WO2019135466A1 - High-strength polyethylene fiber having improved processability - Google Patents

High-strength polyethylene fiber having improved processability Download PDF

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Publication number
WO2019135466A1
WO2019135466A1 PCT/KR2018/011217 KR2018011217W WO2019135466A1 WO 2019135466 A1 WO2019135466 A1 WO 2019135466A1 KR 2018011217 W KR2018011217 W KR 2018011217W WO 2019135466 A1 WO2019135466 A1 WO 2019135466A1
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Prior art keywords
polyethylene
strength
melt index
fiber
polyethylene fiber
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PCT/KR2018/011217
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French (fr)
Korean (ko)
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김승훈
이민성
박종훈
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주식회사 휴비스
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Publication of WO2019135466A1 publication Critical patent/WO2019135466A1/en

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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/04Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D10/00Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
    • D01D10/02Heat treatment
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • D01D5/088Cooling filaments, threads or the like, leaving the spinnerettes
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • D01D5/096Humidity control, or oiling, of filaments, threads or the like, leaving the spinnerettes
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • D01D5/098Melt spinning methods with simultaneous stretching
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2321/00Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D10B2321/02Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins
    • D10B2321/021Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins polyethylene
    • D10B2321/0211Fibres made from polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds polyolefins polyethylene high-strength or high-molecular-weight polyethylene, e.g. ultra-high molecular weight polyethylene [UHMWPE]
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2401/00Physical properties
    • D10B2401/06Load-responsive characteristics
    • D10B2401/063Load-responsive characteristics high strength

Definitions

  • the present invention relates to a high strength polyethylene fiber having improved processability, and more particularly, to a high strength polyethylene fiber having improved processability by controlling the melt index of a polyethylene resin forming a polyethylene fiber.
  • Polyethylene resin is used for engineering plastics, films, fibers and nonwoven fabrics because of its low price, excellent chemical resistance and product processability.
  • textile field it is made of monofilaments and multifilaments, Applications are being expanded.
  • high-performance polyethylene fibers which require high strength and high elasticity according to the latest fiber trends.
  • a polyethylene resin having a number average molecular weight of 20,000 or more and a weight average molecular weight of 125,000 or less is melted at a spinning temperature of 220 to 335 ° C and extruded into a nozzle having 8 holes to obtain a hot- At a temperature of 200 to 335 DEG C at a minimum spinning speed of 30 m / min, and then stretched 20 times or more to produce fibers of 10 to 20 g / d.
  • this method has a limitation in the production rate due to the low spinning speed according to the nozzle odd number and the spin draw method in the commercial production of the polyethylene filament, and produces the polyethylene filament having excellent uniformity and radiation workability when producing tens to hundreds of multifilament .
  • Korean Patent No. 0909559 discloses a high strength polyethylene fiber having a weight average molecular weight of 300,000 or less and a ratio (Mw / Mn) of a weight average molecular weight to a number average molecular weight of 4.0 or less, .
  • Mw / Mn a ratio of a weight average molecular weight to a number average molecular weight of 4.0 or less
  • high-strength polyethylene fibers are excellent in cutting resistance and are widely used in industrial products such as safety gloves for industrial purposes.
  • the cutting resistance of conventional industrial products made of high-strength polyethylene fibers is a property of being manifested only by the strength of polyethylene fibers. There is a problem that the cut resistance may be lowered when the strength is not uniform or the strength is weakened at a specific portion.
  • high-strength polyethylene fibers using a solvent among high-strength polyethylene fibers produced by conventional techniques have a problem that the whiteness of the polyethylene fibers is lowered due to the influence of the solvent, which limits the use of the fibers.
  • the present invention has been made in an effort to solve the above problems of the prior art, and it is an object of the present invention to provide a polyethylene fiber having improved fixability by controlling the melt index ratio of a polyethylene resin forming high-
  • the polyethylene fiber according to the present invention is intended to provide a high-strength polyethylene fiber having improved cutting resistance by forming a node on the surface of the fiber.
  • the present invention relates to a polyethylene fiber, which is formed of a polyethylene resin and whose main repeating unit is ethylene, wherein the polyethylene resin has a melt index of 0.6 to 2 g / 10 min and a melt index ratio (HLMI / MI) of 20 to 40 Thereby providing the improved high strength polyethylene fiber.
  • a high strength polyethylene fiber having improved processability, wherein a plurality of nodules are formed on the surface of the polyethylene fiber.
  • the polyethylene resin has a molecular weight distribution index of 5 to 10, and provides a high-strength polyethylene fiber with improved processability.
  • the present invention provides a high-strength polyethylene fiber having improved processability, wherein the polyethylene fiber has a strength of 12 to 16 g / d.
  • the present invention also provides an article comprising the above polyethylene fibers.
  • the polyethylene article has a level of 3 or more according to the cutting resistance standard.
