WO2024214591A1 - Polytrimethylene terephthalate fiber, method for producing same, air-mixed filament yarn containing said polytrimethylene terephthalate fiber, and fabric composed thereof - Google Patents
Polytrimethylene terephthalate fiber, method for producing same, air-mixed filament yarn containing said polytrimethylene terephthalate fiber, and fabric composed thereof Download PDFInfo
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- WO2024214591A1 WO2024214591A1 PCT/JP2024/013587 JP2024013587W WO2024214591A1 WO 2024214591 A1 WO2024214591 A1 WO 2024214591A1 JP 2024013587 W JP2024013587 W JP 2024013587W WO 2024214591 A1 WO2024214591 A1 WO 2024214591A1
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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
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- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/02—Yarns or threads characterised by the material or by the materials from which they are made
- D02G3/04—Blended or other yarns or threads containing components made from different materials
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- the present invention relates to a fiber substantially made of polytrimethylene terephthalate, which can be used to produce raw yarn for fabrics having a small shrinkage rate due to heating and a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made of the same.
- Polytrimethylene terephthalate (hereinafter sometimes referred to as PPT) has properties similar to polyamide, such as excellent elastic recovery and dyeability, as well as properties similar to polyethylene terephthalate, such as light resistance, heat setting, dimensional stability, and low water absorption, and so taking advantage of these characteristics, it has been proposed to be used in many fields, such as BCF carpets and brushes (for example, JP-A-9-3724, JP-A-8-173244, JP-A-5-262862, etc.). Furthermore, because polytrimethylene terephthalate fiber has a low Young's modulus, it is said that products with a soft feel can be obtained.
- Patent Document 1 discloses a method in which polytrimethylene terephthalate polymer with an intrinsic viscosity [ ⁇ ] of 0.7 or more is taken up at a spinning speed of 3000 m/min, and is subsequently drawn at 70°C without being wound up, and then is continuously subjected to a relaxation heat treatment at a relaxation rate of 6-20%.
- polytrimethylene terephthalate fibers proposed so far do indeed have a lower Young's modulus than polyethylene terephthalate fibers, when these are made into fabrics, the properties are not fully exhibited, and the softness has not yet been fully satisfactory.
- Patent Document 2 discloses that polytrimethylene terephthalate fiber with a soft texture can be obtained by winding at a spinning speed of 4,500 m/min or more. While this method certainly produces a soft fabric, there are problems with the yarn being tightly wound due to elastic deformation of the yarn when it is wound, resulting in a poor wound shape and crushing of the wound paper tube. Furthermore, because the spinning speed is fast, the yarn is prone to breakage, making it difficult to produce a stable yarn.
- the present invention has been made in consideration of the above background, and its purpose is to provide a low-shrinkage fiber consisting essentially of polytrimethylene terephthalate, which has a small thermal shrinkage rate and can be used to produce raw yarn for fabrics with a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made from the same.
- the desired polytrimethylene terephthalate fiber can be obtained when the boiling water shrinkage rate (hereinafter sometimes referred to as the boiling water shrinkage rate) of a fiber essentially made of polytrimethylene terephthalate and the elastic modulus at an elongation of 20% of the polytrimethylene terephthalate fiber are controlled to a range different from that of the so-called straight drawn yarn or high speed spun yarn described in the above prior art documents, and thus arrived at the present invention.
- the boiling water shrinkage rate hereinafter sometimes referred to as the boiling water shrinkage rate
- a method for producing a polytrimethylene terephthalate fiber comprising melting and solidifying polytrimethylene terephthalate having 90 mol % or more of trimethylene terephthalate repeating units, winding the polytrimethylene terephthalate at a winding speed of 1000 m/min or more, stretching the polytrimethylene terephthalate by 1.1 times or more at a temperature equal to or lower than the glass transition point of the polytrimethylene terephthalate, and then shrinking the fiber by 0.5 to 0.9 times while heating the fiber. 6.
- An air-mixed yarn comprising the polytrimethylene terephthalate fiber according to any one of 1 to 4 above and a polyester fiber. 7.
- the air-mixed yarn according to 6 above in which the boiling water shrinkage rate of the polyester fiber is 7 to 50%.
- the air-mixed yarn according to 6 or 7 above which contains modified cross-section fibers;
- the mixed yarn is treated in boiling water, and then cut to a length of 5 cm under a load of 0.1 cN (0.098 g) ⁇ the total fineness (dtex) of the air-mixed yarn.
- polyester fiber A single fiber
- polytrimethylene terephthalate fiber B single fiber
- a fabric comprising the air-mixed yarn according to any one of claims 6 to 8.
- a fabric comprising the core-sheath type air-mixed yarn according to any one of claims 9 to 11 above. is provided.
- the present invention provides a low-shrinkage fiber substantially made of polytrimethylene terephthalate, which has a small heat shrinkage rate and can be used to produce raw yarn for fabrics with a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made of the same.
- FIG. 2 is a schematic diagram showing an example of the degree of modification in the modified cross-section fiber used in the present invention.
- FIG. 2 is a schematic diagram showing an example of flatness in the flat cross section fiber used in the present invention.
- the polymer used in the present invention is polytrimethylene terephthalate (hereinafter, sometimes referred to as PTT) composed of 90 mol % or more of trimethylene terephthalate repeating units.
- PTT is a polyester containing terephthalic acid as the acid component and trimethylene glycol (also called 1,3-propanediol) as the diol component.
- the PTT may contain 10 mol % or less of other copolymerization components.
- Such copolymerization components include ester-forming monomers such as 5-sodium sulfoisophthalic acid, 5-potassium sulfoisophthalic acid, 3,5-dicarboxylic acid benzenesulfonic acid tetrabutylphosphonium salt, 3,5-dicarboxylic acid benzenesulfonic acid tributylmethylphosphonium salt, 1,4-butanediol, neopentyl glycol, 1,6-hexamethylene glycol, 1,4-cyclohexanediol, 1,4-cyclohexanedimethanol, adipic acid, dodecanedioic acid, and 1,4-cyclohexanedicarboxylic acid.
- ester-forming monomers such as 5-sodium sulfoisophthalic acid, 5-potassium sulfoisophthalic acid, 3,5-dicarboxylic acid benzenesulfonic acid te
- the PTT may be copolymerized or mixed with various additives, such as matting agents, heat stabilizers, defoamers, color-adjusting agents, flame retardants, antioxidants, ultraviolet absorbers, infrared absorbers, crystal nucleating agents, and fluorescent whitening agents.
- additives such as matting agents, heat stabilizers, defoamers, color-adjusting agents, flame retardants, antioxidants, ultraviolet absorbers, infrared absorbers, crystal nucleating agents, and fluorescent whitening agents.
- the polytrimethylene terephthalate polymer used in the present invention preferably has an intrinsic viscosity [ ⁇ ] of 0.5 to 1.6, more preferably 0.6 to 1.5, and even more preferably 0.7 to 1.4.
- the intrinsic viscosity is less than 0.5, the molecular weight of the polymer is too low, making it difficult to achieve strength. On the other hand, if the intrinsic viscosity exceeds 1.6, the low fluidity impairs the spinnability of the low-viscosity polytrimethylene terephthalate, which may cause thread breakage during spinning, and this is not preferred.
- polytrimethylene terephthalate fiber of the present invention is less deformed by hot water treatment, and therefore when made into a fabric, the yarn shrinks less and has a soft texture.
- the polytrimethylene terephthalate fiber is characterized by a low elastic modulus after the first yield point in a tensile strength and elongation measurement, a fabric made using the polytrimethylene terephthalate fiber has a softer drape than that of ordinary polytrimethylene terephthalate fibers.
- the boiling water shrinkage rate of the polytrimethylene terephthalate fibers in this application (hereinafter sometimes referred to as boiling water shrinkage rate) must be 5% or less, preferably 4% or less, and more preferably 3% or less. If the boiling water shrinkage rate is greater than 5%, the fabric will become stiff due to shrinkage of the yarn caused by heat shrinkage.
- the polytrimethylene terephthalate fiber of the present invention must have an elastic modulus of 5 cN/dtex or less at an elongation of 20%, preferably 4 cN/dtex or less, and more preferably 3 cN/dtex or less. If the elastic modulus at an elongation of 20% is greater than 5 cN/dtex, the fabric will become stiff due to subsequent dyeing and other processes.
- the birefringence ⁇ n of the polytrimethylene terephthalate fiber of the present invention is preferably 0.040 or more and 0.08 or less. More preferably, the birefringence ⁇ n is 0.045 or more and 0.075 or less, and even more preferably, the birefringence ⁇ n is 0.050 or more and 0.070 or less. If the birefringence ⁇ n is less than 0.040, the thread strength is reduced and the fabric stretches due to external forces, making it difficult to maintain its shape, which is undesirable.
- the specific gravity which is an alternative index showing the degree of crystallinity of the polytrimethylene terephthalate fiber of the present invention, is preferably 1.350 or less, and more preferably 1.319 or more and 1.350 or less. If the specific gravity is less than 1.319, the yarn becomes brittle during the draw-twist processing, causing frequent yarn breakage and making the draw-twist processing difficult. On the other hand, if the specific gravity is greater than 1.350, it is not preferable because a lot of fluff occurs.
- the thermal stress peak of the polytrimethylene terephthalate fiber of the present invention exists at 50°C to 100°C. If the peak exists at a temperature lower than 50°C, the heat resistance will be low, which is not preferable. Also, if the peak exists at a temperature higher than 100°C, the degree of crystallization will be too high, and soft drapeability will be lost, which is not preferable.
- the peak value of the thermal stress of the polytrimethylene terephthalate fiber of the present invention is 0.2 cN/dtex or less. If the peak value of the thermal stress is greater than 0.2 cN/dtex, deformation due to hot water treatment such as dyeing will be large, and when made into a fabric, the yarn will shrink and have a hard texture, which is not preferable.
- the breaking strength of the polytrimethylene terephthalate fiber of the present invention is 1.5 cN/dtex or more to 3.5 cN/dtex, preferably 1.7 cN/dtex to 3.3 cN/dtex, and more preferably 2.0 cN/dtex to 3.0 cN/dtex.
- breaking strength of the polytrimethylene terephthalate fiber is less than 1.5 cN/dtex, the durability of the product will decrease, which is not preferable. Also, if the breaking strength of the polytrimethylene terephthalate fiber is more than 3.5 cN/dtex, the degree of crystallinity will be too high, and the product will lose its soft drapeability, which is not preferable.
- the breaking elongation of polytrimethylene terephthalate fiber is preferably 30% to 100%. If the breaking elongation of polytrimethylene terephthalate fiber is less than 30%, the degree of crystallinity will be too high, and flexible drapeability will be lost, which is not preferred. On the other hand, if the breaking elongation of polytrimethylene terephthalate fiber is more than 100%, the fiber will stretch when a load is applied to it, and dimensional stability will be poor, which is not preferred.
- polytrimethylene terephthalate fibers as described above can be produced, for example, by the following method. First, polytrimethylene terephthalate composed of 90 mol % or more of trimethylene terephthalate repeating units is melted and solidified, and then wound up at a winding speed of 1000 m/min or more. Then, it is heated with a heating roller at a temperature of ⁇ 20°C of the glass transition point of polytrimethylene terephthalate, and then stretched 1.0 to 2.0 times. Then, it is wound around a heating roller at a temperature of 50 to 150°C, and then temporarily wound into a cheese-like package at a speed of 2000 to 4800 m/min.
- the polytrimethylene terephthalate fiber with a breaking elongation of 50 to 200% wound into a cheese-shaped package in this way is stretched by 1.1 times or more at a temperature below the glass transition point of the polytrimethylene terephthalate, and then the fiber is shrunk by 0.5 to 0.9 times while heating, thereby obtaining polytrimethylene terephthalate fiber that has little shrinkage due to heat and can be made into a fabric with a soft texture.
- the total stretch ratio which is expressed as the product of the stretch ratio at a temperature below the glass transition point and the shrinkage ratio while heating, is preferably 0.9 to 1.25 times, and more preferably 0.95 to 1.20 times. If the total stretch ratio is less than 0.90 times, the yarn will slacken and the yarn will not run stably during stretching, which may cause yarn breakage, and this is not preferred. Also, if the total stretch ratio is more than 1.25 times, the shrinkage rate of the yarn will be too high, and the fabric may not have a soft texture when made into a fabric, which is also not preferred.
- polytrimethylene terephthalate fibers that have been melted and solidified and have a breaking elongation of 50 to 200% can also be produced by winding the fibers at a spinning speed of 1000 m/min or more, followed by drawing them at a low ratio of 1.0 to 2.0 times at a temperature of ⁇ 20°C above the glass transition point of polytrimethylene terephthalate.
- the high-elongation polytrimethylene terephthalate fiber obtained in this manner desirably has a breaking elongation of 50 to 200% or more. More preferably, it is 60 to 190%, and even more preferably, it is 70 to 180%.
