above apparent melting point polymer (T M) about 25 ℃～55 ℃ of a, enough promptly filter to reduce degraded; Then it is extruded the capillary by spinnerets, selecting the latter's cross section (Ac) is about 125 * 10 -6Cm 2To about 1250 * 10 -6Cm 2, and select length (L) and diameter (D RND), feasible (L/D RND) ratio be at least 1.25 and less than 6 (preferably less than 4), and select shape and/or the L capillaceous and the D value of oral pore, to generate cross section difference and/or different long filament (as previously mentioned) of dawn
(ii) the melt that ought extrude is by the discharge distance (L of spinneret capillary QD) at least about 2cm and less than approximately
Figure C9311765600241
The time, make it avoid direct cooling; Then it is chilled to and is lower than polymer transition temperature (Tg), and this thinner long filament of drawing-down to apparent spray silk thread strain is about 5.7～7.6, wherein (dpf) 1Be in the combined filament yarn than fine filament.
(iii) using low-friction surface then is that about 50cm is to about [90 in distance (Lc)
Figure C9311765600251
Distance in, will mix long yarn boundling becomes mixed filament bundle; Interweave to obtain the clustering of long filament bundle, with about 2～6 kilometers/minute winding speed combined filament yarn is twined then.
(2) as Knox and Noe at United States Patent (USP) 5,066, compound spray silk/extension described in 447 or the spray silk/extension that separates, it comprises that stretcher strain method (false add that for example stretches is twisted with the fingers the distortion and the jet drawing-down that stretches) is with preparation:
(i) flat yarn of stretching or stretching air jet texturing combined filament yarn, it has and is at least the long yarn of 5% difference and shrinks, begin temperature (Tc °) by the combined filament yarn that do not stretch at polyester polymers glass transition temperature (Tg) and primary crystallization and stretch and make, its feature also is remaining extension at break (E B) be about 15%～45%, and the intensity (T when 7% elongation 7) be at least about 1g/d; And particularly stretch flat yarn of mixed filament and air jet texturing yarn, be not at least 5% through cold stretch but non-stretching difference when directly carrying out the back heat setting with combined filament yarn being shunk as mentioned above, here, the feature of the different combined filament yarns of cold stretch also is its remaining extension at break (E B) be about 15%～55%, and the intensity during 7% elongation is at least about 1g/d.
(ii) the flat yarn of stretched polyester and the distortion thin combined filament yarn, as previously mentioned, it is made by non-stretching thin mixed filament feeding yarn of the present invention, it is characterized in that its extension at break is about 15～45%, (1-S/Sm) value is at least 0.85, intensity during 7% elongation is at least about 1g/d, and preferred back surrender modulus (Mpy) is about 5～25g/d; Preferably, the feature of the flat thin combined filament yarn of stretching here also be with measure along filament denier disperse (DS) and know along the monofilament uniformity less than about 3% (particularly less than about 2%).
(iii) preferred polyester combined filament yarn, its average yarn filament denier be less than about 1, residue extension at break (E B) be about 15%～55%, the intensity (T when (1-S/Sm) value is at least 0.85,7% elongation 7) be 1g/d at least, and preferred back surrender modulus (Mpy) is about 5～25g/d, be by carrying out cold stretch or hot-stretch through plate shape in that separate at monofilament or the compound method for making or with no latitude, but carrying out or do not carry out after-baking makes, this non-stretching combined filament yarn is as the non-stretching yarn of directly using, permanent elongation is about 40～90%, and (1-S/Sm) value is at least about 0.85; By selecting spray silk orientation mixed filament feeding yarn of the present invention, the intensity (T during its 7% elongation 7) be about 1～1.75g/d, wherein all long filaments are characterised in that the foregoing non-stretching direct combined filament yarn of using of the present invention; Preferably, this flat thin combined filament yarn that stretches be further characterized in that by disperse along filament denier that (DS) record along the monofilament uniformity less than about 3% (particularly less than about 2%)
Thin combined filament yarn of air jet texturing and the even thin combined filament yarn of stretcher strain (iv) evenly stretch; Wherein this method for making comprises and makes evenly stretch air jet texturing or stretching false add of the non-stretching mixed filament feeding yarn that makes with aforementioned spray silk alignment method twist with the fingers distortion, and to generate even stretching varicosity combined filament yarn, the latter is characterised in that remaining extension at break (E B) be about 15%～45%, the intensity (T when (1-S/Sm) value is at least 0.85,7% elongation 7) be at least about 1g/d, and preferred back surrender modulus (Mpy) is about 5～25g/d.
(the varicosity combined filament yarn v) stretches, it is when lax stretching flat combined filament yarn of the present invention of heat or stretching air jet texturing combined filament yarn, different long filaments shrink and are at least 5%, it is directly to carry out cold stretch with yarn by aforementioned non-stretching mixed filament of the present invention but do not carry out after-baking and make, generate even stretching varicosity combined filament yarn thus, the latter is characterised in that its remaining extension at break (E B) be about 15～55%, the (intensity (T when 1～S/Sm) value is at least about 0.85,7% elongation 7) be at least about 1g/d, and preferred back surrender modulus (Mpy) is about 5～25g/d.
(the varicosity combined filament yarn vi) stretches, it is when lax stretching flat combined filament yarn of the present invention of heat or stretching air jet texturing combined filament yarn, different long filaments are punctured at least 5%, be to stretch by non-stretching combined filament yarn of the present invention but do not carry out after-baking and make, as previously mentioned, stretching is to carry out Tg to Tc ° scope with an extensibility, and to generate even stretching varicosity combined filament yarn, the latter is characterised in that remaining extension at break (E B) be about 15%～45%, the intensity (T when (1-S/Sm) value is at least 0.85,7% elongation 7) be at least 1g/d, then surrender the about 5～25g/d of modulus (Mpy).
(shrink tension (the ST that vii) is used for the tight structure fabric Maximum) greater than the stretch yarn of about 0.25g/d.So that make yarn in dyeing and arrangement process, overcome the tube bank between yarn-yarn in fabric, method is to begin temperature (Tc °) non-stretching combined filament yarn is stretched being higher than glass transition temperature (Tg) and low primary crystallization, wherein after-baking is adjusted to produce required contraction S and the balance between the shrink tension ST.
The feature of thin dawn prolate silk of the present invention also is (to claim the dawn number to disperse here, DS) less than about 4% (preferably less than 3%, especially preferably less than 2%) along yarn dawn number variation; The thin combined filament yarn of even dawn number is applicable to be needed among strict dyeing (configuration) inhomogeneity fabric; The form factor (SF) of non-round long filament (adding is in order to improve sense of touch, impression and comfort sense) is at least 1.25, and here, to the round long filament of suitable cross section, form factor is defined as the long filament circularity (P that records M) circularity (P to calculating RND) ratio.The feature of long filament of the present invention also is good mechanical property, and the fracture strength when it is normalized to 20.8 polymer LRV is 5g/d at least.
Detection method
Here a lot of polyester parameters mentioned and assay method are at the USP4 of Knox, 156,071, the USP5 of Knox and Noe, 066,447 and Frankfort and Knox 4,434, therefore done sufficient discussion and description in 882, they all are cited as a reference here, remake here that to go through to be unnecessary.Here, for clear, writing " S " shunk in destarch (write as S sometimes 1, or in table, write as S1); In all embodiments, the differential of spraying gauze is altogether shunk (DHS-S) always less than+2; T B(being Tb sometimes in table) based on the intensity at the dawn in when fracture (, based on stretching the dawn writing Mpy), Tb is defined as common weaving intensity and remaining extensibility RDR (=1+E B/ 100) product, and normalized (T B) nBe defined as [(T B) (20.8/LRV) 0.75(1-% flatting agent/100) -4], combined filament yarn of the present invention is characterised in that T BValue is at least about 5g/d after being normalized to 20.8 polymer LRV, preferably is at least about 6g/d.