  • the polyethylene article has an intrinsic breaking strength of 4.0 N or more.
  • the high-strength polyethylene fiber having improved processability according to the present invention has a high strength and multi-step stretchability by using a polyethylene resin whose melt index ratio is adjusted to 20 to 40, and has an excellent strength.
  • the yarn has a small number of spinning and stretching yarns, It is effective.
  • the high-strength polyethylene fiber of the present invention has an effect of increasing the surface area of the fiber, such as a bamboo shape, on the surface thereof, and lubricating the blade when the blade is in contact with the blade.
  • FIG. 1 is a photograph showing a high-strength polyethylene fiber with improved processability according to the present invention.
  • &quot As used herein, the terms " about, " " substantially, " " etc. ", when used to refer to a manufacturing or material tolerance inherent in the stated sense, Accurate or absolute numbers are used to help prevent unauthorized exploitation by unauthorized intruders of the referenced disclosure.
  • the melt index ratio means a ratio (HLMI / MI) of a high load melt index (HLMI) to a melt index (MI).
  • the high load melt index (HLMI) Melt Index (MI) means the weight discharged when the measurement temperature is 190 ° C and the weight is 2.16 kg.
  • FIG. 1 is a photograph showing a high-strength polyethylene fiber with improved processability according to the present invention.
  • the present invention relates to a polyethylene fiber which is formed of a polyethylene resin and whose main repeating unit is ethylene.
  • the polyethylene resin is a high-strength polyethylene having a melt index of 0.6 to 2 g / 10 min and a melt index ratio (HLMI / MI) Fiber.
  • the polyethylene resin forming the high-strength polyethylene fiber of the present invention preferably uses a polyethylene resin having a melt index of 0.6 to 2.0 g / 10 min, preferably 0.8 to 1.4 g / 10 min.
  • melt index is less than 0.6 g / 10 min, the flowability of the melt of the polyethylene resin in the extruder is not good and the spinning speed can not be increased, which may cause problems such as nozzle face refinement during spinning.
  • melt index exceeds 2.0 g / 10 min, the spinning workability is excellent, but the flowability at an appropriate spinning temperature is not suitable, and it may be difficult to obtain polyethylene fibers having high strength after stretching.
  • the polyethylene resin forming the high-strength polyethylene fiber of the present invention preferably has a melt index ratio (HLMI / MI) adjusted to 20 to 40.
  • Polyethylene resin having a melt index ratio of less than 20 requires control of polyethylene raw material, catalyst technology, and dedicated equipment for the catalyst only, and is difficult to control at less than 20 in raw material companies because of high density control, and manufacturing reproducibility is poor.
  • melt index ratio is 40 or more, high stretch ratio and multi-step stretching are difficult during spinning, stretching, low strength, and cut resistance.
  • the polyethylene resin used in the present invention preferably has a weight average molecular weight (Mw) of 100,000 to 300,000 and a molecular weight distribution index (weight average molecular weight / number average molecular weight, Mw / Mn) of 5 to 10.
  • weight average molecular weight (Mw) is less than 100,000, the spinning workability of spinning is improved, but there is a limit in manifesting high strength.
  • weight average molecular weight is more than 300,000, Workability can be adversely affected.
  • the molecular weight distribution index is less than 5, high-magnification elongation of 10 times or more is required in order to exhibit high strength, and defects of the mowing and elongating rollers are increased, which may deteriorate quality as the number of stretching is increased.
  • the molecular weight distribution index is more than 10, since a large number of high molecular weight polyethylene and low molecular weight polyethylene in polyethylene resin are mixed, a smooth drawing process can not be performed, and thus there is a limitation in expressing high strength.
  • the polyethylene fiber of the present invention in which the repeating unit is substantially ethylene has a node like the bamboo shape of the surface shape of the fiber as shown in Fig.
  • the node is repeatedly formed as a curved portion curved inward between the protruded node portion and the node portion.
  • the nodes formed on the surface of the fiber increase the surface area of the fiber and lubricate when the blade contacts, thereby improving the cut resistance.
  • the nodules formed on the fiber surface irregularly reflect light, thereby improving the whiteness of the fiber.
  • the improvement of cutting resistance and whiteness due to nodules may be insignificant.
  • the number of nodules exceeds 10, Can be degraded.
  • the high-strength polyethylene fiber having improved processability according to the present invention may be produced by melt spinning to form an undrawn yarn and a drawing step to draw the non-drawn yarn.
  • the step of forming a non-drawn filament by the melt-spinning comprises melting the polyethylene resin having the controlled molecular weight distribution index and melt index in an extruder, spinning it at a low speed of 1000 m / min or less by installing a nozzle hot tube, Can be produced.
  • the inside of the extruder can be divided into four zones, and the temperature range of each temperature zone can be set to 200 to 270 ° C, preferably 220 to 250 ° C.
