EP0378194B1 - Fil de filaments composés, procédé et filière pour leur fabrication - Google Patents
Fil de filaments composés, procédé et filière pour leur fabrication Download PDFInfo
- Publication number
- EP0378194B1 EP0378194B1 EP90100443A EP90100443A EP0378194B1 EP 0378194 B1 EP0378194 B1 EP 0378194B1 EP 90100443 A EP90100443 A EP 90100443A EP 90100443 A EP90100443 A EP 90100443A EP 0378194 B1 EP0378194 B1 EP 0378194B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- polyurethane
- component
- polyamide
- spinneret
- composite filament
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002131 composite material Substances 0.000 title claims description 77
- 238000000034 method Methods 0.000 title claims description 16
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 229920002635 polyurethane Polymers 0.000 claims description 82
- 239000004814 polyurethane Substances 0.000 claims description 82
- 239000000306 component Substances 0.000 claims description 74
- 239000004952 Polyamide Substances 0.000 claims description 54
- 229920002647 polyamide Polymers 0.000 claims description 54
- 238000002347 injection Methods 0.000 claims description 22
- 239000007924 injection Substances 0.000 claims description 22
- 239000008358 core component Substances 0.000 claims description 15
- 238000009835 boiling Methods 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 7
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 6
- 239000000155 melt Substances 0.000 claims description 6
- 230000000149 penetrating effect Effects 0.000 claims description 3
- 239000000243 solution Substances 0.000 claims description 3
- 238000001125 extrusion Methods 0.000 claims 1
- 238000009987 spinning Methods 0.000 description 20
- 238000005299 abrasion Methods 0.000 description 18
- 238000010438 heat treatment Methods 0.000 description 16
- 238000009940 knitting Methods 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 6
- 229920000515 polycarbonate Polymers 0.000 description 6
- 239000004417 polycarbonate Substances 0.000 description 6
- 230000007423 decrease Effects 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 230000007547 defect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000005452 bending Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 229920002292 Nylon 6 Polymers 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 210000003734 kidney Anatomy 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 206010037660 Pyrexia Diseases 0.000 description 1
- 239000004433 Thermoplastic polyurethane Substances 0.000 description 1
- WNLRTRBMVRJNCN-UHFFFAOYSA-L adipate(2-) Chemical compound [O-]C(=O)CCCCC([O-])=O WNLRTRBMVRJNCN-UHFFFAOYSA-L 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 229920000547 conjugated polymer Polymers 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 230000006355 external stress Effects 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N hexane Substances CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 238000007578 melt-quenching technique Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000004632 polycaprolactone Substances 0.000 description 1
- 229920001610 polycaprolactone Polymers 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 229920003225 polyurethane elastomer Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000002040 relaxant effect Effects 0.000 description 1
- 230000000452 restraining effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/28—Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
- D01D5/30—Conjugate filaments; Spinnerette packs therefor
- D01D5/34—Core-skin structure; Spinnerette packs therefor
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
- D01F8/12—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyamide as constituent
Definitions
- the present invention relates to polyamide/ polyurethane composite filament yarns having a crimpability, a process and a spinneret for manufacturing the same and hosiery, such as stockings or the like, knitted therewith.
- composite filaments consisting of polyamide and polyurethane components conjugated eccentrically with each other in a unitary filament have an excellent crimpability (Japanese Patent Application Publication Nos. Sho-55-22,570 and 55-27,175).
- side-by-side type composite filaments for example, such as shown in Fig. 4, though these are excellent in crimpability, have a drawback such that separation of the components and deterioration of physical properties are caused by bending or abrasion during processing steps or wearing of textile articles composed of such filaments, due to insufficient compatibility of the both components.
- Another drawback is polyurethane components exposed on the surface of the filament stick to each other due to retarded solidification of polyurethane melt, so that as-spun and wound filament yarns cannot be unwound from a yarn package due to sticking.
- sheath and kidney-like core type composite filaments as shown in Fig. 5 which have been proposed, for example, in Japanese Patent Application Publication No. Sho-55-27,175, have solved the problems presented by the side-by-side type composite filaments, such filaments still have a drawback that a crimp developability by virtue of difference in shrinkage between a high shrinking polyurethane component and a low shrinking polyamide component is poor because the polyurethane core component is completely surrounded with the polyamide sheath component.