Available common DSG assay glass transition temperature of polymer Tg, primary crystallization begins the temperature T c of temperature (Tc °) and crystallization maximal rate MaximumValue; But for example the polyester, these values also can be sheared fusing point T by zero of polymer concerning one group of given compound M° (representing) with Kelvin degree, adopt the method for R.F.Boyer to estimate [see " in the polymer amorphous state in order ", S.E.Reinath, R.L.Miller, J.K.Riecke compiles, Plenum Press company (New York), 1987]; In the formula, Tg=0.65T M°: Tc °=0.75T M°; And Tc Maximum=0.85T M°; Temperature all in the formula are all represented with Kelvin degree.
Method for making of the present invention and product are described with the following example, but are not limited to these embodiment, and have done detailed summary in table.
Embodiment A
In embodiment A, to count long filament and higher Denier long filament than the low dawn carries out cospinning and makes the combined filament yarn (United States Patent (USP) 4 of Knox for example, 156,071 low contraction (crystallization shape) spray silk oriented yarn, and/or the height of the United States Patent (USP) 3,772,872 of Piazza and Reese shrinks (amorphous) spray silk orientation POY long filament, shrink (for example back varicosityization in fabric) so that may produce to mix, for example when low shrinkage continuous yarn mixes with high shrinkage continuous yarn).
This class height and low dpf long filament can be from the spinneret sub-assembly hole ejections that separates, merge then and generate the simple dpf of mixing long filament bundle, but, wherein select size capillaceous (L and D) and number capillaceous to produce different mass velocities preferably from the ejection of list-spinneret sub-assembly hole; For example select capillary make the spray filament length silk dawn ratio [(dpf) 2/ (dpf) 1] approximate [(L 1D 2/ L 2D 1] n* [(D 2/ D 1) 3], here 1 and 2 the expression the different dawn long filament; To newton's polymer melt n=I (and here, to used polymer and processing conditions, experiment finds that the mean value of " n " is 1.1); And the average yarn filament denier that records be defined as (dpf) average=[( #1dpf 1+ #2dpf 2)/( #1+ #2)].
Embodiment 1-6 sprays silk and produces this yarn for about 290 ℃ at polymer temperature (Tp) with the 2GT homopolymers of nominal 21.2LRV; Delay the radially quencher of pipe and be that the air at room temperature of 40-50mpm carries out quenching with one 2.5 inches (2.75cm) is housed with speed; With metering upper oil-pan thread-carrier yarn is occurred at 109cm place, distance spinnerets surface then, then with Table I, II, speed pointed among the III is batched, and its nominal dawn number fades to about 239 200 filament yarns by about 127 to generate as noted." ejecta DPF mean value " by divided by 200 nominal dawn number, and " DPF ratio " is the high dpf that measures to the ratio (it is quite near nominal dpf ratio 3.54 as described below) of the low dpf that measures.This 200 long filament be contain 24 high dpf long filaments (2) and 176 low dpf long filaments (1) spin the material yarn.To embodiment 1-3, normal (dpf) 2/ (dpf) 1It is about 3.54 that ratio is respectively, and this is the result who adopts the different size spinneret capillary; This is that 24 length (L) are that 12.5 mils (0.318 mm) and diameter (D) are the capillary of 39 mils (0.975mm), and 176 length (L) are that 36 mils (0.914mm) and diameter (D) are the capillary of 9 mils (0.229mm), fall ratio with regard to producing 3.54 pressure like this; That is, (dpf) 2/ (dpf) 1=[(L 1D 2/ L 2D 1] nX[D 2/ D 1) 3], " n " in the formula is 1 to Newtonian liquid, and to polymer LRV and used processing conditions, experiment finds that its value is 1.1.The average yarn dawn number of measuring= #1 (dpf) 1+ #2 (dpf) 2= #1 (dpf) 1+ #2{[(dpf) 2/ (dpf) 1] (dpf) 2)= #1 (dpf) 1+ 3.54[ #2 (dpf) 1]=[ #1+3.54 ( #2)] (dpf) 1=[24+3.54 (176) is (dpf) 1, in the formula (dpf) 1=average yarn dawn number/[24+3.54 (176)] that record, and (dpf) 2=3.54 (dpf) 1
In embodiment 1, high dpf long filament (2) is ejected (because give speech not long ago, more useful than low dpf long filament through the high dpf long filament of more quenching) from being positioned at the outer shroud how the ring capillaries are arranged.In Fig. 2, the capillary (2) of making high dpf long filament is positioned at the centre of arranging, and there, Pen Chu long filament (2) can tend to " moving " naturally and assemble when quenching here.At embodiment 3, prepare the capillary that the capillary of high dpf long filament (2) arranges by many rings and arrange symmetrically.The data of embodiment 1～3 and include a hurdle " stretching DPF mean value " in Table I～III, it is calculated divided by 200 by " the stretching thing dawn number " that be documented among the embodiment 4-6 and provide in Table IV-IV.
We are surprised to find in practice, and symmetry arrangement among the embodiment 3 produces best amount and counts uniformity, and that the skin among the embodiment 1 is arranged is the poorest.The arrange fracture strength (T of (1) of symmetry arrangement (3) and outer shroud B) in fact equal, (2) are obviously the poorest and interior ring is arranged.
In embodiment 4-6, with the yarn of ejection of embodiment 1-3, at 400mpm, adopting 180 ℃ stretching and careful drawn to the permanent elongation of setting temperature is between 25%～45% and the average yarn long filament of its nominal (dpf) respectively DLess than 1dpf.Stretch yarn for example other uniformity of identical relative level and fracture strength have been observed to the spray silk feeding yarn among the embodiment 1-3, optimum long filament is arranged and will be depended on the number of long filament, dpf ratio, and required along filament denier uniformity (DS) and tensile strength (as here with T BRecord) balance.
In down a series of, be not that long filament is mixed, but make and the separately yarn bundle of stretch high dpf and low dpf to obtain the data of long filament character and behavior, people will understand that this long filament can be mixed together.
Embodiment 7
From the spinning head sub-assembly that separates, use 15 * 60 and 9 * 36 mil capillaries respectively, spray the independent bundle of 50 high dpf and 200 low dpf long filaments; And separately winding (aggregation of data is in Table VII).The low dpf long filament of gained has higher pull resistance (modulus T than high dpf long filament 7, T B) and low extension at break (E B).Experience based on drawn and stretcher strain, we select 4 to 1 dpf than being about 2 higher dpf long filament so that produce the dpf that stretches that is used for thin fabric, to avoid producing " flash of light " from the difference reflection from the different big or small filament surfaces of differently curved part.4 to 1 dpf ratio makes the E about 20%～40% BValue produces difference, but E BThe less difference of value generally can be preferred to mechanical performance and the uniformity that generates optimum stretch yarn.
Embodiment 8
Stretch to obtain 1.4X, the extensibility series of 1.5X and 1.6X with 400 meters/minute at about 180 ℃ draft temperature and about 180 ℃ setting temperature.It is about 10～20% that the difference of tensile elongation is generally, and the long filament of higher dpf has higher elongation.Stretch yarn is summarized in the Table VIII.