  • the temperature range is less than 200 ° C, the uniformity of the non-drawn yarn is good, but there is a high possibility of occurrence of static electricity during spinning, and the workability in the stretching process is low.
  • the temperature range is higher than 270 ⁇ , the stretching magnification can be improved in the stretching step, but cooling and solidification of the unstretched yarn becomes difficult to lower the uniformity of the unstretched yarn, and the number of stretch- Can fall.
  • the spinning nozzle for spinning may be from 60 to 400 holes to produce a high strength polyethylene fiber having improved processability of the present invention.
  • the non-drawn yarn produced as described above can be subjected to the stretching step using a multi-stage stretching roller.
  • the high-strength polyethylene fiber with improved processability of the present invention is stretched by a three-stage stretching process, wherein the stretching temperature is from 60 to 100 ⁇ ⁇ , the stretching temperature is from 80 to 120 ⁇ ⁇ and the stretching temperature is from 100 to 120 ⁇ ⁇ Lt; / RTI >
  • the two-step stretching temperature is higher than the first-step stretching temperature
  • the third-step stretching temperature is also preferably higher than the second-step stretching temperature
  • the melt of the fibers may occur on the surface of the rollers, resulting in an increase in the number of times the surface of the rollers is cut and the number of the rollers is increased.
  • the three-step stretching is carried out in order to fix the fiber heat and to prevent the fiber from shrinking, and it is preferable that the stretching is practically carried out in the first-stage and second-stage stretching.
  • the nodes of the surface of the high-strength polyethylene fiber according to the present invention are presumed to be formed by the use of the polyethylene resin whose molecular weight distribution index and melt index are controlled and the step of stretching as described above. And it is presumed that the nodes formed in the three-step stretching step are fixed.
  • the total draw ratio DR When the total draw ratio DR is lower than 6, the strength of the polyethylene fibers is lowered. When the total draw ratio DR is higher than 10, the filament is more likely to occur during drawing, May be deteriorated.
  • the high-strength polyethylene fiber having improved processability according to the present invention formed by using and stretching the polyethylene resin whose molecular weight distribution index and melt index are controlled has a strength of 12 to 16 g / d, a mono-fineness of 0.5 to 2.5, And the number of strands is 60 to 400.
  • the high strength polyolefin fibers may also be used in a wide variety of other types of articles.
  • Non-limiting examples include, for example, insulating materials for refrigeration units (e.g., refrigerators, freezers, vending machines, etc.); Automotive parts (eg, front or back sheet, headrest, arm rest, donor panel, rear shelf / package tray, steering wheel and interior trim, dashboard, etc); Architectural panels and components (eg roofs, wall joints, underfloor, etc.); Clothing (eg, coat, shirt, trousers, gloves, apron, work clothes, shoes, boots, hats, sock liner etc); Furniture and bedding (eg, sleeping bags, comforters, etc.); Fluid storage / transfer systems (eg, liquid / gas hydrocarbons, liquid nitrogen, oxygen, hydrogen, or crude oil pipes or tanks); Extreme environments (eg underwater or universe); Food and beverage products (eg cups, cup holders, plates, etc.); Containers and bottles; And the like.
  • insulating materials for refrigeration units e.g., refrigerators, freezers, vending machines, etc.
  • Automotive parts eg, front or back sheet, headrest,
  • the polyolefin fibers can be used in "garments" which means that they include any article having a shape that is generally adapted to a portion of the body.
  • items include, but are not limited to, clothing (e.g., shirts, trousers, jeans, slacks, skirts, coats, activewear, sportswear, aerobics and gym clothes, swimwear, cycling jerseys or shorts, bathing suit, lace suit, sweat suit, body suit, etc.); Footwear (for example, shoes, socks, boots, etc.); (E.g., undergarment, undergarment, undergarment, undergarment, undergarment, undergarment, undergarment, t-shirts, etc.), compression garments, and hanging garments (e.g., kilt nappa, toga, poncho, cloak, shawl, etc.).
  • clothing e.g., shirts, trousers, jeans, slacks, skirts, coats, activewear, sportswear, aerobics and gym clothes
  • a polyethylene resin having a melt index of 0.6 to 2 g / 10 min and a molecular weight distribution index of 5 to 10 is put into an extruder to extrude the molten polymer and cooled using a cooling device, And an unstiffened yarn with an emulsion was wound thereon, and the unstretched yarn was subjected to stretching and heat treatment. Thereafter, a high strength polyethylene fiber with improved processability according to the present invention was produced by winding using an interlocking device and a winder.
  • the stretching was performed by a three-stage stretching using a multi-stage stretching roller.
  • the stretching was carried out at a stretching temperature of about 70 ⁇ ⁇ , a stretching temperature of about 92 ⁇ ⁇ of about 3 ⁇ ⁇ , and a stretching temperature of about 105 ⁇ Respectively.