- the breaking elongation of the high-elongation polytrimethylene terephthalate fiber is less than 50%, the fiber will be highly crystallized, and it will not be possible to make a fabric with a soft feel, which is not preferred.
- the breaking elongation is greater than 200%, crystallization will not progress when stretched at a temperature below the glass transition point, resulting in significantly lower strength and lower durability when made into a fabric, which is also not preferred.
- the polytrimethylene terephthalate fiber that has been melted and solidified is stretched at a temperature below the glass transition point of polytrimethylene terephthalate, more preferably at a temperature below the glass transition point -5°C, and even more preferably at a temperature below the glass transition point -10°C, by 1.1 times or more, more preferably 1.2 times or more, and even more preferably 1.3 times or more.
- the degree of crystallinity will be high, and it will not be possible to produce a fabric with a soft feel, which is not preferred. Also, if the material is stretched at a ratio lower than 1.1, the durability of the fabric will be low, which is also not preferred.
- the stretched fibers are not yet crystallized and the polymers are highly oriented, their dimensional stability due to heat is low. Therefore, by shrinking the fibers by a factor of 0.5 to 0.9 while heating, the dimensional stability and durability can be improved.
- the fiber shrinkage is less than 0.5 times, the degree of orientation crystallinity of the resulting polytrimethylene terephthalate fiber will be too low, and the durability of the fabric will be low when it is made into a fabric, which is not preferred. Also, if the fiber shrinkage is more than 0.9 times, the degree of crystallinity will be too high, and it will not be possible to make a fabric with a soft feel, which is also not preferred.
- Polyester fiber for core thread
- the polytrimethylene terephthalate fiber and the polyester fiber are mixed by air processing to obtain an air-mixed yarn.
- polyester fibers used in this case are preferably exemplified by fibers spun and drawn by a conventional method, such as polytrimethylene terephthalate (PTT) fibers, polyethylene terephthalate (PET) fibers, side-by-side or eccentric core-sheath type composite fibers of polytrimethylene terephthalate and polyethylene terephthalate, side-by-side or eccentric core-sheath type composite fibers of polytrimethylene terephthalate and polytrimethylene terephthalate, side-by-side or eccentric core-sheath type composite fibers of polyethylene terephthalate and polyethylene terephthalate, etc.
- PTT polytrimethylene terephthalate
- PET polyethylene terephthalate
- side-by-side or eccentric core-sheath type composite fibers of polytrimethylene terephthalate and polyethylene terephthalate side-by-side or eccentric core-sheath type composite fibers of polyethylene terephthalate
- the boiling water shrinkage rate is 7 to 50% in order to increase the yarn length difference between the core yarn and the sheath yarn by subjecting the air-mixed yarn to a heat treatment or the like.
- the polytrimethylene terephthalate fiber as the sheath yarn and the polyester fiber as the core yarn are aligned, intertwined (preferably 30 to 150 pieces/m) by air processing (interlace or Taslan (registered trademark)), and taken up by a roller to obtain an air-mixed yarn.
- the overfeed rate during air-mixing processing is preferably 0.5 to 2%.
- the air-mixed yarn of the present invention may contain fibers with irregular cross sections other than a circular cross section.
- it may be composed of fibers with irregular cross sections such as cross-shaped, triangular, or star-shaped cross sections, which can provide a unique texture.
- flat cross-section fibers are also exemplified as modified cross-section fibers.
- the use of flat cross-section fibers is preferable because it allows for a unique texture to be obtained.
- the air-mixed yarn thus obtained can be a sheath-core air-mixed yarn with a large thread length difference between the core and sheath, using a low-shrinkage fiber made of polytrimethylene terephthalate, which has a soft texture, as the sheath yarn.
- the air-mixed yarn is subjected to a heat treatment such as dyeing processing, whereby the polytrimethylene terephthalate fiber becomes a sheath yarn and the polyester-based fiber becomes a core yarn, thereby forming a core-sheath type air-mixed yarn containing a core yarn and a sheath yarn.
- the total fineness must be 30 to 400 dtex, and more preferably 50 to 200 dtex. If the total fineness is less than 30 dtex, the total fineness is too fine and air-mixing processing may be difficult. On the other hand, if the total fineness is more than 400 dtex, the softness of the fabric may be lost.
- the number of single fibers (filaments) is preferably 40 to 400 (more preferably 40 to 200).
- the yarn length difference between the core yarn and the sheath yarn is 5% or more (more preferably 6-40%). If the yarn length difference is less than 5%, a sufficient sense of volume cannot be obtained.
- LA is the yarn length (cm) of the polyester fiber core yarn
- LB is the yarn length (cm) of the polytrimethylene terephthalate fiber sheath yarn.
- the polytrimethylene terephthalate fiber of the sheath yarn is 50 to 90% (more preferably 60 to 80%) of the weight of the mixed yarn. If the weight ratio of the polytrimethylene terephthalate fiber of the sheath yarn is 50% or less, not only will a soft feel not be obtained, but the dyeing difference between the core yarn and the sheath yarn may become more visible.
- fabric (grey fabric) is obtained by knitting and weaving the above-mentioned air-mixed yarn, and then dyeing and sweat absorbing are appropriately performed to obtain a fabric as a product. At that time, the yarn length difference between the sheath yarn and the core yarn of the mixed yarn appears by the heat treatment of the dyeing process, and the fabric is made of sheath-core air-mixed yarn.
- the fabric may be made of only the sheath-core air-mixed yarn, but it may also be made of the sheath-core air-mixed yarn and other yarns.
- the other yarns are not particularly limited and may be any of non-crimped yarns, false-twisted crimped yarns, latent crimped yarns, spun yarns, etc.
- the structure of the fabric is not particularly limited, and it may be either knitted or woven. Examples include knitted fabrics with knitting structures such as plain weave, knit miss, smooth, rib, pique, plaited knit, denby, and half, and woven fabrics with weaving structures such as plain weave, twill, and satin, but are not limited to these.
- the number of layers may be a single layer or multiple layers of two or more layers.
- the fabric may be used to make textile products such as sportswear, outerwear, innerwear, men's clothing, women's clothing, nursing clothing, workwear, car seat covering materials, and bedding. Since such fabrics and textile products use the air-mixed yarn, they have a soft feel and excellent fluffiness.
- the glass transition point was measured from a temperature rise curve obtained by sealing a specified amount of polymer chips in an aluminum sample pan and heating the chips from room temperature to 300° C. at a heating rate of 10° C./min in a nitrogen atmosphere using a DSC.
- Fineness fineness of multifilament yarn
- JIS-L-1013 The fineness of the multifilament yarn was measured in accordance with JIS-L-1013. The measured value was divided by the number of single yarns in the multifilament yarn to determine the single yarn fineness.
- Breaking strength and breaking elongation Based on JIS-L-1013, measurements were made using a constant speed extension tensile tester, Tensilon manufactured by Orientec Co., Ltd., at a gripping distance of 20 cm and a pulling speed of 20 cm/min.
- Example 1 Dimethyl terephthalate and 1,3-propanediol were charged in a molar ratio of 1:2, and titanium tetrabutoxide equivalent to 0.1% by weight of dimethyl terephthalate was added, and the transesterification reaction was completed under normal pressure at a heater temperature of 240° C. Next, titanium tetrabutoxide was further added in an amount of 0.1% by weight of the theoretical polymer amount, and titanium dioxide was added in an amount of 0.5% by weight of the theoretical polymer amount, and the reaction was carried out at 270° C. for 3 hours.
- the resulting polymer was composed of 100 mol % trimethylene terephthalate repeating units, had an intrinsic viscosity of 1.0 dl/g, and had a glass transition point of 51° C.
- the resulting polymer was dried in a conventional manner to reduce the water content to 50 ppm, then melted at 265° C. and extruded through a single-row spinneret having 36 holes with a diameter of 0.27 mm.
- the extruded molten multifilament was quenched by blowing air at a speed of 4.0 m/min to convert it into a solid multifilament, after which a 10% water emulsion finishing agent containing 60% by weight of octyl stearate, 15% by weight of polyoxyethylene alkyl ether, and 3% by weight of potassium phosphate was applied using a guide nozzle so that the amount of oil applied to the fiber was 0.6% by weight.
- the solid multifilament was then wound around a roll heated to 50°C with a peripheral speed of 2100 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.3 times. It was then wound at a winding speed of 2600 m/min using a winding machine that drives both the spindle and the touch roll, to obtain a cheese-like package wound with 72 dtex/36 filament fibers.
- the fiber wound on the package was stretched to 1.5 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.7 times.
- the fiber was then wound at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
- a polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 10%) was prepared as a core yarn.
- the sheath yarn and core yarn were then aligned and interlaced at an overfeed rate of 1.5% to obtain an air-mixed yarn with an entanglement rate of 69 entanglements/m.
- the physical properties of the resulting polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- Example 2 A polymer was produced in the same manner as in Example 1, and the polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a double-arranged spinneret having 72 holes with a diameter of 0.23 mm.
- the solid multifilament was wound around a roll heated to 50°C and having a peripheral speed of 2100 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.3 times.Then, using a winder that drives both the spindle and the touch roll, the multifilament was wound at a winding speed of 2600 m/min to obtain a cheese-like package wound with 72 dtex/72 filament fibers.
- the fiber wound on the package was stretched to 1.4 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.75 times, and then wound up at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
- a polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 13%) was prepared as a core yarn.
- Example 2 The sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn with an entanglement rate of 71 entanglements/m.
- the physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- Example 3 A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
- the solid multifilament was wound around a roll heated to 50°C and having a peripheral speed of 2350 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.1 times.Then, using a winder that drives both the spindle and the touch roll, the winding was performed at a winding speed of 2600 m/min to obtain a cheese-like package wound with 72 dtex/36 filament fibers.
- the fiber wound on the package was stretched to 1.6 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.65 times, and then wound up at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
- a conjugate drawn yarn (total fineness 56 dtex/24 strands, boiling water shrinkage rate 17%) made by bonding two components of polyester (polyethylene terephthalate/polyethylene terephthalate) was prepared as a core yarn.
- Example 2 The sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn with an entanglement rate of 65/m.
- the physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- Example 4 A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
- the solid multifilament was wound around a roll heated to 50°C and having a peripheral speed of 3000 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.2 times.Then, using a winder that drives both the spindle and the touch roll, the winding was performed at a winding speed of 3600 m/min to obtain a cheese-like package wound with 56 dtex/36 filament fibers.
- the fiber wound on the package was stretched to 1.3 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.85 times, and then wound up at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
- a conjugate drawn yarn (total fineness 33 dtex/24 strands, boiling water shrinkage rate 21%) made by bonding together polyethylene terephthalate and polytrimethylene terephthalate was prepared as a core yarn.
- Example 2 The sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn with an entanglement rate of 71 entanglements/m.
- the physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- Examples 5 to 6 The same procedure as in Example 1 was carried out, except that the cross-sectional shape of the sheath yarn and the number of single fibers were changed as shown in Table 1.
- the physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- Example 1 A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
- Example 2 An oil agent was applied to the extruded molten multifilament in the same manner as in Example 1, and the solid multifilament was then wound around a roll heated to 55° C. and having a peripheral speed of 1,500 m/min, and then wound around a roll heated to 130° C. so as to be stretched 2.1 times. Thereafter, the solid multifilament was wound at a winding speed of 3,000 m/min using a winder that drives both the spindle and the touch roll, to obtain a cheese-like package wound with a fiber of 72 dtex/36 filaments (polytrimethylene terephthalate fiber yarn for sheath yarn). On the other hand, polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 12%) was prepared as a core yarn.
- polyester (polyethylene terephthalate) drawn yarn total fineness 56 dtex/36 strands, boiling water shrinkage rate 12%) was prepared as a
- Example 2 the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn having an entanglement number of 65/m.
- the physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- the air-mixed yarn obtained had a small core-sheath yarn length difference and was poor in swelling.
- Example 2 A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
- the solid multifilament was wound around a roll heated to 55°C and having a peripheral speed of 1500 m/min, and then wound around a roll heated to 130°C so that it was stretched 2.1 times.Then, using a winder that drives both the spindle and the touch roll, the winding was performed at a winding speed of 3000 m/min to obtain a cheese-like package wound with 56 dtex/36 filament fibers.
- the fiber wound on the package was stretched to 1.05 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.92 times, and then wound up at a speed of 600 m/min to obtain tritrimethylene terephthalate fiber (yarn for sheath yarn).
- a polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 10%) was prepared as a core yarn.
- Example 2 the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn having an entanglement number of 63/m.
- the physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
- the air-mixed yarn obtained had a stiff sheath yarn and was poor in feel.
- the present invention provides a low-shrinkage fiber essentially made of polytrimethylene terephthalate, which has a small thermal shrinkage rate and can be used to produce raw yarn for fabrics with a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made from the same, and therefore has great industrial value.