- the spinneret shown in Fig. 2 comprises a vertical conduit 2 extending from a polyamide leading duct 1, having an orifice 3 of small diameter opening downwards, and an injection pipe 5 extending obliquely downwards from a polyurethane leading duct 4, protruding the tip end portion into said conduit 2.
- the degree of the protrusion is adjusted to an extent that the inner circumference of the opening tip end of the injection pipe 5 is just tangent internally to the inner circumference of the conduit 2.
- the polyamide component A surrounds the most part of the polyurethane component and decreases gradually its thickness along the periphery, so that stress concentration as aforementioned is relaxed so that excellent adhesion is obtained between the polyamide and polyurethane components, not allowing the both components to split easily and sticking of polyurethane components to each other can be prevented between as-spun filament yarns wound on a take-up roll.
- both the side-by-side type and sheath and kidney-like core type filaments are attended by a problem of fisheyes caused by a poor stability of polyurethane melt during spinning.
- the fisheye is meant a local thick portion in drawn filament after spinning, winding and drawing, which causes a poor draw-twisting operability of undrawn filament yarns as well as inferior qualities of articles, such as stockings, composed of the filament yarns.
- the number of fisheyes is a value obtained by counting thick portions having a diameter five times the normal diameter of the unitary filament constituting a drawn yarn and converting the count to the number per 1 kg of the filament yarn.
- a composite filament yarn comprising a metallic conductive core exposed at a small part of the surface is shown in EP-A-0 276 756.
- EP-A-0 276 756 A composite filament yarn comprising a metallic conductive core exposed at a small part of the surface is shown in EP-A-0 276 756.
- the exposed part is uniform or not, even if the exposed part is not throughout the length of the yarn, in order to minimize metal abrasion.
- the first object of the present invention is to constantly provide uniform, incomplete sheath and core type composite filaments consisting of a polyamide and a polyurethane, with excellent physical properties, such as crimpability, abrasion resistance or the like, and exhibiting a good processability with a restrained stickiness of undrawn yarns.
- the second object is to largely reduce fisheyes of drawn yarns by passing a polyamide/polyurethane composite polymer through a constriction in a nozzle to effect fluid orientation.
- the polyurethane core component is preferred to be exposed substantially in a uniform width preferably between 3% and 15%, of the circumference of the filament.
- said exposed width has a standard deviation of not exceeding 1.6%, about a mean value.
- the composite filaments of the invention are preferred to have a cross-sectional shape of the polyamide sheath component wherein a thin portion having a thickness of not more than 1/20 of the diameter of the composite filament, extends by a width of not exceeding 1/5, preferably 1/10, of the diameter of the composite filament, and terminates suddenly reducing the thickness. With such a shape, it is easy to maintain a uniform exposed width of the polyurethane core component.
- the conjugate ratio of the polyamide and polyurethane components is preferably 40/60 ⁇ 80/20, more preferably 45/55 ⁇ 70/30, by volume.
- the invention can provide composite filament yarns having preferably not more than 500 fisheyes/kg after drawing.
- said polyamide component has a relative viscosity of 2.0 ⁇ 2.6 determined with 10 mg/ml solution in 95.7% sulfuric acid and said polyurethane component has a melt viscosity at 210°C of 2,000 ⁇ 5,000 Pa ⁇ s (20,000 ⁇ 50,000 poise).
- the injection pipe contemplated in the spinneret is preferred to have an inside diameter of 30 ⁇ 80% of that of the conduit.
- the slit contemplated in the spinneret is preferred to have, in its projected figure on a horizontal plane, a length of 2 ⁇ 20% of the inside diameter of said conduit and a width of 0.2 ⁇ 10% of the circumference of said conduit.
- the conduit preferably expands divergently from the constricted portion towards the orifice.
- the constricted portion has a bore diameter in the range of 0.20 ⁇ 0.45 mm, preferably 0.25 ⁇ 0.40 mm, and the orifice has an opening diameter in the range 0.5 ⁇ 0.7 mm.
- a molten polyamide component is supplied from a polyamide leading duct 1 into a vertical conduit 2 and then extruded from a spinneret orifice 3.