  • the weight average molecular weight, the molecular weight distribution index, the melt index, the melt index ratio, and the total draw ratio (DR) were the same as in Tables 3 and 4 and the other spinning conditions were the same in the respective Examples and Comparative Examples.
  • FIG. 1 is a SEM photograph of a polyethylene fiber of Example 1 showing that nodes are formed at regular intervals.
  • the strength, the occurrence frequency, the index of cut resistance, the level and the breaking strength of the examples 1 to 5 and the comparative examples 1 to 5 were measured.
  • the index of cut resistance, level and endurance were measured after knitting with the polyethylene fibers of Examples 1 to 5 and Comparative Examples 1 to 5.
  • Table 3 shows the blade occurrence frequency, cutting resistance level and cutting strength of the examples.
  • Table 3 shows the blade occurrence frequency, cutting strength level and cutting strength of the comparative examples.
  • Measurement of melt index Measured according to ASTM D1238dp. The measurement temperature was 190 ° C, and the weight was defined as 21.6 kg of high-load melt index and 2.16 kg of melt index. Preheating was performed for 5 minutes and free run for 3 minutes , And the value measured 10 times was defined as an average value.
  • Strength is defined as the value of g / d divided by the denier, when the tensile fibers are cut, by holding the fibers in an universal testing machine and applying tensile load at the above speed to yield a stress-strain curve.
  • Mesdan Yarn cut tester a device manufactured in accordance with EN388 standard, was used to evaluate the cut resistance of fabric or knitted fabric. The measurement was performed by placing an aluminum foil wrapped with a filter paper on a rubber support, placing the control sample and the test sample, measuring the control sample and the test sample five times before the test, and evaluating the index as follows.
  • Control specimen TTest specimen CControl specimen IIndex One C 1 T 1 C 2 i1 2 C 2 T 2 C 3 i2 3 C 3 T 3 C 4 i3 4 C 4 T 4 C 5 i4 5 C 5 T 5 C 6 i5
  • Cutting force (N) The method of evaluating the cutting force of a fabric or a knitted fabric was a model STM610 of Satara, manufactured according to the ISO13997 standard. Cutting is measured by the cutting force required when cutting the material to a blade quality of 20 mm when the range of force is applied to the blade perpendicular to the surface of the sample. The measuring sequence is a gradual application of a constant force between the sample and the blade. And repeat the test with different forces until at least 15 records with a cut length between 5 mm and 50 mm are obtained.
  • the cutting force is obtained in the range of 5 mm to 15 mm, 15 mm to 30 mm, and 30 mm to 50 mm, and the value obtained by multiplying the correction factor C by the cutting length is plotted and the force at a cutting length of 20 mm is measured by the cutting force.
  • C is a correction coefficient
  • l is 5.0N neoprene phase cutting operation length mm
  • K 20
  • Example 1 Example 2
  • Example 3 Example 4
  • Example 5 Weight average molecular weight (g / mol) 250000 250000 250000 110000 130000 Molecular weight distribution index 7.6 7.8 7.6 5.8 7.8
  • the melt index (g / 10 min) 0.9 0.75 0.9 1.2 1.2 Melt index ratio (HLMI / MI) 31 38 31 26 38 Drawing Ratio (DR) 8 7.8 8 8.8 7.5

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  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
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Abstract

The present invention relates to a high-strength polyethylene fiber having improved processability, the polyethylene fiber being formed from a polyethylene resin, thereby having ethylene as a major repeating unit thereof, wherein the polyethylene resin has a melt index of 0.6 to 2g/10min, and a melt index ratio (HLMI/MI) of 20 to 40.

Description

공정성이 향상된 고강도 폴리에틸렌 섬유High Strength Polyethylene Fiber with Improved Fairness
본 발명은 공정성이 향상된 고강도 폴리에틸렌 섬유에 관한 것으로, 구체적으로 폴리에틸렌 섬유를 형성하는 폴리에틸렌 수지의 용융지수를 조절하여 공정성이 향상된 고강도 폴리에틸렌 섬유에 관한 것이다.The present invention relates to a high strength polyethylene fiber having improved processability, and more particularly, to a high strength polyethylene fiber having improved processability by controlling the melt index of a polyethylene resin forming a polyethylene fiber.
폴리에틸렌 수지는 가격이 저렴하고, 내화학성, 제품 가공성이 우수하여, 엔지니어링 플라스틱, 필름, 섬유 및 부직포 용도로 활용이 증가되고 있으며, 섬유 분야에서는 모노필라멘트 및 멀티필라멘트로 제조되어 의류용, 산업용 등으로 용도가 확대되고 있다. 특히 최신 섬유 동향에 따라 고강도 및 고탄성률을 요구하는 고 기능성 폴리에틸렌 섬유에 관한 관심이 증가하고 있다.Polyethylene resin is used for engineering plastics, films, fibers and nonwoven fabrics because of its low price, excellent chemical resistance and product processability. In the textile field, it is made of monofilaments and multifilaments, Applications are being expanded. Particularly, there is an increasing interest in high-performance polyethylene fibers which require high strength and high elasticity according to the latest fiber trends.