Embodiment 9
With 172 dawn 200 long filaments and the 172 dawn 50 long filament bundles of embodiment 7,, use the beginning temperature to be (25 ℃ of room temperatures with 400mpm and 1.64 stretching ratios, the the 1st and 2) fixed head, stretch, it (is the maximum percent crystallization in massecuite temperature T c of 2GT polyester that draft temperature rises to 180 ℃ by room temperature (cold stretch) Maximum), X is pointed as Table I, shrinks and reduces along with rising, and particularly being higher than about 120 ℃ is that primary crystallization begins temperature T c °, so reduce to about 2% 130 ℃ of differentials contractions.This shows, can produce to have stretched at higher draft temperature and mix the dawn and count filament yarn, by being of same mixture dawn number feeding material gained flat yarn (be non-varicosity, have similar contraction because mix the dpf long filament).We often produce when low draft temperature stretches can self-expanding mixing contraction stretching yarn.
Embodiment 10
In embodiment 10 for the 1-11 item, the heat setting plate temperature is room temperature (25 ℃), extensibility with 400mpm and 1.64X, to being that 2.45 long filament and 176 average dpf are that the common 200-200 spray gauze that 0.78 long filament is formed carries out drawn by 24 average dpf, and draft temperature is risen to 180 ℃ by 25 ℃.Along with the rising of draft temperature, shrink S 1Reducing to 5.8% by 47.2%, is to shrink S after 114 ℃ at draft temperature 1Reduction reduced, this has supported the result of embodiment 9.At the 12-13 item,, the 127 dawn feeding yarns of being made up of 24 1.65dpf long filaments and 176 0.5dpf long filaments are stretched with the 1.4X extensibility.The 12nd is cold drawn and does not carry out after-baking (being that fixed head maintains 25 ℃ of room temperatures).In the 13rd, 127 dawn yarns are stretched and formalize at 180 ℃ at 180 ℃, obtain 5.9 contraction S 1, then be 28.4 in the 12nd.This has illustrated selects the set-stretching temperature can control the degree of contraction.The data of embodiment 10 are summarized in Table X.
Embodiment 11
127-200 and 159-200 (dawn is counted long filament) yarn with embodiment 3 (24 high dawn numbers and 174 low dawn numbers), with 1.4X and 1.6X extensibility, in 200 meters/minute air jet texturings that stretch, the temperature that stretches and formalize fades to 180 ℃ by room temperature (being that heater is opened), can prepare it and shrink high extremely about 40% the stretching air jet texturing yarn less than 2%, this provides a kind of possibility of mixing pulled down yarn from identical feeding feedstock production.Data are summarised in Table X I.
Embodiment 12
Adopt 1/7/1BB disc type mixing bunker (PU dish-type), will be as common 200 dawn-200 long filaments (the 5-8 item in the Table III) of spray gauze, lead with 1.506 extensibilitys and 1.707D/Y,, on Barmag FK6-900K, twist with the fingers distortion in 180 ℃ of false adds that stretch with 450 meters/minute.Stretch yarn dawn number is 136.7 (0.68dpf) when 40.6% elongation, and its intensity is 3.66g/d, and modulus is 20.7g/d.Destarch is punctured into 5.6%, and Leesona reeled yarn contraction (tolerance of textured yarn bulk density) is 23.7%, and this mixes the dpf filament yarn and counts the higher bulk density of filament yarn generation than 100% little dawn, and depends on final fracture elongation, the melange yarn that can make.
Embodiment 13
With the stretching feeding yarn of embodiment 12, at 115 ℃ of draft temperatures (being about cold crystallization temperature Tcc), adopt 75 ℃ and give draft temperature and extensibility 1.64X, carry out drawn at 4000 meters/minute, produce 10% destarch and shrink.This dawn number of stretch yarn in 37.5% when elongation be 124.8 (average filaments (dpf) DBe 0.62), intensity is 3.98g/d, its modulus is 66.8g/d, T 7Be 2.47g/d.The dawn number that this thin dawn is counted yarn is separated into 2.2%, and slow Uster is 0.6%, and this makes these be suitable for the final use of strict dyeing.
Embodiment 14
Shrink S with 50 1Be 21% thereby (1-S 1/ Sm) ratio is 0.67 1.83 denier filaments, and 200 are shunk S 1Be 5.2% thereby (1-S 1/ Sm) ratio is that 0.92 0.46 denier filament (referring to the 17th and 18 of Table VIII) carries out common spray with 2473mpm, the mixing pulled down yarn that manufacturing can the back distortion.Hate 2.28 denier filaments and 200 0.57 denier filaments (in the Table VII the 13rd and 14) to carry out common spray with 50 with 2473mpm, make be punctured into 7.8% with 39.4% similar can the back textured yarn.When spray silk speed was low, the contraction of low dpf long filament increased, and this has reduced the difference in shrinkage between the low and high dpf long filament and has produced excessive weaving loss.Preferably, the contraction of low shrinkage continuous yarn that is to say (1-S less than about 10% 1/ Sm) value is at least approximately 0.85, is explained orally as the 13rd and 17 of Table VII, and this produces to mix and shrinks and reduced the fabric loss, has enough shrink tensions to overcome the tube bank in the fabric if shrink component, and this equals high contraction of shrinking component at the most.For reducing the fabric loss in the fabric body when the varicosity of back, draw through the time, be enough to enlarge shrink and the temperature of varicosityization under carry out excessive feeding, then varicosityization can take place; Shrink so that varicosityization is enlarged but preferably stay some residues, this has helped to sew up the difference randomization of tightness, and has improved the configuration uniformity.The residual contraction of about 3-4% is for being enough through knitting and light weight fabric.
Embodiment 15
At polymer temperature (Tg) is under about 290 ℃, 2GT homopolymers by nominal 21.2LRY sprays 20D (mixing) filament yarn, carry out quenching with the radially quencher of delaying pipe that 1.7 inches (4.32cm) are housed and speed for the air at room temperature of about 30-50mpm, long filament is being assembled apart from the about 109cm of spray filament surface place with metering upper oil-pan thread-carrier then, stretch again afterwards, generate nominal dawn number and fade to 200 filament yarns at 220 dawn by 124 dawn, wherein this 200 filament yarn is made up of 24 non-circle cross-section long filaments of high dpf and 176 low dpf circular section long filaments.The capillary pipe length (L) that is used to generate the spinneret capillary of 176 long lines of low dpf is 36 mils (0.914mm), and diameter (D) is 9 mils (0.229 mm).Selection is used to generate the spinneret capillary of 24 high dpf long filaments to form required fiber cross section; The yarn that to make high dpf component wherein be following cross section: 1) triangle strip, 2) octagonal band, 3) the polygonal band, 4) hollow yarn.For obtaining that dpf leads is 3.5: 1, uses that 24 capillary pipe lengths (L) are arranged is that 56 mils (1.42mm) and diameter (D) are that the metering plate capillaceous of 90 mils (2.29mm) makes polymer generate non-circular capillary with control.To low dpf component, using its capillary pipe length (L) is that 90 mils (2.29mm) and diameter (D) are the low pressure drop metering plates of 40 mils (1.02mm), and low like this dpf polymer flow speed has in fact been controlled by spinneret capillary.
This method for making is used to generate by mixing the dawn and counts long filament and mix the yarn that the shape of cross section long filament is formed, this has just reduced low dawn number and high dawn and has counted difference between the elongation of long filament, thereby (promptly can be stretched to the component of extending for about 20%～40% altogether all can generate to have improved common stretching, count uniformity to improve mechanical performance and dawn), and generate and lowly to shrink high denier filament, thereby make the combined filament yarn that is suitable for doing directly with flat yarn.