- a molten polyurethane component is supplied from a polyurethane leading duct 4 and injected through an injection pipe 5 into the conduit 2.
- This injection pipe 5 extending obliquely from the duct 4, penetrates and protrudes into the conduit 2 and opens immediately before the orifice 3.
- the inside diameter of the injection pipe 5 is determined in the range between 30% and 80% of the inside diameter of the conduit, depending upon the conjugate ratio of the both components.
- the length of the protrusion and the slanting angle of the injection pipe 5 may be adequately selected so that, in the projected figure on a horizontal plane of the pipe, the inner circumference at the tip end opening of the pipe may reach a distance of about 1/2 ⁇ 3/4 of the diameter of the conduit 2 and the projected length ⁇ of the generating line at the under side of the inner periphery of the pipe may be about 2 ⁇ 20% of the diameter of the conduit 2.
- the injection pipe 5 is provided at its under side with a slit 6 extending along the entire length ⁇ of the portion protruded into the conduit.
- the under side is meant a portion along the lower generating line in a vertical plane including the longitudinal axis of the pipe. If the position of the slit deviates from the under side, disposition of a neck portion as will be illustrated hereinafter that is formed by the slit also deviates from the thinnest portion of the polyamide sheath, so that the crimpability of the resulting composite filament yarns will be undesirably deteriorated.
- the slit 6 is preferred to have a width of about 0.2 ⁇ 10% of the circumference of the conduit 2. If the width is less than 0.2%, the objective cross-sectional conjugate shape cannot be obtained and a core and complete sheath type may be formed. Alternatively, the width should not exceed 10.0%, because when it exceeds 10.0%, the polyurethane component is exposed so excessively on the surface of the filament that drawbacks of side-by-side type composite filament yarns, such as poor abrasion resistance and intense stickiness of wound undrawn yarns, will appear.
- the polyurethane component flow is incorporated, with appropriate conjugate ratio and eccentricity, to the polyamide component flow flowing down in the conduit 2, while a part of the polyurethane component flow which is radially projected in a restricted width and penetrates through the thinnest portion of said polyamide flow up to the inner wall of the conduit flows down from the above-described slit 6 along the inner wall of the conduit 2.
- the projected part of the polyurethane core component is interposed between two split thin portions of the polyamide sheath component.
- the thus conjugated polymer flow is spun from the orifice 3 to form a composite filament.
- the injection pipe is positioned to open its protruded portion into a level immediately above the orifice, the relative arrangement of the both components is preserved in the spun filament, substantially without being disturbed.
- the spinneret to be employed in the present invention is preferred to have a constricted portion 7 in the conduit for the polyamide/polyurethane conjugated flow to pass through.
- the constricted portion through which the polyamide/polyurethane conjugated flow passes is preferred to have a bore diameter in the range of 0.20 ⁇ 0.45 mm, preferably 0.25 ⁇ 0.40 mm
- the conduit after the constricted portion to the orifice is preferred to expand like a trumpet 8 having an opening diameter in the range of 0.5 ⁇ 0.7 mm.
- the conjugated molten polyamide/polyurethane components flowing through the constricted portion of 0.20 ⁇ 0.45 mm diameter are fluid oriented whereby fisheyes of the composite filament yarns can be largely reduced.
- no more than 1,000 fisheyes, preferably no more than 500 fisheyes, per 1 kg of yarn, are counted in the composite filament yarn of the present invention produced with the spinneret having the constriction, while no less than about 2,000 fisheyes per 1 kg of yarn are counted in the conventional yarns.
- the bore diameter of the constricted portion 7 exceeds 0.45 mm, the fisheye restraining effect becomes insufficient.
- it is less than 0.20 mm a pressure loss at the constricted portion is too large to adapt the spinneret to the practical operation.
- the divergent trumpet-like conduit formed after the constriction can mitigate, by virtue of a stress relaxing function, a kneeing phenomenon (bending of the extruded polymer immediately after spinning) and prevent filament breakages due to depositing of polymer decomposition products on the rim of the orifice.
- a polyurethane core component B is disposed, with adequate conjugate ratio and eccentricity, in a polyamide sheath component A and the polyurethane core component is uniformly exposed on the surface of the filament by a polyurethane neck portion D penetrating the thinnest portion C of said polyamide sheath component A.