미국특허 제4,228,118호에서는 수평균분자량이 20,000 이상, 중량평균분자량이 125,000 이하인 폴리에틸렌 수지를 사용하여 방사온도 220 내지 335℃에서 용융한 후 8홀인 노즐에 압출하여 열연신온도 115 내지 132℃, 핫 튜브온도 200 내지 335℃를 두고 최소 방사속도 30m/min로 권취한 후 20배 이상 연신하여 10 내지 20g/d의 섬유를 제조하였다. 하지만, 이러한 방법은 폴리에틸렌 섬유의 상업적인 제조에 있어 노즐 홀수 및 스핀드로우 방법에 따른 방사속도가 낮아 생산량에 한계가 있으며, 수십 내지 수백의 멀티필라멘트를 생산할 때 균제도 및 방사 작업성이 우수한 폴리에틸렌 섬유를 생산하는데 어려움이 있다.In U.S. Patent No. 4,228,118, a polyethylene resin having a number average molecular weight of 20,000 or more and a weight average molecular weight of 125,000 or less is melted at a spinning temperature of 220 to 335 ° C and extruded into a nozzle having 8 holes to obtain a hot- At a temperature of 200 to 335 DEG C at a minimum spinning speed of 30 m / min, and then stretched 20 times or more to produce fibers of 10 to 20 g / d. However, this method has a limitation in the production rate due to the low spinning speed according to the nozzle odd number and the spin draw method in the commercial production of the polyethylene filament, and produces the polyethylene filament having excellent uniformity and radiation workability when producing tens to hundreds of multifilament .
또한, 대한민국 등록특허 제0909559호에서는 중량평균분자량이 300,000이하이고, 분자량분포지수인 중량평균분자량과 수평균분자량의 비(Mw/Mn)가 4.0이하이며, 고강도를 발현하는 고강도 폴리에틸렌 섬유에 대해 명시하고 있다. 하지만, 원료의 분자량분포지수를 4.0 이하로 제어하기가 어려우며, 분자량분포지수가 낮게 형성되어 고강도를 발현하기 위해서는 10배 이상 고연신이 필요하여 방사작업성 등이 공정성이 저하되는 문제점이 있다.In addition, Korean Patent No. 0909559 discloses a high strength polyethylene fiber having a weight average molecular weight of 300,000 or less and a ratio (Mw / Mn) of a weight average molecular weight to a number average molecular weight of 4.0 or less, . However, it is difficult to control the molecular weight distribution index of the raw material to 4.0 or less. In order to form a low molecular weight distribution index and exhibit high strength, 10 times or more of high stretching is required.
일반적으로 고강도 폴리에틸렌 섬유는 내절단성이 우수하여 산업용 안전장갑 등 산업용 물품으로 많이 사용되고 있으나, 종래의 고강도 폴리에틸렌 섬유로 제조되는 산업용 물품의 내절단성은 폴리에틸렌 섬유의 강도로만 발현되는 물성으로 고강도 폴리에틸렌 섬유의 강도가 균일하지 못하거나 특정 부분에서 강도가 약화될 경우 내절단성이 저하될 수 있는 문제점이 있었다.Generally, high-strength polyethylene fibers are excellent in cutting resistance and are widely used in industrial products such as safety gloves for industrial purposes. However, the cutting resistance of conventional industrial products made of high-strength polyethylene fibers is a property of being manifested only by the strength of polyethylene fibers. There is a problem that the cut resistance may be lowered when the strength is not uniform or the strength is weakened at a specific portion.
더불어, 종래의 기술로 생산된 고강도 폴리에틸렌 섬유 중 용매를 사용하는 고강도 폴리에틸렌 섬유는 용매의 영향으로 폴리에틸렌 섬유의 백색도가 저하되어 사용용도가 제한되는 문제점이 있었다.In addition, high-strength polyethylene fibers using a solvent among high-strength polyethylene fibers produced by conventional techniques have a problem that the whiteness of the polyethylene fibers is lowered due to the influence of the solvent, which limits the use of the fibers.