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Abstract
Description
本発明は、加熱による収縮率が小さく、やわらかな風合いを有する布帛用の原糸を作製することができる、実質的にポリトリメチレンテレフタレートからなる繊維及びその製造方法、並びに該ポリトリメチレンテレフタレート繊維を含む空気混繊糸、及びそれからなる布帛に関するもの
である。
The present invention relates to a fiber substantially made of polytrimethylene terephthalate, which can be used to produce raw yarn for fabrics having a small shrinkage rate due to heating and a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made of the same.
ポリトリメチレンテレフタレート(以下、PPTと称する場合がある)は、弾性回復性や染色性に優れるといったポリアミドに類似した性質、並びに耐光性、熱セット性、寸法安定性、低吸水率といったポリエチレンテレフタレートに類似した性質を併せ持つことから、これらの特徴を生かしてBCFカーペット、ブラシ等の多くの分野への利用が提案されている(例えば、特開平9-3724号公報、特開平8-173244号公報、特開平5-262862号公報など)。さらに、ポリトリメチレンテレフタレート繊維は、低ヤング率であるため、ソフトな風合の製品が得られるとされている。 Polytrimethylene terephthalate (hereinafter sometimes referred to as PPT) has properties similar to polyamide, such as excellent elastic recovery and dyeability, as well as properties similar to polyethylene terephthalate, such as light resistance, heat setting, dimensional stability, and low water absorption, and so taking advantage of these characteristics, it has been proposed to be used in many fields, such as BCF carpets and brushes (for example, JP-A-9-3724, JP-A-8-173244, JP-A-5-262862, etc.). Furthermore, because polytrimethylene terephthalate fiber has a low Young's modulus, it is said that products with a soft feel can be obtained.
また、ポリトリメチレンテレフタレート繊維を製造する方法については、300~4000m/分で溶融紡糸した未延伸糸を、一旦巻取った後又は巻取ることなく連続して、未延伸糸のガラス転移温度以上の温度で一段又は多段に熱延伸する方法が提案されている。そして、その際の紡糸・延伸条件として、例えば、特開2001-207329号公報(特許文献1)には、極限粘度[η]が0.7以上のポリトリメチレンテレフタレートポリマーを紡糸速度3000m/分で引き取り、一旦巻き取ることなく引き続き70℃で延伸した後、連続して弛緩率6~20%で弛緩熱処理を施す方法が開示されている。 Furthermore, a method has been proposed for producing polytrimethylene terephthalate fibers in which undrawn yarns melt-spun at 300-4000 m/min are hot-drawn in one or multiple stages at a temperature equal to or higher than the glass transition temperature of the undrawn yarn, either after being wound up or continuously without being wound up. As spinning and drawing conditions for this process, for example, JP 2001-207329 A (Patent Document 1) discloses a method in which polytrimethylene terephthalate polymer with an intrinsic viscosity [η] of 0.7 or more is taken up at a spinning speed of 3000 m/min, and is subsequently drawn at 70°C without being wound up, and then is continuously subjected to a relaxation heat treatment at a relaxation rate of 6-20%.
しかしながら、従来提案されているポリトリメチレンテレフタレート繊維は、確かにポリチレンテレフタレート繊維と比較して低ヤング率であるものの、これを布帛とした場合、その特性が充分に発揮されず、ソフト性の点でまだ充分満足のいくものが得られていない。 However, although the polytrimethylene terephthalate fibers proposed so far do indeed have a lower Young's modulus than polyethylene terephthalate fibers, when these are made into fabrics, the properties are not fully exhibited, and the softness has not yet been fully satisfactory.
一方、特開2001-348729号公報(特許文献2)には、紡糸速度4500m/min以上の速度で捲き取ることにより、やわらかな風合いのポリトリメチレンテレフタレート繊維が得られることが開示されている。確かにこの方法ではソフトな布帛となるが、糸の捲き取り時糸の弾性変形で捲き締まりが生じ、巻形状が悪く、巻き取った紙管がつぶれてしまうなどの問題があった。さらに、紡糸速度が速いため糸切れしやすく、安定した糸の製造は困難であった。 On the other hand, Japanese Patent Application Laid-Open No. 2001-348729 (Patent Document 2) discloses that polytrimethylene terephthalate fiber with a soft texture can be obtained by winding at a spinning speed of 4,500 m/min or more. While this method certainly produces a soft fabric, there are problems with the yarn being tightly wound due to elastic deformation of the yarn when it is wound, resulting in a poor wound shape and crushing of the wound paper tube. Furthermore, because the spinning speed is fast, the yarn is prone to breakage, making it difficult to produce a stable yarn.
本発明は上記の背景に鑑みなされたものであり、その目的は、熱による収縮率が小さく、やわらかな風合いを有する布帛用の原糸を製造することが可能な、実質的にポリトリメチレンテレフタレートからなる低収縮繊維及びその製造方法、並びに該ポリトリメチレンテレフタレート繊維を含む空気混繊糸、及びそれからなる布帛を提供することにある。 The present invention has been made in consideration of the above background, and its purpose is to provide a low-shrinkage fiber consisting essentially of polytrimethylene terephthalate, which has a small thermal shrinkage rate and can be used to produce raw yarn for fabrics with a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made from the same.
本発明者らは上記課題を解決するために鋭意研究した結果、実質的にポリトリメチレンテレフタレートからなる繊維の沸騰水収縮率(以下、沸水収縮率と称する場合がある)と、該ポリトリメチレンテレフタレート繊維の伸度20%における弾性率を、上記先行技術文献に記載の、いわゆる直延糸や高速紡糸糸とは異なる範囲に制御するとき、所望のポリトリメチレンテレフタレート繊維が得られることを見出し、本発明に到達した。 As a result of intensive research conducted by the inventors to solve the above problems, they discovered that the desired polytrimethylene terephthalate fiber can be obtained when the boiling water shrinkage rate (hereinafter sometimes referred to as the boiling water shrinkage rate) of a fiber essentially made of polytrimethylene terephthalate and the elastic modulus at an elongation of 20% of the polytrimethylene terephthalate fiber are controlled to a range different from that of the so-called straight drawn yarn or high speed spun yarn described in the above prior art documents, and thus arrived at the present invention.
かくして、本発明によれば、
1.90モル%以上がトリメチレンテレフタレート繰返単位から構成されるポリトリメチレンテレフタレート繊維であって、該ポリトリメチレンテレフタレート繊維の沸騰水収縮率が5%以下で、且つ該ポリトリメチレンテレフタレート繊維の伸度20%における弾性率が5cN/dtex以下であることを特徴とするポリトリメチレンテレフタレート繊維、
2.ポリトリメチレンテレフタレート繊維の複屈折率Δnが0.040以上であり、比重が1.350以下である上記1記載のポリトリメチレンテレフタレート繊維、
3.ポリトリメチレンテレフタレート繊維の熱応力のピークが50~100℃に存在し、且つ熱応力のピーク値が0.2cN/dtex以下である上記1又は2に記載のポリトリメチレンテレフタレート繊維、
4.ポリトリメチレンテレフタレート繊維の破断強度が1.5~3.5cN/dtexであり、且つ破断伸度が30~100%である上記1又は2に記載のポリトリメチレンテレフタレート繊維、
5.90モル%以上がトリメチレンテレフタレート繰返し単位から構成されるポリトリメチレンテレフタレートを溶融固化し、1000m/分以上の巻取り速度で巻き取った後、該ポリトリメチレンテレフタレートのガラス転移点以下の温度で1.1倍以上延伸し、次いで加熱しながら、0.5~0.9倍の倍率で繊維を収縮させることを特徴とするポリトリメチレンテレフタレート繊維の製造方法、
6.上記1~4のいずれか1項に記載のポリトリメチレンテレフタレート繊維と、ポリエステル系繊維とを含むことを特徴とする空気混繊糸、
7.ポリエステル系繊維の沸騰水収縮率が7~50%である上記6に記載の空気混繊糸、
8.異型断面繊維を含む、上記6又は7に記載の空気混繊糸、
9.上記6に記載の空気混繊糸を加熱処理してなる、芯糸と鞘糸とから構成される、総繊度が30~400dtexの空気混繊糸であって、該芯糸がポリエステル系繊維からなり、該鞘糸が、単繊維繊度が0.3~10dtexのポリトリメチレンテレフタレート繊維からなり、且つ、下記方法で定義する該芯糸と該鞘糸との糸足差が5%以上であることを特徴とする芯鞘型空気混繊糸、
(糸足差の測定方法)
混繊糸を沸騰水下にて処理した後、0.1cN(0.098g)×空気混繊糸の総繊度(dtex)の荷重をとりつけて5cmの長さにカットし、カットした空気混繊糸から、ポリエステル系繊維A(単繊維)とポリトリメチレンテレフタレート繊維B(単繊維)とを取り出し、それぞれ、0.1cN(0.098g)×の単繊維繊度(dtex)の荷重をかけて長さを測定し、下記式により糸足差(%)を算出する、
糸足差(%)=(LB-LA)/LA×100
ただし、LAは芯糸のポリエステル系繊維の糸長(cm)であり、LBは鞘糸のポリトリメチレンテレフタレート繊維の糸長(cm)である、
10.鞘糸の重量比率が芯鞘型空気混繊糸全重量に対し、50~90%である上記9に記載の芯鞘型空気混繊糸、
11.異型断面繊維を含む、上記9又は10に記載の芯鞘型空気混繊糸、
12.上記6~8のいずれか1項に記載の空気混繊糸を含む布帛、
13.上記9~11のいずれか1項に記載の芯鞘型空気混繊糸を含む布帛、
が提供される。
Thus, according to the present invention,
1. A polytrimethylene terephthalate fiber having 90 mol % or more of a trimethylene terephthalate repeat unit, the polytrimethylene terephthalate fiber having a boiling water shrinkage rate of 5% or less and an elastic modulus at an elongation of 20% of 5 cN/dtex or less.
2. The polytrimethylene terephthalate fiber according to the above item 1, wherein the polytrimethylene terephthalate fiber has a birefringence Δn of 0.040 or more and a specific gravity of 1.350 or less.
3. The polytrimethylene terephthalate fiber according to the above 1 or 2, wherein the peak of thermal stress of the polytrimethylene terephthalate fiber exists at 50 to 100° C. and the peak value of the thermal stress is 0.2 cN/dtex or less.
4. The polytrimethylene terephthalate fiber according to 1 or 2 above, wherein the polytrimethylene terephthalate fiber has a breaking strength of 1.5 to 3.5 cN/dtex and a breaking elongation of 30 to 100%.
5. A method for producing a polytrimethylene terephthalate fiber, comprising melting and solidifying polytrimethylene terephthalate having 90 mol % or more of trimethylene terephthalate repeating units, winding the polytrimethylene terephthalate at a winding speed of 1000 m/min or more, stretching the polytrimethylene terephthalate by 1.1 times or more at a temperature equal to or lower than the glass transition point of the polytrimethylene terephthalate, and then shrinking the fiber by 0.5 to 0.9 times while heating the fiber.
6. An air-mixed yarn comprising the polytrimethylene terephthalate fiber according to any one of 1 to 4 above and a polyester fiber.
7. The air-mixed yarn according to 6 above, in which the boiling water shrinkage rate of the polyester fiber is 7 to 50%.
8. The air-mixed yarn according to 6 or 7 above, which contains modified cross-section fibers;
9. An air-mixed core-sheath type air-mixed yarn having a total fineness of 30 to 400 dtex, which is obtained by heat-treating the air-mixed yarn described in 6 above and is composed of a core yarn and a sheath yarn, the core yarn being made of a polyester fiber, the sheath yarn being made of a polytrimethylene terephthalate fiber having a single fiber fineness of 0.3 to 10 dtex, and the yarn length difference between the core yarn and the sheath yarn, as defined by the following method, is 5% or more.
(Method of measuring thread length difference)
The mixed yarn is treated in boiling water, and then cut to a length of 5 cm under a load of 0.1 cN (0.098 g) × the total fineness (dtex) of the air-mixed yarn. From the cut air-mixed yarn, polyester fiber A (single fiber) and polytrimethylene terephthalate fiber B (single fiber) are taken out, and their lengths are measured under a load of 0.1 cN (0.098 g) × the single fiber fineness (dtex). The yarn length difference (%) is calculated according to the following formula:
Thread length difference (%) = (LB-LA)/LA x 100
where LA is the yarn length (cm) of the polyester fiber core yarn, and LB is the yarn length (cm) of the polytrimethylene terephthalate fiber sheath yarn.
10. The sheath-core air-mixed yarn according to claim 9, wherein the weight ratio of the sheath yarn is 50 to 90% of the total weight of the sheath-core air-mixed yarn.
11. The core-sheath type air-mixed yarn according to 9 or 10 above, which contains a modified cross-section fiber.
12. A fabric comprising the air-mixed yarn according to any one of claims 6 to 8.
13. A fabric comprising the core-sheath type air-mixed yarn according to any one of claims 9 to 11 above.
is provided.