- the exposed width of the neck portion D on the surface of the filament becomes substantially uniform in the range of between 2% and 25%, preferably between 3% and 15%, of the circumference of the filament. If the exposed width is smaller than the above range, the crimpability becomes insufficient, while if the exposed width is too large, it is not preferred because there is apt to appear an ill effect of stickiness as well as deterioration of abrasion resistance due to separation of the two components.
- the shape and exposed width of the neck portion are made uniform and the variation thereof due to influence of temperature condition change or the like becomes extremely small, so that the variation of the exposed width is restrained in a standard deviation about a mean value of not more than 2.0%, in a preferred embodiment not more than 1.6%, within a lot of the same specification, not to mention in the same filament.
- uniform polyamide/polyurethane composite filament undrawn yarns with reduced stickiness can be obtained and knit operability of these yarns is improved, whereby knitted goods of excellent qualities can be obtained with largely decreased knitting defects such as barré or the like.
- the conjugate ratio of the polyamide component to the polyurethane component is preferably within the range of 40/60 ⁇ 80/20, more preferably 45/55 ⁇ 70/30, by volume. Satisfactory crimp properties are obtained in the above range.
- Preferable polyamide applicable to the present invention are poly- ⁇ -capramide and copolymers thereof containing not more than 30 mole % of copolymerizable component.
- other known polyamides such as polyhexamethylene adipamide, copolymers thereof, blend polymers thereof, or the like, can be applied.
- Suitable polyurethanes applicable to the present invention are thermoplastic polyurethane elastomers having a hardness of 90 ⁇ 100, that is determined in accordance with JIS K-6301, the testing method of Shore hardness (A-type).
- thermoplastic polyurethane elastomers having a hardness of 90 ⁇ 100, that is determined in accordance with JIS K-6301, the testing method of Shore hardness (A-type).
- Polyurethanes having a hardness of less than 90 are difficult to balance the melt viscosity with polyamides (difficult to spin with stability), while polyurethanes having a hardness of exceeding 100 are apt to be low in elastic recovery.
- Polyurethane elastomers given a crosslinkage structure in molecules by melt-blending a polyisocyanate compound prior to conjugate spinning, are also preferred for their excellent heat resistance, crimpability and compatibility with polyamides.
- polyurethanes are polycarbonate based polyurethanes, most preferably polyurethanes comprising soft segments of polycarbonate/polyester blend (blend ratio of two components being 8/2 ⁇ 4/6).
- the polyamide components to be applied to the process according to the present invention has a relative viscosity within the range of 2.0 ⁇ 2.6, determined with 10 mg/ml solution in 95.7% sulfuric acid, while the polyurethane components have a melt viscosity of 2,000-5,000 Pa ⁇ s (20,000 ⁇ 50,000 poise), determined with a flow-tester at 210°C. If the viscosity difference decreases beyond the above range, a satisfactory crimpability cannot be assured, while if the viscosity difference is too large, stabilized spinning operation may possibly be impeded due to the aforementioned kneeing phenomenon.
- the spun filament yarn is taken up on a bobbin after solidification by quenching, and then the wound as-spun yarn is drawn at an appropriate draw ratio and further subjected to heat treatment, etc., followed by winding on a pirn, according to the conventional process.
- the as-spun yarn is, without being taken-up on a roll, subjected to direct drawing or heat treatment.
- the present invention includes both the above processes.
- the polyamide/polyurethane composite filament drawn yarns according to the invention are preferred to have a shrinkage in boiling water of generally 5 ⁇ 30%, more preferably 7 ⁇ 25%. If it exceeds 30%, the yarns excessively shrink in the heat treatment process after knitting, so that short sized knitted goods are yielded, while if less than 5%, sufficient crimps do not develop in the heat treatment process after knitting and the articles such as stockings will be lack in stretchability.
- the heat treatment is preferred to be conducted continuously at a relax ratio slightly larger than the shrinkage in boiling water determined with drawn yarns.
- the relax ratio during a relax heat treatment is smaller than the shrinkage in boiling water of drawn yarns, the wound yarns develop feeble crimps, while in the case where the heat treatment is conducted at a relax ratio fairly larger than the shrinkage in boiling water, the heat-treated yarns develop ripple-like fine crimps like an elongated spring.