This invention makes itself to contain a lot of changes and further improve this point and will become clear, during particularly along with these or other technology progress, for example, can use the stretching wrapping machine of any kind; The after-baking if desired of feeding yarn and/or stretch yarn, can use any heater (thermal conductance silk for example, hot-air and/or steam jet, by heat pipe, heating using microwave, etc.); Housekeeping operation can be adopted common roll-type maneuver, and preferred here metering arrangement small articles operator, and arrangement can carry out in several steps is for example in spray silk process at the stretching prefinishing or after stretching but put in order before twining; Can use heat or not hot entanglement air-jet method make to interweave and strengthened, and can be in some steps for example in spray silk process and the enhancing that interweaves in the drawing process, and can use other equipment for example on the weft yarn sheet of yarn, to use the entanglement reed.In addition, if desired, can be from fan-shaped spinneret capillary hole, coalescent adding hollow filament is as a kind of (or multiple) long filament component of combined filament yarn of the present invention after the warp, the light fabric that has big bulkiness with generation to be improving the drapability of fabric, and as awaiting the reply jointly of people such as Aneja application apply for No._ _ _ _ _ disclosed in (DD-4555H), also produce different cross sections at least, being disclosed in here of this application also is cited as a reference.
The low high DPF D.S. of the DPF Ten. Eb Ib Sm of Table I item number ejecta spray silk ejecta DPF DPF is stretching thing
Dawn is counted (g/d) (%) (g/d) (%) DPF mean value of speed average ratio (%)
(mpm)?1 239 2195 1.20 3.44 0.93 3.21 1.67 2.36 145.5 5.79 62.23 0.68?2 239 2195 1.20 3.62 0.92 3.33 3.84 2.37 156.9 6.09 60.48 0.60 3 239 2195 1.20 3.55 0.92 3.28 1.45 2.35 146.5 5.79 62.07 0.63?4 212 2469 1.06 3.70 0.81 2.99 2.07 2.38 129.7 5.47 64.66 0.60?5 199 2195 1.00 3.43 0.78 2.67 1.83 2.53 139.1 6.05 63.21 0.54?6 199 2195 1.00 3.77 0.75 2.84 1.45 2.60 150.3 6.51 61.49 0.52?7 199 2195 1.00 3.27 0.79 2.58 1.88 2.11 132.7 4.91 64.20 0.56?8 199 2195 1.00 3.43 0.78 2.67 1.59 2.51 139.9 6.02 63.10 0.54?9 191 2743 0.96 3.41 0.75 2.55 2.12 2.75 125.2 6.19 65.35 0.5510 180 2195 0.90 3.51 0.70 2.45 1.82 2.58 134.6 6.05 63.90 0.5011 177 2469 0.89 3.40 0.69 2.36 2.11 2.62 123.7 5.86 65.58 0.5112 159 2743 0.80 1.91 2.45 113.0 5.22 67.23 0.4913 159 2195 0.80 3.30 0.63 2.08 1.43 2.76 134.1 6.46 63.99 0.4414 159 2195 0.80 3.36 0.63 2.10 1.91 2.58 126.7 5.85 65.12 0.4615 159 2195 0.80 3.46 0.62 2.15 1.86 2.58 122.1 5.73 65.83 0.4716 142 2469 0.71 3.27 0.56 1.84 1.42 2.70 124.9 6.09 65.40 0.4117 127 2743 0.64 3.55 0.49 1.74 2.23 2.71 101.4 5.46 69.02 0.41
The low high DPF D.S. of the DPF Ten. Eb Tb Sm of Table II item number ejecta spray silk ejecta DPF DPF is stretching thing
Dawn is counted (g/d) (g/d) (g/d) (%) DPF mean value of speed average ratio (%)
(mpm) 1 239 2195 1.20 3.82 0.87 3.34 2.19 2.15 157.6 5.54 60.37 0.60 2 239 2195 1.20 3.23 0.93 2.99 3.08 2.09 153.2 5.29 61.05 0.61 3 239 2195 1.20 3.49 0.90 3.15 1.97 2.09 151.2 5.25 61.35 0.62 4 212 2469 1.06 3.83 0.77 2.97 2.20 2.14 137.7 5.09 63.43 0.58 5 199 2195 1.00 3.62 0.74 2.69 1.81 2.01 136.8 4.76 63.57 0.55 6 199 2195 1.00 3.63 0.74 2.69 2.54 1.91 141.7 4.62 62.82 0.54 7 199 2195 1.00 3.15 0.78 2.45 1.84 2.24 133.8 5.24 64.02 0.55 8 199 2195 1.00 3.27 0.77 2.51 2.22 1.97 126.2 4.46 65.21 0.57 9 191 2743 0.96 3.52 0.72 2.53 3.07 2.41 122.6 5.36 65.76 0.56?10 180 2195 0.90 3.50 0.68 2.38 2.14 2.08 125.7 4.69 65.28 0.52?11 177 2469 0.89 3.11 0.69 2.16 2.19 2.18 124.6 4.90 65.45 0.51?12 159 2743 0.80 3.85 0.58 2.23 1.60 2.72 117.4 5.91 66.56 0.48?13 159 2195 0.80 3.29 0.61 2.01 2.07 2.47 135.4 5.81 63.79 0.44?14 159 2195 0.80 3.72 0.59 2.19 2.33 2.22 125.5 5.01 65.31 0.46?15 159 2195 0.80 3.75 0.59 2.19 1.45 2.30 121.2 5.09 65.97 0.47?16 142 2469 0.71 3.63 0.53 1.92 2.15 2.19 105.8 4.51 68.34 0.45?17 127 2743 0.64 0.64 0.47 1.72 1.85 2.09 89.9 3.97 70.78 0.43
The low high DPF D.S. of the DPF Ten. Eb Tb T of Table III item number ejecta spray silk ejecta DPF DPF 7T 20S 1Sm 1-S 1/ Sm is stretching thing
Dawn is counted (g/d) (g/d) (g/d) (g/d) (g/d) (%) (%) DPF mean value of speed average ratio (%)
(mpm)
239 2195 1.20 3.91 0.89 3.46 1.62 2.48 154.4 6.31 0.61 0.57 58.2 60.87 0.04 0.61 2 239 2195 1.20 3.35 0.93 3.12 2.10 2.41 156.9 6.19 0.62 0.56 56.8 60.48 0.06 0.60 3 239 2195 1.20 3.85 0.89 3.43 1.58 2.35 148.6 5.84 0.61 0.56 57.4 61.75 0.07 0.62 4 212 2469 1.06 3.47 0.82 2.84 1.57 2.54 134.6 5.96 0.64 0.60 55.6 63.91 0.13 0.59 5 199 2195 1.00 3.55 0.76 2.70 1.56 2.56 144.9 6.27 0.63 0.61 52.1 62.33 0.16 0.53 6 199 2195 1.00 3.74 0.75 2.80 1.59 2.61 149.5 6.51 0.59 0.53 55.3 61.62 0.10 0.52 7 199 2195 1.00 3.31 0.78 2.58 1.58 2.55 140.3 6.13 0.62 0.61 54.5 63.03 0.14 0.54 8 199 2195 1.00 3.49 0.77 2.67 1.75 2.47 138.6 5.89 0.62 0.61 51.6 63.30 0.18 0.54 9 191 2743 0.96 3.40 0.74 2.52 1.72 2.71 123.9 6.07 0.68 0.69 45.3 65.55 0.31 0.55?10 180 2195 0.90 3.67 0.68 2.50 1.88 2.46 128.8 5.63 0.59 0.61 52.8 64.80 0.21 0.51?11 177 2469 0.89 3.22 0.70 2.25 1.40 2.61 123.7 5.84 0.66 0.65 46.6 65.58 0.29 0.51?12 159 2743 0.80 3.83 0.59 2.27 2.09 2.44 115.0 5.25 0.79 0.86 53.1 66.93 0.21 0.48?13 159 2195 0.80 3.19 0.63 2.01 1.52 2.72 133.4 6.35 0.63 0.64 50.7 64.09 0.21 0.44?14 159 2195 0.80 3.72 0.60 2.23 1.65 2.62 137.0 6.21 0.63 0.63 53.4 63.54 0.16 0.44?15 159 2195 0.80 3.45 0.61 2.12 1.60 2.60 127.2 5.91 0.66 0.65 50.5 65.04 0.22 0.45?16 142 2469 0.71 3.40 0.55 1.87 1.64 2.42 111.1 5.11 0.73 0.77 34.0 67.52 0.50 0.44?17 127 2743 0.64 3.32 0.50 1.65 1.28 2.68 101.4 5.40 0.85 0.97 11.7 69.01 0.83 0.41
The Table IV item number feeding thing modulus in tension T that stretched 7Ten. Eb Tb WTB S 1D.S.