本発明によれば、熱による収縮率が小さく、やわらかな風合いを有する布帛用の原糸を製造することが可能な、実質的にポリトリメチレンテレフタレートからなる低収縮繊維及びその製造方法、並びに該ポリトリメチレンテレフタレート繊維を含む空気混繊糸、及びそれからなる布帛を提供することができる。 The present invention provides a low-shrinkage fiber substantially made of polytrimethylene terephthalate, which has a small heat shrinkage rate and can be used to produce raw yarn for fabrics with a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made of the same.
以下、本発明について詳細を説明する。
(1)ポリマー原料
本発明に用いるポリマーは、90モル%以上がトリメチレンテレフタレート繰返し単位から構成されるポリトリメチレンテレフタレート(以下、PTTと称する場合がある)である。ここでPTTとは、テレフタル酸を酸成分とし、トリメチレングリコール(1,3-プロパンジオールともいう)をジオール成分としたポリエステルである。該PTTは、10モル%以下で他の共重合成分を含有していてもよい。
The present invention will be described in detail below.
(1) Polymer Raw Material The polymer used in the present invention is polytrimethylene terephthalate (hereinafter, sometimes referred to as PTT) composed of 90 mol % or more of trimethylene terephthalate repeating units. Here, PTT is a polyester containing terephthalic acid as the acid component and trimethylene glycol (also called 1,3-propanediol) as the diol component. The PTT may contain 10 mol % or less of other copolymerization components.
そのような共重合成分としては、5-ナトリウムスルホイソフタル酸、5-カリウムスルホイソフタル酸、3,5-ジカルボン酸ベンゼンスルホン酸テトラブチルホスホニウム塩、3,5-ジカルボン酸ベンゼンスルホン酸トリブチルメチルホスホニウム塩、1,4-ブタンジオール、ネオペンチルグリコール、1,6-ヘキサメチレングリコール、1,4-シクロヘキサンジオール、1,4-シクロヘキサンジメタノール、アジピン酸、ドデカン二酸、1,4-シクロヘキサンジカルボン酸等のエステル形成性モノマーが挙げられる。 Such copolymerization components include ester-forming monomers such as 5-sodium sulfoisophthalic acid, 5-potassium sulfoisophthalic acid, 3,5-dicarboxylic acid benzenesulfonic acid tetrabutylphosphonium salt, 3,5-dicarboxylic acid benzenesulfonic acid tributylmethylphosphonium salt, 1,4-butanediol, neopentyl glycol, 1,6-hexamethylene glycol, 1,4-cyclohexanediol, 1,4-cyclohexanedimethanol, adipic acid, dodecanedioic acid, and 1,4-cyclohexanedicarboxylic acid.
また、必要に応じて、上記PTTには、各種の添加剤、例えば、艶消し剤、熱安定剤、消泡剤、整色剤、難燃剤、酸化防止剤、紫外線吸収剤、赤外線吸収剤、結晶核剤、蛍光増白剤などを共重合、または混合してもよい。 If necessary, the PTT may be copolymerized or mixed with various additives, such as matting agents, heat stabilizers, defoamers, color-adjusting agents, flame retardants, antioxidants, ultraviolet absorbers, infrared absorbers, crystal nucleating agents, and fluorescent whitening agents.
本発明に用いるポリトリメチレンテレフタレートポリマーは、極限粘度[η]が0.5~1.6であることが好ましく、より好ましくは0.6~1.5である。さらに好ましくは0.7~1.4である。 The polytrimethylene terephthalate polymer used in the present invention preferably has an intrinsic viscosity [η] of 0.5 to 1.6, more preferably 0.6 to 1.5, and even more preferably 0.7 to 1.4.
該極限粘度が0.5未満の場合は、ポリマーの分子量が低すぎるため強度発現が困難となる場合があり、一方、該極限粘度が1.6越える場合は、流動性が低いため低粘度のポリトリメチレンテレフタレートの曵糸性が損なわれ紡糸時糸切れの原因となる場合があるため、好ましくない。 If the intrinsic viscosity is less than 0.5, the molecular weight of the polymer is too low, making it difficult to achieve strength. On the other hand, if the intrinsic viscosity exceeds 1.6, the low fluidity impairs the spinnability of the low-viscosity polytrimethylene terephthalate, which may cause thread breakage during spinning, and this is not preferred.
(2)ポリトリメチレンテレフタレート繊維
本発明のポリトリメチレンテレフタレート繊維は、熱水処理による変形が小さいため、布帛とした際に、糸の縮みが少なくやわらかな風合いを有する。またこのポリトリメチレンテレフタレート繊維の特徴として引っ張り強伸度測定における1次降伏点以降の弾性率が低いため、それを用いた布帛を作製すると、通常のポリトリメチレンテレフタレート繊維に対してさらに柔軟なドレープ性有する布帛となる。
(2) Polytrimethylene terephthalate fiber The polytrimethylene terephthalate fiber of the present invention is less deformed by hot water treatment, and therefore when made into a fabric, the yarn shrinks less and has a soft texture. In addition, since the polytrimethylene terephthalate fiber is characterized by a low elastic modulus after the first yield point in a tensile strength and elongation measurement, a fabric made using the polytrimethylene terephthalate fiber has a softer drape than that of ordinary polytrimethylene terephthalate fibers.
このようなポリトリメチレンテレフタレート繊維の糸物性として、本願におけるポリトリメチレンテレフタレート繊維の沸騰水収縮率(以下、沸水収縮率と称する場合がある)は5%以下であることが必要であり、好ましくは4%以下、さらに好ましくは3%以下である。該沸騰水収縮率が5%よりも大きい場合、熱収縮による糸の縮みによって布帛が硬くなる。 As for the yarn properties of such polytrimethylene terephthalate fibers, the boiling water shrinkage rate of the polytrimethylene terephthalate fibers in this application (hereinafter sometimes referred to as boiling water shrinkage rate) must be 5% or less, preferably 4% or less, and more preferably 3% or less. If the boiling water shrinkage rate is greater than 5%, the fabric will become stiff due to shrinkage of the yarn caused by heat shrinkage.
また、本発明のポリトリメチレンテレフタレート繊維は、伸度20%における弾性率が5cN/dtex以下であることが必要であり、好ましくは4cN/dtex以下、さらに好ましくは3cN/dtex以下である。伸度20%における弾性率が5cN/dtexよりも大きくなると、その後の染色加工などによって、布帛が硬くなる。 The polytrimethylene terephthalate fiber of the present invention must have an elastic modulus of 5 cN/dtex or less at an elongation of 20%, preferably 4 cN/dtex or less, and more preferably 3 cN/dtex or less. If the elastic modulus at an elongation of 20% is greater than 5 cN/dtex, the fabric will become stiff due to subsequent dyeing and other processes.
さらに、本発明のポリトリメチレンテレフタレート繊維の複屈折率Δnは0.040以上、0.08以下であることが好ましい。より好ましくは複屈折率Δnが0.045以上0.075以下、さらに好ましくは複屈折率Δnが0.050以上0.070以下である。該複屈折率Δnが0.040よりも小さい場合、糸強度が小さくなり、外力により布帛が伸びてしまうことで形態維持が難しくなるため好ましくない。 Furthermore, the birefringence Δn of the polytrimethylene terephthalate fiber of the present invention is preferably 0.040 or more and 0.08 or less. More preferably, the birefringence Δn is 0.045 or more and 0.075 or less, and even more preferably, the birefringence Δn is 0.050 or more and 0.070 or less. If the birefringence Δn is less than 0.040, the thread strength is reduced and the fabric stretches due to external forces, making it difficult to maintain its shape, which is undesirable.
さらに、本発明のポリトリメチレンテレフタレート繊維の結晶化度を示す代替指標となる比重は1.350以下であることが好ましく、1.319以上、1.350以下であることがさらに好ましい。比重が1.319よりも小さい場合、延伸仮撚加工において糸条が脆化して糸切れが多発し、延伸仮撚加工が困難となる。一方、比重が1.350よりも大きい場合、毛羽が多発するので好ましくない。 Furthermore, the specific gravity, which is an alternative index showing the degree of crystallinity of the polytrimethylene terephthalate fiber of the present invention, is preferably 1.350 or less, and more preferably 1.319 or more and 1.350 or less. If the specific gravity is less than 1.319, the yarn becomes brittle during the draw-twist processing, causing frequent yarn breakage and making the draw-twist processing difficult. On the other hand, if the specific gravity is greater than 1.350, it is not preferable because a lot of fluff occurs.
また、本発明のポリトリメチレンテレフタレート繊維の熱応力のピークが50℃~100℃に存在することが好ましい。該ピークが50℃よりも低い温度に存在する場合、耐熱性が低くなり、好ましくない。また該ピークが100℃よりも高い温度に存在する場合、結晶化度が高くなりすぎてしまい、柔軟なドレープ性が失われるため、好ましくない。 In addition, it is preferable that the thermal stress peak of the polytrimethylene terephthalate fiber of the present invention exists at 50°C to 100°C. If the peak exists at a temperature lower than 50°C, the heat resistance will be low, which is not preferable. Also, if the peak exists at a temperature higher than 100°C, the degree of crystallization will be too high, and soft drapeability will be lost, which is not preferable.
さらに、本発明のポリトリメチレンテレフタレート繊維の熱応力のピーク値は0.2cN/dtex以下となることが好ましい。該熱応力のピーク値が0.2cN/dtexよりも大きくなると染色等、熱水水処理による変形が大きくなるため、布帛とした際に、糸が縮み硬い風合いとなるため好ましくない。 Furthermore, it is preferable that the peak value of the thermal stress of the polytrimethylene terephthalate fiber of the present invention is 0.2 cN/dtex or less. If the peak value of the thermal stress is greater than 0.2 cN/dtex, deformation due to hot water treatment such as dyeing will be large, and when made into a fabric, the yarn will shrink and have a hard texture, which is not preferable.
また、本発明のポリトリメチレンテレフタレート繊維の破断強度は1.5cN/dtex以上~3.5cN/dtex、好ましくは1.7cN/dtex~3.3cN/dtex、さらに好ましくは2.0cN/dtex~3.0cN/dtexである。 The breaking strength of the polytrimethylene terephthalate fiber of the present invention is 1.5 cN/dtex or more to 3.5 cN/dtex, preferably 1.7 cN/dtex to 3.3 cN/dtex, and more preferably 2.0 cN/dtex to 3.0 cN/dtex.
ポリトリメチレンテレフタレート繊維の破断強度が1.5cN/dtexよりも小さい場合、製品の耐久性が低下するため、好ましくない。またポリトリメチレンテレフタレート繊維の破断強度が3.5cN/dtexよりも大きい場合、結晶化度が高くなりすぎてしまい、柔軟なドレープ性が失われるため、好ましくない。 If the breaking strength of the polytrimethylene terephthalate fiber is less than 1.5 cN/dtex, the durability of the product will decrease, which is not preferable. Also, if the breaking strength of the polytrimethylene terephthalate fiber is more than 3.5 cN/dtex, the degree of crystallinity will be too high, and the product will lose its soft drapeability, which is not preferable.
ポリトリメチレンテレフタレート繊維の破断伸度は30%~100%であることが好ましい。ポリトリメチレンテレフタレート繊維の破断伸度が30%よりも小さい場合、結晶化度が高くなりすぎてしまい、柔軟なドレープ性が失われるため、好ましくない。一方、ポリトリメチレンテレフタレート繊維の破断伸度が100%よりも大きい場合、維に負荷がかかった際に、繊維が伸びてしまい、寸法安定性が優れないため好ましくない。 The breaking elongation of polytrimethylene terephthalate fiber is preferably 30% to 100%. If the breaking elongation of polytrimethylene terephthalate fiber is less than 30%, the degree of crystallinity will be too high, and flexible drapeability will be lost, which is not preferred. On the other hand, if the breaking elongation of polytrimethylene terephthalate fiber is more than 100%, the fiber will stretch when a load is applied to it, and dimensional stability will be poor, which is not preferred.
(3)ポリトリメチレンテレフタレート繊維の製造方法
上記のようなポリトリメチレンテレフタレート繊維は、例えば、以下の製造方法により造することができる。
先ず、90モル%以上がトリメチレンテレフタレート繰返し単位から構成されるポリトリメチレンテレフタレートを溶融固化した後、1000m/分以上の巻取り速度で巻き取り、引き続いてポリトリメチレンテレフタレートのガラス転移点±20℃の加熱ローラーで加熱し、続いて1.0~2.0倍延伸を行い、さらに50~150℃の加熱ローラーに巻き付けた後、2000~4800m/分の速度で一旦チーズ状パッケージに巻き取る。
(3) Method for Producing Polytrimethylene Terephthalate Fibers The polytrimethylene terephthalate fibers as described above can be produced, for example, by the following method.
First, polytrimethylene terephthalate composed of 90 mol % or more of trimethylene terephthalate repeating units is melted and solidified, and then wound up at a winding speed of 1000 m/min or more. Then, it is heated with a heating roller at a temperature of ±20°C of the glass transition point of polytrimethylene terephthalate, and then stretched 1.0 to 2.0 times. Then, it is wound around a heating roller at a temperature of 50 to 150°C, and then temporarily wound into a cheese-like package at a speed of 2000 to 4800 m/min.