- a relax heat treatment there may be a process of heating the yarns traveling through a tube heater with air as a heating medium, a process of hot plate heat treatment wherein the yarns travel on a plate heater, or the like.
- Composite filament yarns according to the present invention are desirably composed of 1 ⁇ 10 constituent filaments of 3 ⁇ 30d and have a total fineness of 5 ⁇ 50d.
- the total fineness is in the range of 5 ⁇ 30d and the number of the constituent filaments is in the range of 1 ⁇ 6. If the unitary filaments constituting the yarn have a fineness of less than 3d, the stockings show an insufficient durability when they are worn. While if more than 30d, the stockings will have stiff hand.
- the stockings in the present invention include all of the overknee stockings, full length stockings and panty hoses.
- the exposed width is largely varied by a slight change of conditions, as described hereinbefore, resulting in uneven crimp properties, posing a problem of low abrasion resistance and causing local stickiness due to exposed polyurethane components.
- the composite filament yarns of the present invention since the neck portion has a width evenly stabilized in appropriate size, are prominently excellent in crimp properties, durability and processability. Further, defects of knitted goods, such as barré or the like, decrease largely, whereby knitted goods having excellent qualities can be obtained.
- polyamide/polyurethane composite filament drawn yarns having excellent crimp properties and abrasion resistance as well as improved processability and good quality with largely decreased fisheyes.
- the composite filaments of the present invention can be used alone or in combination with other kinds of fibers, such as polyamide fibers, cotton fibers, polyurethane core covering yarns or the like, according to conventional processes, such as doubling, ply-twisting, intermingling, mix-knitting, mix-weaving or the like.
- the composite filament yarns of the invention are suitable for textile products, such as stockings, tights, ladies' lingerie and foundation garments or the like.
- shrinkage percentage, stretch percentage and abrasion resistance which represent crimp property are determined according to the following methods:
- Shrinkage percentage (%) (l 0 -l 1 )/l 0 ⁇ 100
- the yarn after drawing and heat treatment in relax is circular knitted. After continuously repeating abrasion with a load of 1 kg, separation of two components on the surface of the knitted goods is microscopically observed and evaluated.
- Grade 3 no separation observed after 3,000 cycle abrasion.
- Grade 4 no separation observed after 5,000 cycle abrasion.
- the quality of the knitted goods is evaluated by observing barré defects of the circular knit which is knitted at a rotation rate of 600 r.p.m. with a usual tubular knitting machine having 4 feeders (400 needles) and then heat-treated in relax in boiling water to develop crimps.
- Nylon-6 having a relative viscosity of 2.35 and a polycarbonate based polyurethane having a melt viscosity at 210°C of 3200 Pa ⁇ s (32,000 poise) and a Shore A hardness of 95 were separately melted and then metered separately at a volume ratio of 50:50.
- the molten two polymers were conjugate spun, at a take-up speed of 500 m/min., from a spinneret for conjugate spinning as shown in Fig. 1, to form an undrawn yarn of 55d/2f.
- the spinneret for conjugate spinning used therefor had a conduit of 2 mm I.D. and a polyurethane injection pipe of 1 mm I.D. and 1.26 mm O.D.
- the conduit and the polyurethane injection pipe made an angle of 35° and the distance between the lowest point of the inner circumference of the tip end opening of the pipe and the nearest inner wall of the conduit ( ⁇ in Fig. 1) was 0.16 mm. Further, the length of a slit at the under side of the injection pipe ( ⁇ in Fig. 1) was 0.4 mm and the width of the slit was varied into 6 sizes as follows: Width of the slit (mm):0.01, 0.02, 0.10, 0.30, 0.50 and 0.70.
- all of the composite filament yarns Y2 ⁇ Y5 according to the present invention had a cross-sectional shape of unitary filament wherein a polyurethane core was almost lapped in a polyamide sheath, exposing on the surface of the filament with a neck portion having a uniform width of within 25% of the circumference of the filament. Additionally, the filament yarns of the invention showed good results in crimp properties, abrasion resistance and sticking of undrawn yarns.