( g/d ) ( g/d ) ( g/d ) ( ％ ) ( g/d ) ( g/d ) ( ％ ) ( ％ ) 1 199 126.6 1.60 79.1 2.45 4.17 34.70 5.62 136.0 5.30 2.22 2 199 125.4 1.62 80.2 2.59 4.11 31.21 5.39 120.6 4.95 2.23 3 199 124.0 1.64 79.7 2.71 4.23 31.50 5.56 125.0 5.10 1.92 4 199 126.9 1.60 69.5 2.39 4.11 34.68 5.54 132.2 5 199 127.1 1.60 70.6 2.53 4.14 33.68 5.53 131.9 6 177 120.6 1.50 78.0 2.52 4.15 37.52 5.71 141.0 7 159 115.8 1.40 77.1 2.27 4.07 45.74 5.93 158.7 8 239 151.9 1.60 72.5 2.13 3.83 36.10 5.21 152.6 5.60 2.67 9 239 150.5 1.62 74.3 2.22 3.86 34.50 5.19 146.9 5.30 2.3510 239 148.8 1.64 72.4 2.28 3.79 30.60 4.95 127.0 5.30 2.5011 239 152.4 1.60 60.4 1.93 3.54 36.18 4.82 140.612 239 152.8 1.60 63.4 2.09 3.72 34.49 5.00 141.513 212 144.9 1.50 72.6 2.11 3.95 43.50 5.67 180.914 191 139.8 1.40 70.2 2.07 3.73 42.48 5.31 161.815 159 101.5 1.60 73.6 3.00 4.56 35.04 6.16 124.416 159 101.7 1.60 72.7 2.86 4.45 34.61 5.99 118.817 159 101.7 1.60 76.8 3.03 4.42 31.41 5.81 108.818 142 96.3 1.50 88.0 2.94 4.27 34.42 5.74 109.819 127 93.0 1.40 88.5 2.79 3.71 31.11 4.86 87.120 180 114.1 1.60 82.8 2.76 4.28 33.40 5.71 124.0 5.90 1.3321 180 113.0 1.62 83.6 2.86 4.34 32.03 5.73 119.4 6.10 1.6222 180 111.6 1.64 85.0 3.01 4.40 31.10 5.77 117.5 5.75 1.74
The Table V item number feeding thing modulus in tension T that stretched 7Ten. Eb Tb WTB
( g/d ) ( g/d ) ( g/d ) ( ％ ) ( g/d ) ( g/d ) 1 199 127.0 1.6 56.3 2.25 3.42 31.78 4.51 104.3 2 199 126.8 1.6 60.1 2.21 3.42 34.61 4.60 114.3 3 199 126.8 1.6 57.3 2.30 3.45 32.24 4.56 107.4 4 177 120.3 1.5 62.3 2.27 3.48 36.37 4.75 116.9 5 159 115.9 1.4 72.3 2.40 3.85 40.01 5.39 135.8 6 239 152.4 1.6 54.5 2.01 3.11 33.11 4.14 118.9 7 239 152.2 1.6 54.1 1.91 2.95 31.71 3.89 107.6 8 239 152.4 1.6 57.1 2.00 3.19 24.51 3.97 126.0 9 212 144.7 1.5 59.9 1.98 3.12 34.71 4.20 117.610 191 139.5 1.4 59.8 1.92 3.12 39.25 4.34 127.011 159 101.5 1.6 60.9 2.65 3.81 31.33 5.00 93.112 159 101.3 1.6 57.7 2.52 3.72 32.20 4.92 92.513 159 101.5 1.6 61.7 2.66 3.73 29.38 4.83 85.714 142 96.3 1.5 59.5 2.57 3.78 34.48 5.08 96.315 127 92.7 1.4 60.7 2.49 3.53 36.27 4.81 93.3
The Table VI item number feeding thing modulus in tension T that stretched 7Ten. Eb Tb WTB S 1D.S.
( g/d ) ( g/d ) ( g/d ) ( ％ ) ( g/d ) ( g/d ) ( ％ ) ( ％ ) 1 199 127.2 1.60 77.6 2.46 4.06 34.29 5.45 131.8 5.70 1.74 2 199 126.1 1.62 76.3 2.50 4.11 34.01 5.51 131.1 7.85 1.88 3 199 124.4 1.64 73.5 2.62 4.17 32.07 5.51 124.6 5.55 1.65 4 199 126.7 1.60 65.7 2.31 4.01 35.65 5.44 132.8 5 199 126.9 1.60 68.1 2.49 3.95 31.27 5.19 116.4 6 177 120.3 1.50 71.4 2.51 4.16 39.28 5.79 148.1 7 159 116.2 1.40 64.4 2.19 3.35 37.45 4.60 111.6 8 239 152.7 1.60 68.0 2.07 3.69 36.90 5.05 151.6 5.65 2.19 9 239 151.2 1.62 68.7 2.18 3.72 34.20 4.99 140.7 5.85 2.2110 239 149.5 1.64 70.5 2.24 3.82 33.50 5.10 141.2 5.60 2.3011 239 152.4 1.60 61.9 1.98 3.59 37.56 4.94 149.812 239 152.6 1.60 60.1 2.01 3.70 38.90 5.14 159.213 212 144.6 1.50 62.7 2.11 3.87 41.66 5.48 168.714 191 139.4 1.40 69.7 2.12 3.93 45.19 5.71 177.815 159 101.2 1.60 68.9 2.97 4.43 34.31 5.95 118.616 159 101.3 1.60 68.4 2.81 4.45 37.06 6.10 127.017 159 101.2 1.60 80.1 3.05 4.33 30.20 5.64 102.018 142 96.0 1.50 76.9 2.91 4.24 36.00 5.77 114.219 127 92.6 1.40 84.6 2.78 3.84 34.87 5.18 98.320 180 114.6 1.60 80.0 2.69 4.19 33.14 5.58 120.4 5.80 1.7121 180 113.5 1.62 76.9 2.78 4.23 32.40 5.60 118.3 4.30 1.5322 180 112.2 1.64 77.5 2.93 4.33 31.50 5.69 117.0 5.70 1.54
Table VII item number ejecta #fils DPF spray silk D.S. Ten. Eb Tb T 7T 20S 1Sm 1-S 1/ Sm
Dawn count speed (%) (g/d) (%) (g/d) (g/d) (g/d) (%) (%)
(mpm)?1 172.0 200 0.86 2195 1.86 2.51 143.4 6.11 0.64 0.59 49.9 62.6 0.20?2 172.0 50 3.44 2195 1.64 2.10 186.7 6.02 0.57 0.52 56.4 55.9 -0.01?3 153.0 200 0.77 2469 1.74 2.81 128.2 6.41 0.68 0.64 32.7 64.9 0.50?4 153.0 50 3.06 2469 1.80 2.51 166.8 6.70 0.59 0.56 56.3 58.9 0.04?5 143.0 200 0.72 2195 1.70 2.52 121.0 5.57 0.64 0.62 43.3 66.0 0.34?6 143.0 50 2.86 2195 1.43 2.18 169.2 5.87 0.57 0.54 55.1 58.6 0.06?7 138.0 200 0.69 2743 1.61 2.67 114.0 5.71 0.75 0.80 14.4 67.1 0.79?8 138.0 50 2.76 2743 1.58 2.52 142.4 6.11 0.63 0.59 50.2 62.7 0.20?9 127.0 200 0.64 2469 2.06 2.86 121.1 6.32 0.72 0.74 22.6 66.0 0.6610 127.0 50 2.54 2469 1.34 2.59 153.6 6.57 0.63 0.59 51.1 61.0 0.1611 115.0 200 0.58 2195 2.24 2.72 121.9 6.04 0.71 0.69 31.8 65.9 0.5212 115.0 50 2.30 2195 1.34 2.49 162.9 6.54 0.60 0.57 56.1 59.6 0.0613 114.0 200 0.57 2743 1.35 2.86 107.9 5.95 0.83 0.93 7.8 68.0 0.8914 114.0 50 2.28 2743 1.50 2.78 140.4 6.68 0.63 0.59 39.4 63.0 0.3715 102.0 200 0.51 2469 1.55 2.57 103.3 5.22 0.80 0.86 12.5 68.7 0.8216 102.0 50 2.04 2469 1.24 2.35 133.3 5.19 0.64 0.59 44.9 64.1 0.3017 91.7 200 0.46 2743 1.79 2.76 104.9 5.66 0.95 1.10 5.2 68.5 0.9218 91.7 50 1.83 2743 1.18 2.85 135.2 6.70 0.69 0.65 21.0 63.8 0.67
The Table VIII item number ejecta long filament extensibility modulus T that number stretches 7Ten. Eb Tb WTB
( g/d ) ( g/d ) ( g/d ) ( ％ ) ( g/d ) ( g/d ) 1 172.0 200 108.1 1.6 85.1 2.73 4.40 34.51 5.92 127.19 2 172.0 50 108.1 1.6 59.7 1.31 2.60 42.50 3.71 84.71 3 153.0 200 102.5 1.5 88.4 2.77 4.24 34.55 5.70 114.85 4 153.0 50 102.8 1.5 1.49 3.53 55.81 5.50 137.94 5 143.0 200 89.8 1.6 88.2 3.19 4.59 28.03 5.88 87.72 6 143.0 50 89.8 1.6 57.8 1.60 3.39 45.62 4.94 96.28 7 138.0 200 98.9 1.4 81.0 2.58 4.10 40.41 5.76 124.20 8 138.0 50 99.2 1.4 62.6 1.51 3.68 57.60 5.80 141.16 9 127.0 200 85.3 1.5 91.8 3.08 4.20 27.42 5.35 76.8210 127.0 50 85.5 1.5 66.3 1.76 3.95 52.36 6.02 122.1611 115.0 200 72.1 1.6 101.4 3.66 4.62 23.81 5.72 62.5612 115.0 50 72.0 1.6 67.8 2.04 3.99 41.66 5.65 84.7013 114.0 200 82.3 1.4 91.1 2.90 4.01 33.79 5.36 88.5314 114.0 50 82.5 1.4 69.0 1.74 3.84 53.20 5.88 116.0215 102.0 200 68.5 1.5 96.4 3.48 4.36 27.35 5.55 66.9016 102.0 50 68.5 1.5 73.1 2.12 3.93 41.03 5.54 79.3217 91.7 200 66.1 1.4 97.0 3.26 3.95 26.09 4.98 56.3518 91.7 50 66.1 1.4 75.2 2.02 3.81 44.87 5.52 81.40