このようにしてチーズ状パッケージに巻き取られた破断伸度50~200%のポリトリメチレンテレフタレート繊維を、該ポリトリメチレンテレフタレートのガラス転移点以下の温度で1.1倍以上延伸した後、加熱しながら、0.5~0.9倍の倍率で繊維を収縮させることにより、熱による収縮が小さく、やわらかな風合いを有する布帛とすることが可能なポリトリメチレンテレフタレート繊維を得ることができる。 The polytrimethylene terephthalate fiber with a breaking elongation of 50 to 200% wound into a cheese-shaped package in this way is stretched by 1.1 times or more at a temperature below the glass transition point of the polytrimethylene terephthalate, and then the fiber is shrunk by 0.5 to 0.9 times while heating, thereby obtaining polytrimethylene terephthalate fiber that has little shrinkage due to heat and can be made into a fabric with a soft texture.
この際、ガラス転移点以下の温度での延伸倍率と、加熱しながらの収縮倍率との積で表される、トータル延伸倍率は、0.9~1.25倍が好ましく、0.95~1.20倍がさらに好ましい。トータル延伸倍率が0.90倍よりも小さい場合、糸が緩み、延伸時糸の走行が安定せず断糸の原因となる場合があるため、好ましくない。また、トータル延伸倍率が1.25倍よりも大きい場合、糸の収縮率が高くなりすぎ、布帛とした際にやわらかな風合いとならない場合があるため、好ましくない。 In this case, the total stretch ratio, which is expressed as the product of the stretch ratio at a temperature below the glass transition point and the shrinkage ratio while heating, is preferably 0.9 to 1.25 times, and more preferably 0.95 to 1.20 times. If the total stretch ratio is less than 0.90 times, the yarn will slacken and the yarn will not run stably during stretching, which may cause yarn breakage, and this is not preferred. Also, if the total stretch ratio is more than 1.25 times, the shrinkage rate of the yarn will be too high, and the fabric may not have a soft texture when made into a fabric, which is also not preferred.
尚、破断伸度50~200%の溶融後固化したポリトリメチレンテレフタレート繊維は、例えば、紡糸速度1000m/分以上の巻取り速度で巻き取り、引き続いてポリトリメチレンテレフタレートのガラス転移点±20℃の温度で、1.0~2.0倍の低倍率で延伸して製造することもできる。 In addition, polytrimethylene terephthalate fibers that have been melted and solidified and have a breaking elongation of 50 to 200% can also be produced by winding the fibers at a spinning speed of 1000 m/min or more, followed by drawing them at a low ratio of 1.0 to 2.0 times at a temperature of ±20°C above the glass transition point of polytrimethylene terephthalate.
また、紡糸速度4000m/分以上の速度で加熱ローラーに巻取り、巻取機にて巻き取ることも可能である。これらの方法の中で、巻取機にてポリトリメチレンテレフタレート繊維を直接巻取る際の巻締りを抑制する目的で、巻取前に50~150℃の加熱ローラーで加熱しても問題はない。 It is also possible to wind the fiber around a heated roller at a spinning speed of 4000 m/min or more, and then wind it up using a winder. Among these methods, there is no problem with heating the fiber with a heated roller at 50 to 150°C before winding, in order to prevent winding tightness when the polytrimethylene terephthalate fiber is directly wound up on the winder.
このようにして得られる高伸度ポリトリメチレンテレフタレート繊維は、破断伸度50~200%以上であることが望ましい。より好ましくは60~190%、さらに好ましくは70~180%である。 The high-elongation polytrimethylene terephthalate fiber obtained in this manner desirably has a breaking elongation of 50 to 200% or more. More preferably, it is 60 to 190%, and even more preferably, it is 70 to 180%.
該高伸度ポリトリメチレンテレフタレート繊維の破断伸度が50%未満の場合、繊維の結晶化が高くなってしまい、やわらかな風合いの布帛にできないため、好ましくない。一方、破断伸度200%よりも大きくなると、ガラス転移点以下の温度で延伸した際に結晶化が進まず、強度が著しく低く、布帛とした際に耐久性が低くなるため好ましくない。 If the breaking elongation of the high-elongation polytrimethylene terephthalate fiber is less than 50%, the fiber will be highly crystallized, and it will not be possible to make a fabric with a soft feel, which is not preferred. On the other hand, if the breaking elongation is greater than 200%, crystallization will not progress when stretched at a temperature below the glass transition point, resulting in significantly lower strength and lower durability when made into a fabric, which is also not preferred.
続いて、溶融後固化したポリトリメチレンテレフタレート繊維をポリトリメチレンテレフタレートのガラス転移点以下の温度、さらに好ましくはガラス転移点-5℃以下、さらに好ましくはガラス転移点-10℃以下の温度で1.1倍以上、さらに好ましくは1.2倍以上、さらに好ましくは1.3倍以上延伸する。 Then, the polytrimethylene terephthalate fiber that has been melted and solidified is stretched at a temperature below the glass transition point of polytrimethylene terephthalate, more preferably at a temperature below the glass transition point -5°C, and even more preferably at a temperature below the glass transition point -10°C, by 1.1 times or more, more preferably 1.2 times or more, and even more preferably 1.3 times or more.
この際、ガラス転移点よりも高い温度で延伸した場合は、結晶化度が高くなってしまい、やわらかな風合いの布帛にできないため、好ましくない。また、1.1倍よりも低い倍率で延伸した場合、布帛とした際に耐久性が低くなるため好ましくない。 In this case, if the material is stretched at a temperature higher than the glass transition point, the degree of crystallinity will be high, and it will not be possible to produce a fabric with a soft feel, which is not preferred. Also, if the material is stretched at a ratio lower than 1.1, the durability of the fabric will be low, which is also not preferred.
また延伸した繊維は、結晶化が進んでおらず、ポリマーが高い配向を示していることで熱による寸法安定性が低いことから、加熱しながら、0.5倍以上~0.9倍以下の倍率で繊維を収縮させることによって寸法安定性及び耐久性が向上する。 In addition, since the stretched fibers are not yet crystallized and the polymers are highly oriented, their dimensional stability due to heat is low. Therefore, by shrinking the fibers by a factor of 0.5 to 0.9 while heating, the dimensional stability and durability can be improved.
この際、繊維の収縮が0.5倍よりも低い場合、得られたポリトリメチレンテレフタレート繊維の配向結晶化度が低くなりすぎ、布帛とした際に耐久性が低くなるため好ましくない。また繊維の収縮が0.9倍よりも大きい場合は結晶化度が高くなってしまい、やわらかな風合いの布帛にできないので、好ましくない。 In this case, if the fiber shrinkage is less than 0.5 times, the degree of orientation crystallinity of the resulting polytrimethylene terephthalate fiber will be too low, and the durability of the fabric will be low when it is made into a fabric, which is not preferred. Also, if the fiber shrinkage is more than 0.9 times, the degree of crystallinity will be too high, and it will not be possible to make a fabric with a soft feel, which is also not preferred.
(4)ポリエステル系繊維(芯糸用)
本発明においては、上記ポリトリメチレンテレフタレート繊維と、ポリエステル系繊維とを空気加工により混繊して空気混繊糸を得る。
(4) Polyester fiber (for core thread)
In the present invention, the polytrimethylene terephthalate fiber and the polyester fiber are mixed by air processing to obtain an air-mixed yarn.
この際使用するポリエステル系繊維としては、ポリトリメチレンテレフタレート(PTT)繊維、ポリエチレンテレフタレート(PET)繊維、ポリトリメチレンテレフタレートとポリエチレンテレフタレートとのサイドバイサイド型もしくは偏芯芯鞘型複合繊維、ポリトリメチレンテレフタレートとポリトリメチレンテレフタレートとのサイドバイサイド型もしくは偏芯芯鞘型複合繊維、ポリエチレンテレフタレートとポリエチレンテレフタレートとのサイドバイサイド型もしくは偏芯芯鞘型複合繊維など、常法により紡糸、延伸された繊維が好ましく例示される。また、制電剤、難燃剤、耐熱剤、耐候剤、酸化チタン等の添加剤を加えることは何ら差し支えない。
かかるポリエステル系繊維においては、空気混繊糸に加熱処理等を加えて、芯糸と鞘糸との糸足差を大きくする上で、沸水収縮率が7~50%であることが好ましい。
The polyester fibers used in this case are preferably exemplified by fibers spun and drawn by a conventional method, such as polytrimethylene terephthalate (PTT) fibers, polyethylene terephthalate (PET) fibers, side-by-side or eccentric core-sheath type composite fibers of polytrimethylene terephthalate and polyethylene terephthalate, side-by-side or eccentric core-sheath type composite fibers of polytrimethylene terephthalate and polytrimethylene terephthalate, side-by-side or eccentric core-sheath type composite fibers of polyethylene terephthalate and polyethylene terephthalate, etc. In addition, additives such as antistatic agents, flame retardants, heat resistance agents, weather resistance agents, titanium oxide, etc. may be added without any problem.
In such polyester fibers, it is preferable that the boiling water shrinkage rate is 7 to 50% in order to increase the yarn length difference between the core yarn and the sheath yarn by subjecting the air-mixed yarn to a heat treatment or the like.
(5)空気混繊糸の製造方法
次いで、鞘糸用糸条として前記ポリトリメチレンテレフタレート繊維と、芯糸用糸条として前記ポリエステル系繊維とを引き揃え、空気加工(インターレースまたはタスラン(登録商標))で交絡(好ましくは30~150個/m)し、ローラーで引き取ることにより空気混繊糸を得ることができる。空気混繊加工時のオーバーフィード率は0.5~2%が好ましい。
(5) Manufacturing method of air-mixed yarn Next, the polytrimethylene terephthalate fiber as the sheath yarn and the polyester fiber as the core yarn are aligned, intertwined (preferably 30 to 150 pieces/m) by air processing (interlace or Taslan (registered trademark)), and taken up by a roller to obtain an air-mixed yarn. The overfeed rate during air-mixing processing is preferably 0.5 to 2%.
さらに、本発明の空気混繊糸は、丸断面以外の異型断面繊維を含んでいてもよい。例えば、十字型断面、三角断面、または星形断面などの異型断面繊維から構成することもでき、こうすれば独特の風合いを得ることができる。ここで、異型断面繊維の異型度とは、図1に示す通り、繊維断面の最大内接円径rと最小外接円径Rを測定して、異型度=R/rで算出した値であり、異型度=R/rの値は1.15~10.0が好ましく、1.2~10.0がさらに好ましい。該異型度が1.15未満では、丸断面との差が小さくなるおそれがある。また、異型度が10.0を越えると、紡糸時に糸断面形状外側と内側で配向差などが大きくなり、得られた糸は毛羽・タルミが多く、加工に適さないおそれがある。 Furthermore, the air-mixed yarn of the present invention may contain fibers with irregular cross sections other than a circular cross section. For example, it may be composed of fibers with irregular cross sections such as cross-shaped, triangular, or star-shaped cross sections, which can provide a unique texture. Here, the irregularity of the irregular cross section fiber is the value calculated by measuring the maximum inscribed circle diameter r and the minimum circumscribed circle diameter R of the fiber cross section as shown in Figure 1, and the irregularity value = R/r is preferably 1.15 to 10.0, and more preferably 1.2 to 10.0. If the irregularity is less than 1.15, the difference from the circular cross section may be small. Also, if the irregularity exceeds 10.0, the orientation difference between the outer and inner cross sections of the yarn during spinning becomes large, and the obtained yarn may have a lot of fluff and slack, making it unsuitable for processing.
また、異型断面繊維として扁平断面繊維も例示される。扁平断面繊維を用いることにより独特の風合いを得ることができるので好ましい。ここで扁平断面繊維の扁平度とは、図2に示す如く、繊維断面に外接する長方形を描き、その長辺Lと短辺Hを測定して、扁平度=L/Hで算出した値であり、本発明においては、扁平度=L/Hの値は2.0~10.0であることが好ましい。該扁平度が2.0未満では、丸断面との差が小さくなるおそれがある。また、該扁平度が10.0を越えると、紡糸時、毛羽が発生しやすくなり安定性が不良となるおそれがある。 Furthermore, flat cross-section fibers are also exemplified as modified cross-section fibers. The use of flat cross-section fibers is preferable because it allows for a unique texture to be obtained. Here, the flatness of a flat cross-section fiber is a value calculated by drawing a rectangle circumscribing the cross-section of the fiber, measuring its long side L and short side H, and calculating the flatness = L/H, as shown in Figure 2. In the present invention, the value of the flatness = L/H is preferably 2.0 to 10.0. If the flatness is less than 2.0, the difference from a round cross-section may become small. Also, if the flatness exceeds 10.0, fluff may be easily generated during spinning, resulting in poor stability.