본 발명은 상기와 같은 종래기술의 문제점을 해결하기 위해 발명된 것으로 고강도 폴리에틸렌 섬유를 형성하는 폴리에틸렌 수지의 용융지수비가 조절되어 고정성이 향상된 폴리에틸렌 섬유를 제공하고자 한다.Disclosure of Invention Technical Problem [8] Accordingly, the present invention has been made in an effort to solve the above problems of the prior art, and it is an object of the present invention to provide a polyethylene fiber having improved fixability by controlling the melt index ratio of a polyethylene resin forming high-
또한, 본 발명에 의한 폴리에틸렌 섬유는 섬유 표면에 마디를 형성하여 내절단성이 향상된 고강도 폴리에틸렌 섬유를 제공하고자 한다.Also, the polyethylene fiber according to the present invention is intended to provide a high-strength polyethylene fiber having improved cutting resistance by forming a node on the surface of the fiber.
본 발명은 폴리에틸렌 수지로 형성되어 주요 반복 단위가 에틸렌인 폴리에틸렌 섬유로서, 상기 폴리에틸렌 수지는 용융지수가 0.6 내지 2g/10min이고, 용융지수비(HLMI/MI)가 20 내지 40인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유를 제공한다.The present invention relates to a polyethylene fiber, which is formed of a polyethylene resin and whose main repeating unit is ethylene, wherein the polyethylene resin has a melt index of 0.6 to 2 g / 10 min and a melt index ratio (HLMI / MI) of 20 to 40 Thereby providing the improved high strength polyethylene fiber.
또한, 상기 폴리에틸렌 섬유의 표면에 다수의 마디부가 형성되는 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유를 제공한다.Further, there is provided a high strength polyethylene fiber having improved processability, wherein a plurality of nodules are formed on the surface of the polyethylene fiber.
또한, 상기 폴리에틸렌 수지는 분자량 분포지수가 5 내지 10인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유를 제공한다.Further, the polyethylene resin has a molecular weight distribution index of 5 to 10, and provides a high-strength polyethylene fiber with improved processability.
또한, 상기 폴리에틸렌 섬유의 강도가 12 내지 16g/d인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유를 제공한다.Further, the present invention provides a high-strength polyethylene fiber having improved processability, wherein the polyethylene fiber has a strength of 12 to 16 g / d.
또한, 상기의 폴리에틸렌 섬유를 포함하는 것을 특징으로하는 물품을 제공한다.The present invention also provides an article comprising the above polyethylene fibers.
또한, 상기 폴리에틸렌 물품은 내절단성 규격에 의한 레벨(Level)이 3 이상인 것을 특징으로 하는 물품을 제공한다.In addition, the polyethylene article has a level of 3 or more according to the cutting resistance standard.
또한, 상기 폴리에틸렌 물품은 내절단력이 4.0N 이상인 것을 특징으로 하는 물품을 제공한다.Further, the polyethylene article has an intrinsic breaking strength of 4.0 N or more.
본 발명에 따른 공정성이 향상된 고강도 폴리에틸렌 섬유는 용융지수비가 20내지 40로 조절된 폴리에틸렌 수지를 이용하여 고배율, 다단연신이 가능하여 강도가 우수한 효과가 있으며 방사, 연신 사절수가 최소화되어 공정 작업성이 우수한 효과가 있다.The high-strength polyethylene fiber having improved processability according to the present invention has a high strength and multi-step stretchability by using a polyethylene resin whose melt index ratio is adjusted to 20 to 40, and has an excellent strength. The yarn has a small number of spinning and stretching yarns, It is effective.
또한, 본 발명의 고강도 폴리에틸렌 섬유는 표면에 대나무 형상과 같은 마디가 형성되어, 섬유 표면적을 증가시키고, 내절단성 측정 시 칼날이 접촉하였을 때 윤활작용을 하여 내절단성이 향상되는 효과가 있다.In addition, the high-strength polyethylene fiber of the present invention has an effect of increasing the surface area of the fiber, such as a bamboo shape, on the surface thereof, and lubricating the blade when the blade is in contact with the blade.
도 1은 본 발명에 의한 공정성이 향상된 고강도 폴리에틸렌 섬유를 나타낸 사진이다.1 is a photograph showing a high-strength polyethylene fiber with improved processability according to the present invention.
이하 본 발명에 첨부된 도면을 참조하여 본 발명의 바람직한 일실시예를 상세히 설명하기로 한다. 우선, 도면들 중, 동일한 구성요소 또는 부품들은 가능한 동일한 참조부호를 나타내고 있음에 유의하여야 한다. 본 발명을 설명함에 있어, 관련된 공지기능 혹은 구성에 대한 구체적인 설명은 본 발명의 요지를 모호하지 않게 하기 위하여 생략한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. First, it should be noted that, in the drawings, the same components or parts have the same reference numerals as much as possible. In the following description of the present invention, a detailed description of known functions and configurations incorporated herein will be omitted so as to avoid obscuring the subject matter of the present invention.