Table I X item number ejecta long filament extensibility stretching S1 D.S. %U
Dawn is counted temperature (%) (%)
(℃)?1 172 200 1.64 25 48.1 1.92 0.49?2 172 50 1.64 25 60.8 16.58 4.89?3 172 200 1.64 100 18.2 3.95 0.90?4 172 50 1.64 100 46.8 12.41 5.04?5 172 200 1.64 110 11.7 1.72 0.49?6 172 50 1.64 110 32.5 11.47 3.01?7 172 200 1.64 115 10.3?8 172 50 1.64 115 20.5?9 172 200 1.64 120 9.8 3.48 0.7410 172 50 1.64 120 18.1 7.68 1.8411 172 200 1.64 130 8.3 2.86 0.7612 172 50 1.64 130 10.3 5.03 1.3813 172 200 1.64 140 7.4 2.78 0.7014 172 50 1.64 140 8.5 4.02 1.1115 172 200 1.64 150 6.6 2.99 0.7716 172 50 1.64 150 7.4 3.48 0.9617 172 200 1.64 160 6.2 2.90 0.7518 172 50 1.64 160 6.7 3.64 1.0419 172 200 1.64 170 5.6 2.47 0.7320 172 50 1.64 170 6.5 3.31 1.0621 172 200 1.64 180 5.4 5.29 1.2822 172 50 1.64 180 6.1 3.37 1.08
The low high DPF extensibility of the DGP set-stretching S1 D.S. %U of Table X item number feeding thing
Amount number temperature temperature (%) (%)
(C) (C)?1 199 0.78 2.58 1.64 25 25 47.2 2.89 0.55?2 199 0.78 2.58 1.64 100 25 22.1 2.67 0.77?3 199 0.78 2.5?8 1.64 110 25 14.2 2.77 0.73?4 199 0.78 2.58 1.64 115 25 10.0 2.07 0.60?5 199 0.78 2.58 1.64 120 25 10.8 2.07 0.60?6 199 0.78 2.58 1.64 130 25 9.0 1.59 0.60?7 199 0.78 2.58 1.64 140 25 7.9 2.03 0.75?8 199 0.78 2.58 1.64 150 25 7.3 2.49 0.85?9 199 0.78 2.58 1.64 160 25 6.6 2.15 0.8510 199 0.78 2.58 1.64 170 25 6.2 2.50 0.8811 199 0.78 2.58 1.64 180 25 5.8 2.44 0.9212 127 0.50 1.65 1.40 25 25 28.4 1.58 0.4813 127 0.50 1.65 140 180 180 5.9 1.82 0.54
The undue modulus in tension T that formalizes that feeds of Table X I item number feeding thing extensibility stretching temperature 7T 20Ten. Eb Tb S1
Dawn is gone into (g/d) (g/d) (g/d) (%) (g/d) (%) of temperature thing dawn number (g/d) several times
(C) (％) (C)?1 127 1.4 25 16 25 104.5 23.9 1.05 1.95 2.57 37.5 3.53 21.2?2 127 1.4 25 16 180 110.8 46.3 0.97 1.83 2.26 31.0 2.96 1.4?3 127 1.4 115 16 25 103.8 20.0 1.19 2.19 2.64 32.6 3.50 7.8?4 127 1.4 115 16 180 108.2 36.2 1.10 2.07 2.58 33.5 3.44 1.6?5 127 1.4 180 16 25 103.8 18.9 1.27 2.44 2.54 22.3 3.11 3.8?6 127 1.4 180 16 180 104.2 37.7 1.42 2.43 2.74 27.5 3.49 1.9?7 159 1.6 25 16 25 116.3 28.0 1.06 1.84 2.66 37.2 3.65 40.3?8 159 1.6 25 16 180 138.1 34.3 0.76 1.23 2.37 49.6 3.55 1.7?9 159 1.6 115 16 25 114.4 21.1 1.27 2.37 2.66 26.0 3.35 8.710 159 1.6 115 16 180 120.6 29.8 0.94 2.07 2.76 34.0 3.70 1.911 159 1.6 180 16 25 114.4 18.4 1.23 2.63 2.91 24.8 3.63 4.412 159 1.6 180 16 180 115.1 24.7 1.24 2.58 2.85 24.7 3.55 2.6

Claims (32)

1. the method for preparing non-stretching mixed filament polyester spray silk orientated yarns, described yarn peak contraction tension force temperature T (ST Maximum) in high about 5～30 ℃ scope than glass transition temperature of polymer Tg, this yarn is made up of the long filament that its cross section of two classes and/or dawn number differ from one another at least, the at least a of this filament types is fine filament, and every rhizoid dawn number of this fine filament is called (dpf) here less than about 1 1, said filament types has identical polyester polymers, and this method for making comprises:
(i) selecting polyester polymers to make it relative viscosity LRV is about 13～23, zero shearing fusing point T M° be about 240～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃; This polymer melted and be heated to than melting point polymer T M° high about 25 ℃～55 ℃ temperature Tp; Filter this polymer melt rapidly to reduce degraded; This melt by different outlet opening shapes spinneret capillary and/or have difference (L/D RND 4) capillary of value to be to generate its cross section and/or the different filament types of dawn number; Wherein concerning this fine filament type, the cross-sectional area A c of spinneret capillary is about 125 * 10 -6Cm 2～1250 * 10 -6Cm 2, select length L and diameter D RND, make its ratio (L/D RND 4) be at least about 1.25 and less than about 6;
(ii) when the melt of newly extruding from spinneret capillary at least about 2cm and less than about 12 (dpf) 1 1/2The distance L of cm DQProtect it to make it not be subjected to direct cooling during discharge; Drawing-down and the gained long filament is chilled to be lower than glass transition temperature of polymer Tg then; Wherein this fine filament type is about 5.7～7.6 by drawing-down to the scope of apparent spray silk thread strain; At the extremely about [50+90 (dpf) of about 50cm 1 1/2] using low-friction surface in the distance L c of cm, long filament is assembled becomes endless tow; With about 2～6 kilometers/minute speed endless tow is batched; The long filament generation combined filament yarn that interweaves; The extension at break E of this combined filament yarn wherein BIntensity T for about 40%～160%, 7% when elongation 7Be about 0.5～1.75g/d, shrinkage value is for can make (1-S/Sm) value be at least about 0.05, and differential is shunk (DHS-S) less than making an appointment with+2%, and wherein S is that destarch is shunk, and Sm is maximum potential minification, and DHS is 180 ℃ of xeothermic contractions that record.