かくして得られた空気混繊糸は、柔らかな風合いを有するポリトリメチレンテレフタレートからなる低収縮繊維を鞘糸に用いた、芯鞘の糸足差が大きい芯鞘型空気混繊糸とすることができる。 The air-mixed yarn thus obtained can be a sheath-core air-mixed yarn with a large thread length difference between the core and sheath, using a low-shrinkage fiber made of polytrimethylene terephthalate, which has a soft texture, as the sheath yarn.
(6)芯鞘型空気混繊糸の製造方法
本発明においては、上記空気混繊糸に染色加工などの熱処理を施すことにより、前記ポリトリメチレンテレフタレート繊維が鞘糸に、前記ポリエステル系繊維が芯糸になり、芯糸と鞘糸とを含む芯鞘型空気混繊糸となる。
(6) Manufacturing method of core-sheath type air-mixed yarn In the present invention, the air-mixed yarn is subjected to a heat treatment such as dyeing processing, whereby the polytrimethylene terephthalate fiber becomes a sheath yarn and the polyester-based fiber becomes a core yarn, thereby forming a core-sheath type air-mixed yarn containing a core yarn and a sheath yarn.
かかる空気混繊糸において、鞘糸の単繊維繊度は0.3~10dtexであることが必要であり、より好ましくは0.5~8dtex、さらに好ましくは0.6~5dtexである。該単繊維繊度が10dtexよりも大きい場合、単繊維が太いことによって布帛の柔らかさが失われるおそれがある。また該単繊維繊度が0.3dtexよりも小さい場合、糸切れが頻発し繊維を製造することができないおそれがある。鞘糸の単繊維数(フィラメント数)としては20~150本が好ましい。
一方、芯糸の単繊維繊度は1.0~5.0dtexであることが好ましい。芯糸の単繊維数(フィラメント数)としては12~100本が好ましい。
In such an air-mixed yarn, the single fiber fineness of the sheath yarn must be 0.3 to 10 dtex, more preferably 0.5 to 8 dtex, and even more preferably 0.6 to 5 dtex. If the single fiber fineness is greater than 10 dtex, the fabric may lose its softness due to the thick single fiber. If the single fiber fineness is less than 0.3 dtex, yarn breakage may occur frequently, making it impossible to produce the fiber. The number of single fibers (filament number) of the sheath yarn is preferably 20 to 150.
On the other hand, the core yarn preferably has a single fiber fineness of 1.0 to 5.0 dtex, and the core yarn preferably has 12 to 100 single fibers (filament number).
また、本発明の芯鞘型空気混繊糸において、総繊度は30~400dtexであることが必要であり、より好ましくは50~200dtexである。該総繊度が30dtexよりも小さい場合は総繊度が細すぎて、空気混繊加工が難しくなるおそれがある。一方、該総繊度が400dtexよりも大きい場合、布帛の柔らかさが失われるおそれがある。なお、単繊維数(フィラメント数)としては、40~400本(より好ましくは40~200本)が好ましい。 In addition, in the core-sheath type air-mixed yarn of the present invention, the total fineness must be 30 to 400 dtex, and more preferably 50 to 200 dtex. If the total fineness is less than 30 dtex, the total fineness is too fine and air-mixing processing may be difficult. On the other hand, if the total fineness is more than 400 dtex, the softness of the fabric may be lost. The number of single fibers (filaments) is preferably 40 to 400 (more preferably 40 to 200).
上記芯鞘型空気混繊糸においては、下記で定義する芯糸と鞘糸との糸足差は5%以上(より好ましくは6~40%)であることが肝要である。該糸足差が5%未満では十分な膨らみ感が得られない。 In the above-mentioned core-sheath type air-mixed yarn, it is essential that the yarn length difference between the core yarn and the sheath yarn, as defined below, is 5% or more (more preferably 6-40%). If the yarn length difference is less than 5%, a sufficient sense of volume cannot be obtained.
上記の糸足差は、前述の空気混繊糸を沸騰水下にて処理した後、0.1cN(0.098g)×空気混繊糸の総繊度(dtex)の荷重をとりつけて5cmの長さにカットし、カットした空気混繊糸から、ポリエステル系繊維A(単繊維)とポリトリメチレンテレフタレート繊維B(単繊維)とを取り出し、それぞれ、0.1cN(0.098g)×の単繊維繊度(dtex)の荷重をかけて長さを測定し、下記式により糸足差(%)を算出する。
糸足差(%)=(LB-LA)/LA×100
ただし、LAは芯糸のポリエステル系繊維の糸長(cm)であり、LBは鞘糸のポリトリメチレンテレフタレート繊維の糸長(cm)である。
The above-mentioned yarn length difference was calculated by treating the air-mixed yarn in boiling water, applying a load of 0.1 cN (0.098 g) × the total fineness (dtex) of the air-mixed yarn and cutting it to a length of 5 cm. From the cut air-mixed yarn, polyester fiber A (single fiber) and polytrimethylene terephthalate fiber B (single fiber) were taken out and their lengths were measured under a load of 0.1 cN (0.098 g) × the single fiber fineness (dtex). The yarn length difference (%) was calculated using the following formula.
Thread length difference (%) = (LB-LA)/LA x 100
Here, LA is the yarn length (cm) of the polyester fiber core yarn, and LB is the yarn length (cm) of the polytrimethylene terephthalate fiber sheath yarn.
また、本発明の芯鞘型空気混繊糸において、鞘糸のポリトリメチレンテレフタレート繊維が混繊糸重量対比の50~90%である(より好ましくは60~80%)ことが好ましい。鞘糸のポリトリメチレンテレフタレート繊維の重量比が50%以下の場合、ソフトな風合いが得られないだけでなく、芯糸と鞘糸の染着差が見えやすくなるおそれがある。 Furthermore, in the core-sheath type air-mixed yarn of the present invention, it is preferable that the polytrimethylene terephthalate fiber of the sheath yarn is 50 to 90% (more preferably 60 to 80%) of the weight of the mixed yarn. If the weight ratio of the polytrimethylene terephthalate fiber of the sheath yarn is 50% or less, not only will a soft feel not be obtained, but the dyeing difference between the core yarn and the sheath yarn may become more visible.
(7)芯鞘型空気混繊糸からなる布帛の製造方法
本発明においては、前述の空気混繊糸を用いて製編織することにより布帛(生機)を得た後、適宜、染色加工や吸汗加工を施して製品としての布帛を得る。その際、染色加工の熱処理により混繊糸の鞘糸と芯糸との糸足差が発現し、芯鞘型空気混繊糸からなる布帛となる。
(7) Manufacturing method of fabric made of sheath-core air-mixed yarn In the present invention, fabric (grey fabric) is obtained by knitting and weaving the above-mentioned air-mixed yarn, and then dyeing and sweat absorbing are appropriately performed to obtain a fabric as a product. At that time, the yarn length difference between the sheath yarn and the core yarn of the mixed yarn appears by the heat treatment of the dyeing process, and the fabric is made of sheath-core air-mixed yarn.
ここで、芯鞘型空気混繊糸だけで布帛を構成してもよいが、芯鞘型空気混繊糸と他の糸条とで布帛を構成してもよい。その際、他の糸条は特に限定されず、非捲縮糸、仮撚捲縮加工糸、潜在捲縮糸、紡績糸などのいずれであってもよい。 Here, the fabric may be made of only the sheath-core air-mixed yarn, but it may also be made of the sheath-core air-mixed yarn and other yarns. In this case, the other yarns are not particularly limited and may be any of non-crimped yarns, false-twisted crimped yarns, latent crimped yarns, spun yarns, etc.
布帛の組織は特に限定されず、編物、織物いずれでもよい。例えば、天竺、ニットミス、スムース、フライス、鹿の子、添え糸編、デンビー、ハーフなどの編組織を有する編物や、平織、綾織、サテンなどの織組織を有する織物などが例示されるが、これらに限定されるものではない。層数も単層でもよいし、2層以上の多層であってもよい。 The structure of the fabric is not particularly limited, and it may be either knitted or woven. Examples include knitted fabrics with knitting structures such as plain weave, knit miss, smooth, rib, pique, plaited knit, denby, and half, and woven fabrics with weaving structures such as plain weave, twill, and satin, but are not limited to these. The number of layers may be a single layer or multiple layers of two or more layers.
次いで、前記の布帛を用いて、スポーツウエアー、アウターウエアー、インナーウエアー、紳士衣料、婦人衣料、介護用衣料、作業衣、カーシート表皮材、寝具などの繊維製品としてもよい。かかる布帛や繊維製品は前記の空気混繊糸を用いているので、ソフトな風合いと膨らみに優れる。 Then, the fabric may be used to make textile products such as sportswear, outerwear, innerwear, men's clothing, women's clothing, nursing clothing, workwear, car seat covering materials, and bedding. Since such fabrics and textile products use the air-mixed yarn, they have a soft feel and excellent fluffiness.
以下、本発明の実施例及び比較例を詳述するが、本発明はこれらによって限定されるものではない。なお、実施例中の各測定項目は下記の方法で測定した。 The following describes in detail examples and comparative examples of the present invention, but the present invention is not limited to these. The measurement items in the examples were measured by the following methods.
(1)極限粘度[η]
極限粘度[η]は、オストワルド粘度計を用い、35℃、o-クロロフェノール中での比粘度ηspと濃度C(g/100ミリリットル)の比ηsp/Cを濃度ゼロに外挿し、以下の式(1)に従って求めた。
[η]=lim(ηsp/C) ・・・(1)
C→0
(1) Intrinsic viscosity [η]
The intrinsic viscosity [η] was calculated using an Ostwald viscometer by extrapolating the ratio η/C of the specific viscosity η in o-chlorophenol at 35° C. to the concentration C (g/100 milliliters) to a concentration of zero, according to the following formula (1).
[η]=lim(ηsp/C)...(1)
C → 0
(2)ガラス転移点
ガラス転移点は、規定量のポリマーチップをアルミサンプルパンに封入し、DSCにて窒素雰囲気下で室温~300℃まで昇温速度10℃/minで昇温した昇温曲線からガラス転移点を測定した。
(2) Glass transition point The glass transition point was measured from a temperature rise curve obtained by sealing a specified amount of polymer chips in an aluminum sample pan and heating the chips from room temperature to 300° C. at a heating rate of 10° C./min in a nitrogen atmosphere using a DSC.
(3)繊度(マルチフィラメント糸の繊度)
JIS-L-1013に従ってマルチフィラメント糸の繊度を測定した。またその値をマルチフィラメント糸の単糸数で除することにより単糸繊度を求めた。
(3) Fineness (fineness of multifilament yarn)
The fineness of the multifilament yarn was measured in accordance with JIS-L-1013. The measured value was divided by the number of single yarns in the multifilament yarn to determine the single yarn fineness.
(4)沸騰水収縮率(BWS)
JIS-L-1013に基づき、繊維を枠周1.125mの検尺機を用い、デシテックスの1/30gの初荷重をかけ巻き返し、巻回数20回のカセをつくりデシテックス/1.11gの荷重をかけカセ長をはかる。次に荷重を外し、カセを100℃の熱水中に30分間浸漬した後取り出し、自然乾燥し、再び加重をかけてカセ長をはかり次の式により沸水収縮率を算出した。
沸水収縮率(%)={(L0-L1)/L0}×100
ここで、L0;浸漬前カセ長(mm)、L1;浸漬後カセ長(mm)
(4) Boiling Water Shrinkage (BWS)
Based on JIS-L-1013, the fiber was rewound using a measuring machine with a frame circumference of 1.125 m under an initial load of 1/30 g of decitex, a skein of 20 turns was made, and a load of dtex/1.11 g was applied to measure the skein length. The load was then removed, and the skein was immersed in hot water at 100°C for 30 minutes, then removed and naturally dried, and the skein length was measured under a load again, and the boiling water shrinkage was calculated using the following formula.
Boiling water shrinkage rate (%) = {(L0-L1)/L0}×100
Where L0: reel length before immersion (mm), L1: reel length after immersion (mm)
(5)破断強度、破断伸度
JIS-L-1013に基づいて定速伸長形引張試験機であるオリエンテック(株)社製テンシロンを用いて、つかみ間隔20cm、引張速度20cm/分にて測定した。
(5) Breaking strength and breaking elongation: Based on JIS-L-1013, measurements were made using a constant speed extension tensile tester, Tensilon manufactured by Orientec Co., Ltd., at a gripping distance of 20 cm and a pulling speed of 20 cm/min.
(6)伸度20%時弾性率
JIS-L-1013に基づいて定速伸長形引張試験機であるオリエンテック(株)社製テンシロンを用いて、つかみ間隔20cm、引張速度20cm/分にて測定した。伸度20%におけるSSカーブの接線において傾きを伸度20%時弾性率として求めた。
(6) Elastic modulus at 20% elongation: Measured according to JIS-L-1013 using a constant-speed elongation tensile tester, Tensilon, manufactured by Orientec Co., Ltd., at a gripping distance of 20 cm and a pulling speed of 20 cm/min. The slope of the tangent to the SS curve at 20% elongation was determined as the elastic modulus at 20% elongation.