본 명세서에서 사용되는 정도의 용어 '약', '실질적으로' 등은 언급된 의미에 고유한 제조 및 물질 허용오차가 제시될 때 그 수치에서 또는 그 수치에 근접한 의미로 사용되고, 본 발명의 이해를 돕기 위해 정확하거나 절대적인 수치가 언급된 개시 내용을 비양심적인 침해자가 부당하게 이용하는 것을 방지하기 위해 사용된다.As used herein, the terms " about, " " substantially, " " etc. ", when used to refer to a manufacturing or material tolerance inherent in the stated sense, Accurate or absolute numbers are used to help prevent unauthorized exploitation by unauthorized intruders of the referenced disclosure.
본 발명에서 용융지수비는 고하중용융지수(HLMI)와 용융지수(MI)의 비(HLMI/MI)를 의미하는 것으로 상기 고하중용융지수(High Load Melt Index, HLMI)는 측정온도 190℃, 추 무게 21.6kg 일 때 10분당 토출되는 무게이고, 용융지수(Melt Index, MI)는 측정온도 190℃, 추 무게 2.16kg일 때 토출되는 무게 값을 의미한다. In the present invention, the melt index ratio means a ratio (HLMI / MI) of a high load melt index (HLMI) to a melt index (MI). The high load melt index (HLMI) Melt Index (MI) means the weight discharged when the measurement temperature is 190 ° C and the weight is 2.16 kg.
도 1은 본 발명에 의한 공정성이 향상된 고강도 폴리에틸렌 섬유를 나타낸 사진이다.1 is a photograph showing a high-strength polyethylene fiber with improved processability according to the present invention.
본 발명은 폴리에틸렌 수지로 형성되어 주요 반복 단위가 에틸렌인 폴리에틸렌 섬유로서, 상기 폴리에틸렌 수지는 용융지수가 0.6 내지 2g/10min이고, 용융지수비(HLMI/MI)가 20 내지 40인 공정성이 향상된 고강도 폴리에틸렌 섬유에 관한 것이다.The present invention relates to a polyethylene fiber which is formed of a polyethylene resin and whose main repeating unit is ethylene. The polyethylene resin is a high-strength polyethylene having a melt index of 0.6 to 2 g / 10 min and a melt index ratio (HLMI / MI) Fiber.
본 발명의 고강도 폴리에틸렌 섬유를 형성하는 폴리에틸렌 수지는 용융지수가 0.6 내지 2.0g/10min이고, 바람직하게는 0.8 내지 1.4g/10min인 폴리에틸렌 수지를 사용하는 것이 바람직할 것이다.The polyethylene resin forming the high-strength polyethylene fiber of the present invention preferably uses a polyethylene resin having a melt index of 0.6 to 2.0 g / 10 min, preferably 0.8 to 1.4 g / 10 min.
상기 용융지수가 0.6g/10min미만이면 압출기 내 폴리에틸렌 수지의 용융액의 흐름성이 좋지 못하여 방사속도를 높일 수 없고, 방사시 노즐면 사절 등의 원인으로 작용하는 문제가 발생할 수 있다. 또한, 용융지수가 2.0g/10min을 초과하는 경우 방사 작업성은 우수하나, 적정 방사온도에서 흐름성이 적합하지 않아 연신 후 고강도의 폴리에틸렌 섬유를 수득하기가 어려울 수 있다.If the melt index is less than 0.6 g / 10 min, the flowability of the melt of the polyethylene resin in the extruder is not good and the spinning speed can not be increased, which may cause problems such as nozzle face refinement during spinning. When the melt index exceeds 2.0 g / 10 min, the spinning workability is excellent, but the flowability at an appropriate spinning temperature is not suitable, and it may be difficult to obtain polyethylene fibers having high strength after stretching.
또한, 본 발명의 고강도 폴리에틸렌 섬유를 형성하는 폴리에틸렌 수지는 용융지수비(HLMI/MI)가 20 내지 40로 조절되는 것이 바람직할 것이다.In addition, the polyethylene resin forming the high-strength polyethylene fiber of the present invention preferably has a melt index ratio (HLMI / MI) adjusted to 20 to 40. [
상기 용융지수비가 20미만인 폴리에틸렌 수지는 폴리에틸렌 원부원료 제어, 촉매 기술, 해당 촉매만을 위한 전용설비가 필요하며 고밀도로 제어해야 하기에 원료업체에서 20 미만으로 제어하기에는 어려우며 제조 재현성이 떨어진다. 또한, 용융지수비가 40 이상인 경우, 방사 후 연신 시 고배율, 다단연신이 어려우며, 강도가 낮고, 내절단성이 저하될 수 있다.Polyethylene resin having a melt index ratio of less than 20 requires control of polyethylene raw material, catalyst technology, and dedicated equipment for the catalyst only, and is difficult to control at less than 20 in raw material companies because of high density control, and manufacturing reproducibility is poor. When the melt index ratio is 40 or more, high stretch ratio and multi-step stretching are difficult during spinning, stretching, low strength, and cut resistance.