- the conjugate spinning spinneret provided with an injection pipe having a slit 0.01 mm wide, produced a core and complete sheath type composite filament yarn Y1.
- the yarn Y1 was good in abrasion resistance and sticking of undrawn yarns, it showed poor crimp properties.
- the composite filament yarn Y7 produced with the conventional side-by-side conjugate spinning spinneret had a polyurethane component exposed width mean value of 47% of the circumference of the filament with a standard deviation above the mean value of 2.0%.
- This yarn Y7 had good crimp properties and, however, bad in sticking of undrawn yarn.
- Circular knitted goods knitted therewith had an inferior quality due to many barré.
- the comparative example yarn Y8 had a polyurethane exposed width mean value of 11% of the circumference of the filament with a standard deviation of more than 2.0%. This yarn Y8 was good in crimp properties, sticking property and abrasion resistance and, however, circular knitted goods knitted therewith had an inferior quality due to many barré.
- Nylon-6 having a relative viscosity of 2.35 and a polyurethane comprising soft segments of a blend polymer of polycarbonate and poly-1,6-hexane adipate (blend ratio of 7/3) were conjugate melt-spun with a spinneret same as that used in spinning of the yarn Y3 in Example 1 except that the diameter of the orifice was 0.50 mm and a constricted portion was provided. Changing the diameter of the constricted portion, seven kinds of composite filament yarns Y9 ⁇ Y14 of the present invention were obtained.
- Comparative example yarn Y15 was a conventional, eccentric kidney-like core and complete sheath type composite filament as shown in Fig. 5, wherein the conjugate ratio of polyamide to polyurethane was 1/1 in area.
- a conventional side-by-side type composite filament yarn Y16 as shown in Fig. 4 was obtained in the same manner as the yarn Y12 of the present invention excepting the conjugate figure.
- a polyamide/polyurethane composite filament yarn Y17 was obtained in the same manner except that a conjugate spinning spinneret without the constricted portion was used.
- the as-spun yarns were drawn on the plate heater at a drawing speed of 400 m/min. and a draw ratio of 3.50.
- the drawn yarns were heat-treated in relax with a relax heat treatment apparatus provided with a plate heater between 2 rolls and composite filament yarns of 20d/2f were obtained.
- the appearance of the yarn packages of these resulting composite yarns showed slack, wavy crimps developed. The crimp figure did not change maintaining the slack, wavy crimps, when the yarns were unwound from the yarn package.
- the fisheyes of the composite filament drawn yarns decrease and the pressure loss increases, according as decrease of the diameter of the constricted portion of the conjugate spinning spinneret orifice.
- the diameter of the constricted portion should be 0.20 ⁇ 0.45 mm, preferably 0.25 ⁇ 0.35 mm.
- composite filament yarns of the present invention is superior to the side-by-side type composite filament yarns, in respect of abrasion resistance and prevention of sticking of undrawn yarns.
- the material yarn Y12 for stockings obtained in Example 2 was knit into leg and foot portions with a 4 feeder hosiery knitting machine at a rotation rate of 900 r.p.m. The knitting operation was conducted without difficulties and the resulting stockings had a good quality. In contrast, the material yarns Y17 having many fisheyes could not knit with stability at the rotation rate of 900 r.p.m. due to formation of barré caused by skip stitch, yarn breakage or fluctuation of knitting tension.
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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)
- Multicomponent Fibers (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Claims (19)
- Filé de filament composite comprenant un composant de gaine en polyamide (A), et un composant d'âme en polyuréthane (B) disposés de façon excentrée dans ledit composant de gaine en polyamide, dans la section transversale d'un filament unitaire, ledit composant d'âme en polyuréthane étant exposé, pratiquement sur une largeur uniforme, à la surface du filament par l'intermédiaire d'une partie rétrécie en polyuréthane (D), qui s'étend radialement depuis ledit composant d'âme et qui pénètre dans la partie la plus mince (C) dudit composant de gaine en polyamide, jusqu'à la surface du filament, l'écart type de la largeur exposée ne dépassant pas 2,0 % de la valeur moyenne, le filé étiré ne contenant pas plus de 1000 yeux de poissons/kilo de filé, et le composant d'âme en polyuréthane étant exposé sur une largeur comprise entre 2 % et 25 % de la circonférence du filament.