(7)比重
JIS-L-1013 8.17.1の浮沈法に基づいて試料の比重を測定した。
(7) Specific Gravity The specific gravity of the sample was measured based on the sink-float method of JIS-L-1013 8.17.1.
(8)複屈折率Δn
繊維便覧-原料編、p.969(第5刷、1978年丸善株式会社発行)に準じ、光学顕微鏡とコンペンセーターを用いて、繊維の表面に観察される偏光のリターデーションから求めた。
(8) Birefringence Δn
According to Fiber Handbook - Raw Materials, p. 969 (5th edition, published by Maruzen Co., Ltd. in 1978), the retardation was determined from the polarized light observed on the surface of the fiber using an optical microscope and a compensator.
(9)熱応力の極大値が存在する温度及び熱応力の極大値
鐘紡エンジニアリング社製のKE-2を用いた。初過重0.044cN/dtex、昇温速度100℃/分で測定した。得られたデーターは横軸に温度、縦軸に熱応力をプロットし温度-熱応力曲線を描く。該温度-熱応力曲線の微分係数が正から負へ変化する点の温度、熱応力を求め、応力については繊度で除し、最大応力を求めた。
(9) Temperature at which maximum value of thermal stress exists and maximum value of thermal stress KE-2 manufactured by Kanebo Engineering Co., Ltd. was used. Measurements were performed with an initial load of 0.044 cN/dtex and a heating rate of 100°C/min. The obtained data was plotted with temperature on the horizontal axis and thermal stress on the vertical axis to draw a temperature-thermal stress curve. The temperature and thermal stress at the point where the differential coefficient of the temperature-thermal stress curve changed from positive to negative were determined, and the stress was divided by the fineness to determine the maximum stress.
(10)交絡数
空気加工糸を8.82mNx表示テックス(0.1g/dtex)の荷重下で1mの長さをとり、徐重後、室温で24時間放縮後の結節点の数を読み取り、個/mで表示した。
(10) Number of entanglements The air-textured yarn was cut to a length of 1 m under a load of 8.82 mNx (0.1 g/dtex), and the load was reduced. After letting it shrink for 24 hours at room temperature, the number of knots was read and expressed in units per m.
(11)糸足差
前記沸水収縮率と同様の方法でカセ処理した後、0.1cN(0.098g)×空気混繊糸の総繊度(dtex)の荷重をとりつけて5cmの長さにカットし、カットした空気混繊糸から、ポリエステル系繊維A(単繊維)とポリトリメチレンテレフタレート繊維B(単繊維)とを取り出し、それぞれ、0.1cN(0.098g)×の単繊維繊度(dtex)の荷重をかけて長さを測定し、下記式により糸足差(%)を算出する。
糸足差(%)=(LB-LA)/LA×100
ただし、LAは芯糸のポリエステル系繊維の糸長(cm)であり、LBは鞘糸のポリトリメチレンテレフタレート繊維の糸長(cm)である。
(11) Yarn length difference After treating the yarn in a skein in the same manner as in the boiling water shrinkage, the yarn was cut to a length of 5 cm under a load of 0.1 cN (0.098 g) × the total fineness (dtex) of the air-mixed yarn. From the cut air-mixed yarn, polyester fiber A (single fiber) and polytrimethylene terephthalate fiber B (single fiber) were taken out and their lengths were measured under a load of 0.1 cN (0.098 g) × the single fiber fineness (dtex). The yarn length difference (%) was calculated by the following formula.
Thread length difference (%) = (LB-LA)/LA x 100
Here, LA is the yarn length (cm) of the polyester fiber core yarn, and LB is the yarn length (cm) of the polytrimethylene terephthalate fiber sheath yarn.
(12)風合い
試験者が空気混繊糸を手で触り、〇(膨らみがあり、かつ柔らかい)、△(普通)、×(膨らみに乏しいか、硬い)の3段階に評価した。
(12) Feeling The air-blended yarn was touched by a tester with his/her hand and rated on a three-level scale: ◯ (fluffy and soft), △ (normal), × (poor fluffiness or hard).
[実施例1]
テレフタル酸ジメチルと1,3-プロパンジオールを1:2のモル比で仕込み、テレフタル酸ジメチルの0.1重量%に相当するチタンテトラブトキシドを加え、常圧下ヒーター温度240℃でエステル交換反応を完結させた。次にチタンテトラブトキシドを更に理論ポリマー量の0.1重量%、二酸化チタンを理論ポリマー量の0.5重量%添加し、270℃で3時間反応させた。
[Example 1]
Dimethyl terephthalate and 1,3-propanediol were charged in a molar ratio of 1:2, and titanium tetrabutoxide equivalent to 0.1% by weight of dimethyl terephthalate was added, and the transesterification reaction was completed under normal pressure at a heater temperature of 240° C. Next, titanium tetrabutoxide was further added in an amount of 0.1% by weight of the theoretical polymer amount, and titanium dioxide was added in an amount of 0.5% by weight of the theoretical polymer amount, and the reaction was carried out at 270° C. for 3 hours.
得られたポリマーは、トリメチレンテレフタレート繰返単位100モル%から構成され、その極限粘度は1.0dl/gであった。また、得られたポリマーのガラス転移点は51℃であった。
得られたポリマーを常法により乾燥し、水分を50ppmにした後、265℃で溶融させ、直径0.27mmの36個の孔の開いた一重配列の紡口を通して押出した。
The resulting polymer was composed of 100 mol % trimethylene terephthalate repeating units, had an intrinsic viscosity of 1.0 dl/g, and had a glass transition point of 51° C.
The resulting polymer was dried in a conventional manner to reduce the water content to 50 ppm, then melted at 265° C. and extruded through a single-row spinneret having 36 holes with a diameter of 0.27 mm.
押出された溶融マルチフィラメントを、風速4.0m/分の風を当てて急冷し固体マルチフィラメントに変えた後、ガイドノズルを用いてステアリル酸オクチル60重量%、ポリオキシエチレンアルキルエーテル15重量%、リン酸カリウム3重量%を含んだ油剤を濃度10重量%の水エマルジョン仕上げ剤として繊維に対して油剤付着量が0.6重量%となるように付着させた。 The extruded molten multifilament was quenched by blowing air at a speed of 4.0 m/min to convert it into a solid multifilament, after which a 10% water emulsion finishing agent containing 60% by weight of octyl stearate, 15% by weight of polyoxyethylene alkyl ether, and 3% by weight of potassium phosphate was applied using a guide nozzle so that the amount of oil applied to the fiber was 0.6% by weight.
次いで、固体マルチフィラメントを50℃に加熱した周速度2100m/分のロールに巻き付けた後、1.3倍で延伸されるように80℃の加熱したロールに巻き付け、その後スピンドルとタッチロールの双方を駆動する方式の巻取機を用いて、巻取速度2600m/分で巻き取って72dtex/36フィラメントの繊維の巻かれたチーズ状パッケージを得た。 The solid multifilament was then wound around a roll heated to 50°C with a peripheral speed of 2100 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.3 times. It was then wound at a winding speed of 2600 m/min using a winding machine that drives both the spindle and the touch roll, to obtain a cheese-like package wound with 72 dtex/36 filament fibers.
その後、パッケージに巻かれた繊維を30℃にて1.5倍延伸し、190℃の接触式加熱熱板ヒーターで加熱し、0.7倍で繊維を収縮させ、速度600m/minで巻取り、低収縮のポリトリメチレンテレフタレート繊維(鞘糸用糸条)を得た。
一方、芯糸用糸条として、ポリエステル(ポリエチレンテレフタレート)延伸糸(総繊度56dtex/36本、沸騰水収縮率10%)を用意した。
Thereafter, the fiber wound on the package was stretched to 1.5 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.7 times. The fiber was then wound at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
On the other hand, a polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 10%) was prepared as a core yarn.
次いで、前記鞘糸用糸条と芯糸用糸条とを引き揃えてオ-バーフィード率1.5%でインターレース加工し、交絡数69個/mの空気混繊糸を得た。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。 The sheath yarn and core yarn were then aligned and interlaced at an overfeed rate of 1.5% to obtain an air-mixed yarn with an entanglement rate of 69 entanglements/m. The physical properties of the resulting polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
[実施例2]
実施例1と同様の方法でポリマーを製造した後、得られたポリマーを常法により乾燥し、水分を50ppmにした後、265℃で溶融させ、直径0.23mmの72個の孔の開いた二重配列の紡口を通して押出した。
[Example 2]
A polymer was produced in the same manner as in Example 1, and the polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a double-arranged spinneret having 72 holes with a diameter of 0.23 mm.
押出された溶融マルチフィラメントに、実施例1と同様の方法で油剤を付着させた後、該固体マルチフィラメントを50℃に加熱した周速度2100m/分のロールに巻き付けた後、1.3倍で延伸されるように80℃の加熱したロールに巻き付け、その後スピンドルとタッチロールの双方を駆動する方式の巻取機を用いて、巻取速度2600m/分で巻き取って72dtex/72フィラメントの繊維の巻かれたチーズ状パッケージを得た。 After applying an oil agent to the extruded molten multifilament in the same manner as in Example 1, the solid multifilament was wound around a roll heated to 50°C and having a peripheral speed of 2100 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.3 times.Then, using a winder that drives both the spindle and the touch roll, the multifilament was wound at a winding speed of 2600 m/min to obtain a cheese-like package wound with 72 dtex/72 filament fibers.
その後、パッケージに巻かれた繊維を30℃にて1.4倍延伸し、190℃の接触式加熱熱板ヒーターで加熱し、0.75倍で繊維を収縮させ、速度600m/minで巻取り、低収縮のポリトリメチレンテレフタレート繊維(鞘糸用糸条)を得た。
一方、芯糸用糸条として、ポリエステル(ポリエチレンテレフタレート)延伸糸(総繊度56dtex/36本、沸騰水収縮率13%)を用意した。
Thereafter, the fiber wound on the package was stretched to 1.4 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.75 times, and then wound up at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
On the other hand, a polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 13%) was prepared as a core yarn.
次いで、前記鞘糸用糸条と芯糸用糸条とを引き揃えて実施例1と同様にオ-バーフィード率1.5%でインターレース加工し、交絡数71個/mの空気混繊糸を得た。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。 Then, the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn with an entanglement rate of 71 entanglements/m. The physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
[実施例3]
実施例1と同様の方法でポリマーを作製した後、得られたポリマーを常法により乾燥し、水分を50ppmにした後、265℃で溶融させ、直径0.27mmの36個の孔の開いた一重配列の紡口を通して押出した。
[Example 3]
A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
押出された溶融マルチフィラメントに、実施例1と同様の方法で油剤を付着させた後、該固体マルチフィラメントを50℃に加熱した周速度2350m/分のロールに巻き付けた後、1.1倍で延伸されるように80℃の加熱したロールに巻き付け、その後スピンドルとタッチロールの双方を駆動する方式の巻取機を用いて、巻取速度2600m/分で巻き取って72dtex/36フィラメントの繊維の巻かれたチーズ状パッケージを得た。 After applying an oil agent to the extruded molten multifilament in the same manner as in Example 1, the solid multifilament was wound around a roll heated to 50°C and having a peripheral speed of 2350 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.1 times.Then, using a winder that drives both the spindle and the touch roll, the winding was performed at a winding speed of 2600 m/min to obtain a cheese-like package wound with 72 dtex/36 filament fibers.
その後、パッケージに巻かれた繊維を30℃にて1.6倍延伸し、190℃の接触式加熱熱板ヒーターで加熱し、0.65倍で繊維を収縮させ、速度600m/minで巻取り、低収縮のポリトリメチレンテレフタレート繊維(鞘糸用糸条)を得た。
一方、芯糸用糸条として、ポリエステルの2成分(ポリエチレンテレフタレート/ポリエチレンテレフタレート)を貼り合わせたコンジュゲート延伸糸(総繊度56dtex/24本、沸騰水収縮率17%)を用意した。
Thereafter, the fiber wound on the package was stretched to 1.6 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.65 times, and then wound up at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
On the other hand, a conjugate drawn yarn (total fineness 56 dtex/24 strands, boiling water shrinkage rate 17%) made by bonding two components of polyester (polyethylene terephthalate/polyethylene terephthalate) was prepared as a core yarn.
次いで、前記鞘糸用糸条と芯糸用糸条とを引き揃えて実施例1と同様にオ-バーフィード率1.5%でインターレース加工し、交絡数65個/mの空気混繊糸を得た。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。 Then, the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn with an entanglement rate of 65/m. The physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
[実施例4]
実施例1と同様の方法でポリマーを作製した後、得られたポリマーを常法により乾燥し、水分を50ppmにした後、265℃で溶融させ、直径0.27mmの36個の孔の開いた一重配列の紡口を通して押出した。
[Example 4]
A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
押出された溶融マルチフィラメントに、実施例1と同様の方法で油剤を付着させた後、該固体マルチフィラメントを50℃に加熱した周速度3000m/分のロールに巻き付けた後、1.2倍で延伸されるように80℃の加熱したロールに巻き付け、その後スピンドルとタッチロールの双方を駆動する方式の巻取機を用いて、巻取速度3600m/分で巻き取って56dtex/36フィラメントの繊維の巻かれたチーズ状パッケージを得た。 After applying an oil agent to the extruded molten multifilament in the same manner as in Example 1, the solid multifilament was wound around a roll heated to 50°C and having a peripheral speed of 3000 m/min, and then wound around a roll heated to 80°C so that it was stretched 1.2 times.Then, using a winder that drives both the spindle and the touch roll, the winding was performed at a winding speed of 3600 m/min to obtain a cheese-like package wound with 56 dtex/36 filament fibers.