2. according to the method for making of claim 1, the wherein said combined filament yarn that do not stretch is stretched to generate mixed filament stretch yarn, the latter's remaining extension at break E BIntensity T for about 15%～45%, 7% when elongation 7Be at least about 1g/d, and (1-S/Sm) value is at least approximately 0.85, wherein this yarn also can be out of shape to generate draw-textured yarn.
3. according to the method for making of claim 1, wherein should select processing conditions, make the extension at break E of non-stretching polyester yarn BFor the intensity in about 40%～90%, 7% when elongation is about 1～1.75g/d, shrink S for can make (1-S/Sm) value be at least about 0.85.
4. according to the method for making of claim 3, wherein this non-stretching combined filament yarn is stretched and generates the combined filament yarn that stretches, the latter's remaining extension at break E BIntensity T for about 15%～55%, 7% when elongation 7Be at least about 1g/d, and keep (1-S/Sm) value to be at least about 0.85.
5. according to the method for making of claim 4, wherein this yarn also can be deformed and generate the varicosity combined filament yarn that stretches.
6. according to the method for making of claim 3, wherein this non-stretching combined filament yarn is generated the combined filament yarn that stretches, the latter's remaining extension at break E by cold stretch BIntensity T for about 15%～55%, 7% when elongation 7Scope for about 1～1.75g/d.
7. according to the method for making of claim 3, wherein this non-stretching combined filament yarn is generated the bulk yarn with the described yarn performance of claim 6 by air jet texturing.
8. according to each method for making of claim 1～7, wherein should select processing conditions to generate the non-stretching combined filament yarn of belt length silk, the difference that the long filament of this long filament shrinks S is at least 5%.
9. method for making according to Claim 8, wherein this non-stretching combined filament yarn is stretched, and draft temperature is at least glass transition temperature of polymer Tg approximately and is lower than crystallization start temperature Tc ° to generate varicosity mixed filament stretch yarn, the latter's remaining extension at break E BFor about 15%～45%, and the intensity T during 7% elongation 7Be at least about 1g/d.
10. according to the method for making of claim 9, wherein this yarn also can be deformed the generation draw-textured yarn.
11. according to the method for making of claim 9, wherein this non-stretching combined filament yarn is stretched and is at least 0.85 varicosity mixed filament stretch yarn to generate (1-S/Sm) value.
12. method for making according to Claim 8, wherein this non-stretching mixed filament polyester yarn is sprayed cold air distortion and is generated the bulk yarn that mixes shrinkage continuous yarn, this bulk yarn anti-open and shrinkage in as claim 1 and the described scope of claim 8.
13. according to the method for making of claim 1, wherein should select processing conditions, make its extension at break E to generate non-stretching combined filament yarn BBe about 40%～90%, intensity during 7% elongation is about 1～1.75g/d, it is differed by shrinkage S and is at least about at least two kinds of dissimilar long filaments of 5% and forms, wherein at least a filament types have such contraction S so that (1-S/Sm) value be about 0.85 at least, and the contraction S of another filament types is about 0.25～0.85 for making (1-S/Sm) value at least.
14. according to the method for making of claim 13, wherein this non-stretching combined filament yarn is generated varicosity mixed filament stretch yarn, its remaining extension at break E by jet stretcher strain BIntensity T for about 15%～55%, 7% when elongation 7Be about 1～1.75g/d.
15., wherein select processing conditions to generate non-stretching combined filament yarn, its extension at break E according to the method for making of claim 1 BFor the intensity in about 90%～120%, 7% when elongation is about 0.5～1g/d, shrinks S and can make that (1-S/Sm) value is about 0.25～0.85.
16. according to the method for making of claim 15, wherein this non-stretching combined filament yarn is carried out stretcher strain with air jet texturing method or false add sth. made by twisting deformation method, generates stretch yarn, the latter's extension at break E BIntensity T for about 15%～45%, 7% when elongation 7Be at least about 1g/d, and (1-S/Sm) value is at least about 0.85.
17. according to each method for making of claim 1～16, wherein select processing conditions, make its average filament dawn number and [1.3/ (1+E to generate long filament B/ 100)] product is about 1 or less than 1.
18., wherein select processing conditions to generate such long filament, the dawn number (dpf) of this fine filament according to each method for making of claim 1～17 1Filament denier ratio to the dawn number of high Denier long filament is about 1: 2 to about 1: 6.
19. mixed filament spray silk oriented polyester yarn of forming by at least two kinds of filament types, this two types long filament is difference aspect cross section and/or dawn number, but all have identical polyester polymers, wherein the relative viscosity LRV of polyester polymers is about 13～23, zero shearing fusing point T M° be about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, wherein the extension at break E of this yarn BIntensity T for about 40%～160%, 7% when elongation 7Be about 0.5～1.75g/d, at peak contraction tension force temperature T (ST Maximum) its maximum collapse tension force (ST when being about (Tg+5 ℃) to about (Tg+30 ℃) Maximum) less than about 0.2g/d, and its shrinkage value is for making differential shrink (DHS-S) less than about+2%, value is at least about 0.1 and (1-S/Sm), S is that destarch is shunk in the formula, Sm is maximum potential minification, and DHS is xeothermic contraction (measuring at 180 ℃), and wherein at least a filament types is that filament denier is about 1 or less than 1 fine filament.
20. according to the yarn of claim 19, its extension at break E BIntensity T for about 90%～120%, 7% when elongation 7Be about 0.5～1g/d, and (1-S/Sm) value is at least about 0.25.