- Filé de filament composite selon la revendication 1, dans lequel le composant d'âme en polyuréthane est exposé en une largeur comprise entre 3 % et 15 % de la circonférence du filament.
- Filé de filament composite selon la revendication 1, dans lequel l'écart type de la largeur exposée ne dépasse pas 1,6 % de la valeur moyenne.
- Filé de filament composite selon la revendication 1, dans lequel le composant polyamide et le composant polyuréthane sont dans un rapport en volume compris entre 40/60 et 80/20.
- Filé de filament composite selon la revendication 1, dans lequel le composant polyamide et le composant polyuréthane sont dans un rapport en volume compris entre 45/55 et 70/30.
- Filé de filament composite selon la revendication 1, dans lequel la section transversale du composant de gaine en polyamide comprend une partie mince d'une épaisseur ne dépassant pas 1/20 du diamètre du filament composite et qui s'étend sur une largeur ne dépassant pas 1/5 du diamètre du filament composite et se termine brusquement avec une épaisseur réduite.
- Filé de filament composite étiré selon la revendication 1, qui ne contient pas plus de 500 yeux de poissons/kilo de filé.
- Filé de filament composite selon la revendication 1, dont le rétrécissement dans l'eau bouillante est compris entre 5 et 30 %.
- Procédé de fabrication d'un filé de filament composite par extrusion simultanée de composants en polyamide et en polyuréthane, fondus, à travers l'orifice d'une filière passant par un tube vertical, procédé comprenant le fait d'insérer obliquement un courant de composant polyuréthane fondu, provenant d'en haut et d'incorporer ainsi excentriquement ledit courant de composant polyuréthane dans un courant de composant en polyamide fondu qui s'écoule vers le bas dans ledit conduit, tandis qu'une petite partie dudit courant de composant polyuréthane, projetée radialement dans une largeur rétrécie, pénètre à travers la partie la plus mince dudit courant de composant polyamide et s'écoule vers le bas le long de la paroi intérieure dudit tube, afin de former une partie rétrécie en polyuréthane immédiatement avant d'être extrudée à travers l'orifice de ladite filière,
et comprenant l'étape faisant passer les composants de polymère fondus, associés, avant l'extrusion, successivement à travers un rétrécissement et un tube dilaté. - Procédé selon la revendication 9, dans lequel le composant polyamide a une viscosité relative comprise entre 2,0 et 2,6, déterminée dans 10 mg/ml de solution d'acide sulfurique à 95,7 % et le composant polyuréthane a une viscosité à l'état fondu, à 210°C, comprise entre 2000 et 5000 Pa.s (20 000 et 50 000 poises).
- Filière pour la fabrication d'un filé de filament composites comprenant un composant de gaine en polyamide et un composant d'âme en polyuréthane disposé excentriquement dans ledit composant de gaine en polyamide, dans la section transversale d'un filament unitaire, ledit composant d'âme en polyuréthane étant exposé pratiquement dans une largeur uniforme sur la surface du filament par l'intermédiaire d'une portion rétrécie de polyuréthane s'étendant radialement dudit composant d'âme en polyuréthane et pénétrant dans la partie la plus mince dudit composant de gaine en polyamide, ladite filière comprenant un conduit d'amenée (1) pour le composant en polyamide, relié à un orifice (3) par l'intermédiaire d'un tube vertical (2), comprenant également un autre conduit d'amenée (4) pour le composant en polyuréthane, relié à un tuyau d'injection (5) qui s'étend obliquement à partir du conduit (4) et qui pénètre et fait saillie dans ledit tube (2) qui s'ouvre immédiatement au-dessus dudit orifice (3) et ledit tuyau d'injection (5) comporte une fente (6) qui s'étend longitudinalement et en-dessous de toute la longueur faisant saillie.
- Filière selon la revendication 11, dans laquelle le diamètre intérieur du tuyau d'injection est compris entre 30 % et 80 % du diamètre intérieur du tube.
- Filière selon la revendication 11, dans laquelle la fente du tuyau d'injection, sur une figure projetée sur un plan horizontal, a une longueur comprise entre 2 % et 20 % du diamètre intérieur du tube, et dont la largeur est comprise entre 0,2 % et 10 % de la circonférence du tube.