その後、パッケージに巻かれた繊維を30℃にて1.3倍延伸し、190℃の接触式加熱熱板ヒーターで加熱し、0.85倍で繊維を収縮させ、速度600m/minで巻取り、低収縮のポリトリメチレンテレフタレート繊維(鞘糸用糸条)を得た。
一方、芯糸用糸条として、ポリエチレンテレフタレートとポリトリメチレンレテフタレートとを貼り合わせたコンジュゲート延伸糸(総繊度33dtex/24本、沸騰水収縮率21%)を用意した。
Thereafter, the fiber wound on the package was stretched to 1.3 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.85 times, and then wound up at a speed of 600 m/min to obtain a low-shrinkage polytrimethylene terephthalate fiber (sheath yarn).
On the other hand, a conjugate drawn yarn (total fineness 33 dtex/24 strands, boiling water shrinkage rate 21%) made by bonding together polyethylene terephthalate and polytrimethylene terephthalate was prepared as a core yarn.
次いで、前記鞘糸用糸条と芯糸用糸条とを引き揃えて実施例1と同様にオ-バーフィード率1.5%でインターレース加工し、交絡数71個/mの空気混繊糸を得た。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。 Then, the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn with an entanglement rate of 71 entanglements/m. The physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
[実施例5~6]
実施例1において、鞘糸用糸条の断面形状や単繊維数を表1に示す通り変更した以外は実施例1と同様に実施した。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。
[Examples 5 to 6]
The same procedure as in Example 1 was carried out, except that the cross-sectional shape of the sheath yarn and the number of single fibers were changed as shown in Table 1. The physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
[比較例1]
実施例1と同様の方法でポリマーを作製した後、得られたポリマーを常法により乾燥し、水分を50ppmにした後、265℃で溶融させ、直径0.27mmの36個の孔の開いた一重配列の紡口を通して押出した。
[Comparative Example 1]
A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
押出された溶融マルチフィラメントに、実施例1と同様の方法で油剤を付着させた後、該固体マルチフィラメントを55℃に加熱した周速度1500m/分のロールに巻き付けた後、2.1倍で延伸されるように130℃の加熱したロールに巻き付け、その後スピンドルとタッチロールの双方を駆動する方式の巻取機を用いて、巻取速度3000m/分で巻き取って72dtex/36フィラメントの繊維(鞘糸用ポリトリメチレンテレフタレート繊維糸条)の巻かれたチーズ状パッケージを得た。
一方、芯糸用糸条として、ポリエステル(ポリエチレンテレフタレート)延伸糸(総繊度56dtex/36本、沸騰水収縮率12%)を用意した。
An oil agent was applied to the extruded molten multifilament in the same manner as in Example 1, and the solid multifilament was then wound around a roll heated to 55° C. and having a peripheral speed of 1,500 m/min, and then wound around a roll heated to 130° C. so as to be stretched 2.1 times. Thereafter, the solid multifilament was wound at a winding speed of 3,000 m/min using a winder that drives both the spindle and the touch roll, to obtain a cheese-like package wound with a fiber of 72 dtex/36 filaments (polytrimethylene terephthalate fiber yarn for sheath yarn).
On the other hand, polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 12%) was prepared as a core yarn.
次いで、前記鞘糸用糸条と芯糸用糸条とを引き揃えて実施例1と同様にオ-バーフィード率1.5%でインターレース加工し、交絡数65個/mの空気混繊糸を得た。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。
得られた空気混繊糸は、芯鞘の糸足差が少なく膨らみに乏しいものであった。
Next, the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn having an entanglement number of 65/m. The physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
The air-mixed yarn obtained had a small core-sheath yarn length difference and was poor in swelling.
[比較例2]
実施例1と同様の方法でポリマーを作製した後、得られたポリマーを常法により乾燥し、水分を50ppmにした後、265℃で溶融させ、直径0.27mmの36個の孔の開いた一重配列の紡口を通して押出した。
[Comparative Example 2]
A polymer was prepared in the same manner as in Example 1, and then the resulting polymer was dried in a conventional manner to reduce the moisture content to 50 ppm. The polymer was then melted at 265°C and extruded through a single-layer spinneret having 36 holes with a diameter of 0.27 mm.
押出された溶融マルチフィラメントに、実施例1と同様の方法で油剤を付着させた後、該固体マルチフィラメントを55℃に加熱した周速度1500m/分のロールに巻き付けた後、2.1倍で延伸されるように130℃の加熱したロールに巻き付け、その後スピンドルとタッチロールの双方を駆動する方式の巻取機を用いて、巻取速度3000m/分で巻き取って56dtex/36フィラメントの繊維の巻かれたチーズ状パッケージを得た。 After applying an oil agent to the extruded molten multifilament in the same manner as in Example 1, the solid multifilament was wound around a roll heated to 55°C and having a peripheral speed of 1500 m/min, and then wound around a roll heated to 130°C so that it was stretched 2.1 times.Then, using a winder that drives both the spindle and the touch roll, the winding was performed at a winding speed of 3000 m/min to obtain a cheese-like package wound with 56 dtex/36 filament fibers.
その後、パッケージに巻かれた繊維を30℃にて1.05倍延伸し、190℃の接触式加熱熱板ヒーターで加熱し、0.92倍で繊維を収縮させ、速度600m/minで巻取って、トリトリメチレンテレフタレート繊維(鞘糸用糸条)を得た。
一方、芯糸用糸条として、ポリエステル(ポリエチレンテレフタレート)延伸糸(総繊度56dtex/36本、沸騰水収縮率10%)を用意した。
Thereafter, the fiber wound on the package was stretched to 1.05 times at 30°C, heated with a contact-type hot plate heater at 190°C, and shrunk to 0.92 times, and then wound up at a speed of 600 m/min to obtain tritrimethylene terephthalate fiber (yarn for sheath yarn).
On the other hand, a polyester (polyethylene terephthalate) drawn yarn (total fineness 56 dtex/36 strands, boiling water shrinkage rate 10%) was prepared as a core yarn.
次いで、前記鞘糸用糸条と芯糸用糸条とを引き揃えて実施例1と同様にオ-バーフィード率1.5%でインターレース加工し、交絡数63個/mの空気混繊糸を得た。得られたポリトリメチレンテレフタレート繊維の物性を表1に、混繊糸の物性を表2に示す。
得られた空気混繊糸は、鞘糸が堅く風合いに劣るものであった。
Next, the sheath yarn and the core yarn were aligned and interlaced at an overfeed rate of 1.5% in the same manner as in Example 1 to obtain an air-mixed yarn having an entanglement number of 63/m. The physical properties of the obtained polytrimethylene terephthalate fiber are shown in Table 1, and the physical properties of the mixed yarn are shown in Table 2.
The air-mixed yarn obtained had a stiff sheath yarn and was poor in feel.
本発明によれば、熱による収縮率が小さく、やわらかな風合いを有する布帛用の原糸を製造することが可能な、実質的にポリトリメチレンテレフタレートからなる低収縮繊維及びその製造方法、並びに該ポリトリメチレンテレフタレート繊維を含む空気混繊糸、及びそれからなる布帛を提供することができるので、その工業的価値は極めて大きい。 The present invention provides a low-shrinkage fiber essentially made of polytrimethylene terephthalate, which has a small thermal shrinkage rate and can be used to produce raw yarn for fabrics with a soft feel, a method for producing the same, an air-mixed yarn containing the polytrimethylene terephthalate fiber, and a fabric made from the same, and therefore has great industrial value.
Claims (13)
(糸足差の測定方法)
混繊糸を沸騰水下にて処理した後、0.1cN(0.098g)×空気混繊糸の総繊度(dtex)の荷重をとりつけて5cmの長さにカットし、カットした空気混繊糸から、ポリエステル系繊維A(単繊維)とポリトリメチレンテレフタレート繊維B(単繊維)とを取り出し、それぞれ、0.1cN(0.098g)×の単繊維繊度(dtex)の荷重をかけて長さを測定し、下記式により糸足差(%)を算出する。
糸足差(%)=(LB-LA)/LA×100
ただし、LAは芯糸のポリエステル系繊維の糸長(cm)であり、LBは鞘糸のポリトリメチレンテレフタレート繊維の糸長(cm)である。 An air-mixed core-sheath type air-mixed yarn obtained by heat-treating the air-mixed yarn according to claim 6, which is composed of a core yarn and a sheath yarn and has a total fineness of 30 to 400 dtex, wherein the core yarn is made of a polyester fiber, the sheath yarn is made of a polytrimethylene terephthalate fiber having a single fiber fineness of 0.3 to 10 dtex, and the yarn length difference between the core yarn and the sheath yarn, as defined by the following method, is 5% or more.
(Method of measuring thread length difference)
The mixed yarn was treated in boiling water, and then cut to a length of 5 cm under a load of 0.1 cN (0.098 g) × the total fineness (dtex) of the air-mixed yarn. From the cut air-mixed yarn, polyester fiber A (single fiber) and polytrimethylene terephthalate fiber B (single fiber) were taken out, and their lengths were measured under a load of 0.1 cN (0.098 g) × the single fiber fineness (dtex). The yarn length difference (%) was calculated using the following formula.
Thread length difference (%) = (LB-LA)/LA x 100
Here, LA is the yarn length (cm) of the polyester fiber core yarn, and LB is the yarn length (cm) of the polytrimethylene terephthalate fiber sheath yarn.
A fabric comprising the core-sheath type air-mixed yarn according to any one of claims 9 to 11.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202480025004.7A CN121002238A (en) | 2023-04-11 | 2024-04-02 | Polytrimethylene terephthalate fiber, process for producing the same, air-textured yarn comprising the same, and fabric comprising the same |
| JP2025513903A JPWO2024214591A1 (en) | 2023-04-11 | 2024-04-02 |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11107081A (en) * | 1997-10-02 | 1999-04-20 | Asahi Chem Ind Co Ltd | Production of composite processed yarn |
| JP2001131841A (en) * | 1999-10-25 | 2001-05-15 | Teijin Ltd | Polyester two layer structure yarn and method for producing the same |
| JP2001207329A (en) * | 1999-11-18 | 2001-08-03 | Toray Ind Inc | Polyester yarn and method for producing the same |
| JP2003129337A (en) * | 2001-10-19 | 2003-05-08 | Asahi Kasei Corp | Polytrimethylene terephthalate fiber and method for producing the same |
| JP2004232094A (en) * | 2003-01-28 | 2004-08-19 | Solotex Corp | Monofilament and method for producing the same |
| JP2006200096A (en) * | 2005-01-24 | 2006-08-03 | Solotex Corp | Polytrimethylene terephthalate based filament and method for spinning the same |
| WO2023068178A1 (en) * | 2021-10-19 | 2023-04-27 | 帝人フロンティア株式会社 | Polytrimethylene terephthalate fiber and method for producing same |
-
2024
- 2024-04-02 WO PCT/JP2024/013587 patent/WO2024214591A1/en active Pending
- 2024-04-02 JP JP2025513903A patent/JPWO2024214591A1/ja active Pending
- 2024-04-02 CN CN202480025004.7A patent/CN121002238A/en active Pending
- 2024-04-09 TW TW113113096A patent/TW202507101A/en unknown
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11107081A (en) * | 1997-10-02 | 1999-04-20 | Asahi Chem Ind Co Ltd | Production of composite processed yarn |
| JP2001131841A (en) * | 1999-10-25 | 2001-05-15 | Teijin Ltd | Polyester two layer structure yarn and method for producing the same |
| JP2001207329A (en) * | 1999-11-18 | 2001-08-03 | Toray Ind Inc | Polyester yarn and method for producing the same |
| JP2003129337A (en) * | 2001-10-19 | 2003-05-08 | Asahi Kasei Corp | Polytrimethylene terephthalate fiber and method for producing the same |
| JP2004232094A (en) * | 2003-01-28 | 2004-08-19 | Solotex Corp | Monofilament and method for producing the same |
| JP2006200096A (en) * | 2005-01-24 | 2006-08-03 | Solotex Corp | Polytrimethylene terephthalate based filament and method for spinning the same |
| WO2023068178A1 (en) * | 2021-10-19 | 2023-04-27 | 帝人フロンティア株式会社 | Polytrimethylene terephthalate fiber and method for producing same |
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| JPWO2024214591A1 (en) | 2024-10-17 |
| CN121002238A (en) | 2025-11-21 |
| TW202507101A (en) | 2025-02-16 |
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