21. according to the yarn of claim 20, this yarn particularly suitable is made the stretching feeding yarn.
22. according to the yarn of claim 19, its extension at break E RIntensity T for about 40%～90%, 7% when elongation 7Be about 1～1.75g/d, and (1-S/Sm) value is at least about 0.85.
23. according to the yarn of claim 22, this yarn is specially adapted to directly use yarn.
24. a jet modification mixed filament spray silk oriented polyester yarn, different by its cross section of two classes and/or dawn number at least but long filament that all have an identical polyester polymers is formed, and the relative viscosity LRV of polyester polymers wherein is about 13～23, zero shearing fusing point T M° be about 240～265 ℃, and glass transition temperature Tg is about 40 ℃～80 ℃, and the extension at break E of this yarn wherein BIntensity T when being about 40%～90%, 7% elongation 7Be about 1～1.75g/d, at peak contraction tension force temperature T (ST Maximum) its maximum collapse tension force (ST when being about (Tg+5 ℃) to about (Tg+30 ℃) Maximum) be less than about 0.2g/d, it is about 0.85 for making that (1-S/Sm) value is at least that it shrinks S, and S is destarch contraction and Sm is maximum potential minification here, and wherein at least one class long filament is that its filament denier is about 1 or less than 1 fine filament.
25. one kind can a back varicosity mixed filament spray silk oriented polyester yarn, it counts difference by its cross section of at least two classes and/or dawn, but the long filament that all has an identical polyester polymers forms, and wherein the relative viscosity LRV of polyester polymers about 13～23, zero shears fusing point T M° be about 240 ℃～265 ℃, and glass transition temperature Tg is about 40 ℃～80 ℃, and the extension at break E of this yarn BIntensity T for about 40%～90%, 7% when elongation 7Be about 1～1.75g/d, at peak contraction tension force temperature T (ST Maximum) be the maximum collapse tension force (ST under about (Tg+5 ℃) to about (Tg+30 ℃) Maximum) be less than about 0.2g/d, the contraction S of wherein at least a this class long filament is for can make (1-S/Sm) value be at least about 0.85, and the contraction S of another kind of at least this class long filament can make that (1-S/Sm) value is about 0.25～0.85, wherein the difference of the long filament of this class long filament contraction S is at least 5%, here S is that destarch is shunk, and Sm is maximum potential minification, and wherein at least one class long filament is that its filament denier is about 1 or less than 1 fine filament.
26. one kind can spray silk oriented polyester yarn by back varicosity air jet texturing mixed filament, its long filament different by its cross section of at least two classes and/or dawn number but that all have an identical polyester polymers is formed, here the relative viscosity LRV of polyester polymers is about 13～23, zero shearing fusing point T M° about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, wherein the extension at break E of this yarn BIntensity T for about 40%～90%, 7% when elongation 7Be about 1～1.75g/d, and at peak contraction tension force temperature T (ST Maximum) be the maximum collapse tension force (ST when making an appointment with (Tg+5 ℃) to about (Tg+30 ℃) Maximum) be less than about 0.2g/d, the contraction S of at least a here this class long filament can make (1-S/S Maximum) value is at least about 0.85, and the contraction S of another kind of at least this class long filament is for can make (1-S/Sm) value be at least about 0.25～0.85, and the difference of the contraction S of such long filament is at least 5%, here S is that destarch is shunk and Sm is maximum potential minification, and wherein at least one class long filament is that its filament denier approximates 1 or less than 1 fine filament.
27. a stretching can back varicosity mixed filament polyester yarn, its long filament different by its cross section of at least two classes and/or dawn number but that all have an identical polyester polymers is formed, and wherein the relative viscosity LRV of polyester polymers is about 13～23, zero shearing fusing point T M° it is about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, wherein the difference of the contraction S of this class long filament is at least 5%, and the contraction S of at least a this class long filament is for can make (1-S/Sm) value be at least about 0.85, and the contraction S of another kind of at least this class long filament can make that (1-S/Sm) value is about 0.25～0.85, and the extension at break E of this yarn wherein BIntensity T for about 15%～45%, 7% when elongation 7Be at least about 1g/d, then surrendering modulus Mpy is about 5～25g/d, and wherein at least a this class long filament is that its filament denier approximates 1 or less than 1 fine filament.
28. air jet texturing mixed filament polyester yarn of varicosityization afterwards that stretches, its long filament different by its cross section of at least two classes and/or dawn number but that all have an identical polyester polymers is formed, wherein the relative viscosity LRV of polyester polymers is about 13～23, zero shearing fusing point T M° be about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, wherein the difference of the long filament of these type long filaments contraction S is at least 5%, and the contraction S of at least a this class long filament is for can make (1-S/Sm) value be at least about 0.85, and the contraction S of another kind of at least this class long filament is for can make (1-S/Sm) value be about 0.25～0.85, here S is that destarch is shunk and Sm is maximum potential minification, and the extension at break E of this yarn here BFor the intensity in about 15%～45%, 7% when elongation is at least about 1g/d, back surrender modulus Mpy is about 5～25g/d, and wherein at least a type long filament is that its filament denier is about 1 or less than 1 fine filament.
29. a stretching mixed filament polyester yarn, it counts difference by its cross section of at least two classes and/or dawn, but all has the long filament composition of identical polyester polymers, and wherein the relative viscosity LRV of this polyester polymers is about 13～23, and zero shears fusing point T M° be about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, wherein the extension at break E of this yarn BIntensity T for about 15%～45%, 7% when elongation 7Be 1d/g at least, back surrender modulus Mpy is about 5～25g/d, and (1-S/Sm) value is at least about 0.85, and S is the destarch contraction here, and Sm is maximum potential minification, and wherein at least a long filament is that its filament denier is about 1 or less than 1 fine filament.
30. a stretching false add is twisted with the fingers distortion mixed filament polyester yarn, it by its cross section of at least two classes and/or dawn number different but the long filament that all has an identical polyester polymers formed, wherein the relative viscosity LRV of polyester polymers is about 13～23, zero shearing fusing point T M° be about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, and the extension at break E of this yarn wherein BIntensity T for about 15%～45%, 7% when elongation 7Be at least about 1g/d, then surrendering modulus Mpy is 5～25g/d, and (1-S/Sm) value is at least about 0.85, and S is that destarch is shunk here, and Sm is maximum potential minification, and wherein at least one class long filament is that its filament denier is about 1 or less than 1 fine filament.
31. a stretching air jet texturing mixed filament polyester yarn, it counts difference by its cross section of at least two classes and/or dawn, but the long filament that all has an identical polyester polymers forms, and wherein the relative viscosity LRV of polyester polymers about 13～23, zero shears fusing point T M° be about 240 ℃～265 ℃, glass transition temperature Tg is about 40 ℃～80 ℃, and the extension at break E of this yarn wherein BIntensity T for about 15～45%, 7% when elongation 7Be at least about 1g/d, back surrender modulus Mpy is about 5～25g/d, and (1-S/Sm) value is at least about 0.85, and S is the destarch contraction here, and Sm is maximum potential minification, and wherein at least one class long filament is that its filament denier is about 1 or less than 1 fine filament.
32. according to each yarn of claim 19～31, wherein this average filament dawn number and [1.3/ (1+E B/ 100) product] is about 1 or less than 1.
33. according to each yarn of claim 19～32, it comprises the high dawn of a class and counts long filament, its dawn number is for making that average filament dawn number that this high dawn counts filament types is about 2～6 to the ratio of the average filament dawn number of described fine filament type.
CN93117656A 1992-08-05 1993-08-05 Polyester mixed yarns with fine filaments Expired - Fee Related CN1048765C (en)

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