- Filière selon la revendication 11, dans laquelle le tube comporte une partie rétrécie (7) entre l'ouverture du tuyau d'injection et l'orifice.
- Filière selon la revendication 14, dans laquelle le tube s'élargit en s'écartant de la partie rétrécie vers l'orifice.
- Filière selon la revendication 16, dans laquelle le diamètre de l'alésage de la partie rétrécie est compris entre 0,20 mm et 0,45 mm, et le diamètre de l'orifice est compris entre 0,5 mm et 0,7 mm.
- Filière selon la revendication 17, dans laquelle le diamètre d'alésage de la partie rétrécie est compris entre 0,25 mm et 0,40 mm.
- Article de bonneterie comprenant un filé de filament étiré, selon la revendication 1, dans lequel le filé étiré présente un rétrécissement dans l'eau bouillante compris entre 5 % et 30 %.
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP529989 | 1989-01-12 | ||
JP5299/89 | 1989-01-12 | ||
JP89324089A JPH02277821A (ja) | 1989-01-12 | 1989-12-15 | ポリウレタン系複合繊維延伸糸及びその製造方法 |
JP324089/89 | 1989-12-15 | ||
JP1328213A JPH03193915A (ja) | 1989-12-20 | 1989-12-20 | 複合繊維及びその製造方法 |
JP328213/89 | 1989-12-20 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0378194A2 EP0378194A2 (fr) | 1990-07-18 |
EP0378194A3 EP0378194A3 (en) | 1990-10-31 |
EP0378194B1 true EP0378194B1 (fr) | 1996-04-10 |
Family
ID=27276692
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90100443A Expired - Lifetime EP0378194B1 (fr) | 1989-01-12 | 1990-01-10 | Fil de filaments composés, procédé et filière pour leur fabrication |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0378194B1 (fr) |
DE (2) | DE378194T1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004004251A1 (de) * | 2004-01-21 | 2005-08-18 | Klaus Dr. Rennebeck | Faseranordnung |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5603888A (en) * | 1995-07-13 | 1997-02-18 | Dow Corning Corporation | Method of making fibers |
US5972502A (en) * | 1998-03-04 | 1999-10-26 | Optimer, Inc. | Self-crimping fibers and methods for their preparation |
CN109338486A (zh) * | 2018-12-20 | 2019-02-15 | 常州纺兴精密机械有限公司 | 一种共轭复合纤维及其纺制组件 |
CN110016732A (zh) * | 2019-03-15 | 2019-07-16 | 东华大学 | 一种三维卷曲低熔点聚酯纤维及其制备方法 |
CN115896965A (zh) * | 2022-11-16 | 2023-04-04 | 中纺院(浙江)技术研究院有限公司 | 一种偏心皮芯型锦氨复合全牵伸丝及其制备方法 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3607611A (en) * | 1967-12-21 | 1971-09-21 | Kanegafuchi Spinning Co Ltd | Composite filament having crimpability and latent adhesivity |
GB1316434A (en) * | 1969-07-02 | 1973-05-09 | Ici Ltd | Conjugate filaments |
GB1518500A (en) * | 1975-10-24 | 1978-07-19 | Courtaulds Ltd | Bicomponent filaments |
JPS63256719A (ja) * | 1987-04-13 | 1988-10-24 | Kanebo Ltd | ポリウレタン系複合繊維 |
-
1990
- 1990-01-10 DE DE199090100443T patent/DE378194T1/de active Pending
- 1990-01-10 DE DE69026393T patent/DE69026393T2/de not_active Expired - Lifetime
- 1990-01-10 EP EP90100443A patent/EP0378194B1/fr not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004004251A1 (de) * | 2004-01-21 | 2005-08-18 | Klaus Dr. Rennebeck | Faseranordnung |
Also Published As
Publication number | Publication date |
---|---|
EP0378194A3 (en) | 1990-10-31 |
DE69026393D1 (de) | 1996-05-15 |
EP0378194A2 (fr) | 1990-07-18 |
DE69026393T2 (de) | 1996-09-19 |
DE378194T1 (de) | 1991-06-13 |
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