또한, 본 발명에서 사용되는 폴리에틸렌 수지는 중량평균분자량(Mw)이 100,000 내지 300,000이고, 분자량분포지수(중량평균분자량/수평균분자량, Mw/Mn)가 5 내지 10인 것이 바람직할 것이다.The polyethylene resin used in the present invention preferably has a weight average molecular weight (Mw) of 100,000 to 300,000 and a molecular weight distribution index (weight average molecular weight / number average molecular weight, Mw / Mn) of 5 to 10.
상기 중량평균분자량(Mw)이 100,000 미만일 경우에는 방사시 방사 작업성이 좋아지나 고강도를 발현하는데 한계가 있고, 300,000을 초과하는 경우에는 용융방사시 압출기 내부에서 수지의 흐름성에 영향을 끼쳐 방사 균제도 및 작업성이 불리하게 작용할 수 있다.When the weight average molecular weight (Mw) is less than 100,000, the spinning workability of spinning is improved, but there is a limit in manifesting high strength. When the weight average molecular weight is more than 300,000, Workability can be adversely affected.
상기 분자량분포지수가 5 미만일 경우에는 고강도를 발현하기 위해서 10배 이상의 고배율 연신이 필요하고, 그에 따른 모우나 연신롤러의 결점이 증가하여 연신사절횟수가 증가함에 따라 품질을 떨어뜨릴 수 있다. 또한, 분자량분포지수가 10을 초과하는 경우 폴리에틸렌 수지 내 고분자량 폴리에틸렌과 저분자량 폴리에틸렌이 다수 혼재되어 있어 원활한 연신공정이 이루어질 수 없고, 그에 따라 고강도를 발현하는데 제한이 있다.When the molecular weight distribution index is less than 5, high-magnification elongation of 10 times or more is required in order to exhibit high strength, and defects of the mowing and elongating rollers are increased, which may deteriorate quality as the number of stretching is increased. In addition, when the molecular weight distribution index is more than 10, since a large number of high molecular weight polyethylene and low molecular weight polyethylene in polyethylene resin are mixed, a smooth drawing process can not be performed, and thus there is a limitation in expressing high strength.
상기와 같은 폴리에틸렌 수지를 사용하여 반복 단위가 실질적으로 에틸렌인 본 발명의 폴리에틸렌 섬유는 도 1에서와 같이 섬유의 표면형상이 대나무 형상과 같이 마디가 형성된다.Using the polyethylene resin as described above, the polyethylene fiber of the present invention in which the repeating unit is substantially ethylene has a node like the bamboo shape of the surface shape of the fiber as shown in Fig.
상기 마디는 돌출된 마디부와 상기 마디부의 사이가 내측으로 만곡된 만곡부로 반복적으로 형성된다.The node is repeatedly formed as a curved portion curved inward between the protruded node portion and the node portion.
상기와 같이 섬유 표면에 형성되는 마디는 섬유 표면적을 증가시키고, 칼날이 접촉하였을 때 윤활작용을 하여 내절단성이 향상시킨다.As described above, the nodes formed on the surface of the fiber increase the surface area of the fiber and lubricate when the blade contacts, thereby improving the cut resistance.
또한, 섬유 표면에 형성되는 마디는 빛을 난반사시켜 섬유의 백색도를 향상시키게 된다.In addition, the nodules formed on the fiber surface irregularly reflect light, thereby improving the whiteness of the fiber.
또한, 상기 마디부는 100㎛당 5~10개를 가지는 것이 바람직한 것으로 5개 미만인 경우에는 마디부로 인한 내절단성 향상 효율 및 백색도 향상이 미미할 수 있으며, 10개를 초과한 경우에는 연신율이 낮아져 강도가 저하될 수 있다.In addition, when the number of the nodules is less than 5, the improvement of cutting resistance and whiteness due to nodules may be insignificant. When the number of nodules exceeds 10, Can be degraded.
상기와 같은 본 발명에 따른 공정성이 향상된 고강도 폴리에틸렌 섬유는 용융방사하여 미연신사를 형성하는 단계와 미연신사를 연신하는 연신단계로 제조될 수 있다.The high-strength polyethylene fiber having improved processability according to the present invention may be produced by melt spinning to form an undrawn yarn and a drawing step to draw the non-drawn yarn.
상기 용융방사하여 미연신사를 형성하는 단계는 상기 분자량분포지수와 용융지수가 제어된 폴리에틸렌 수지를 압출기에서 용융시키고, 노즐 핫튜브를 설치하여 1000m/min 이하의 저속으로 방사하고, 냉각 고화하여 미연신사를 제조할 수 있다. The step of forming a non-drawn filament by the melt-spinning comprises melting the polyethylene resin having the controlled molecular weight distribution index and melt index in an extruder, spinning it at a low speed of 1000 m / min or less by installing a nozzle hot tube, Can be produced.
상기 압출기의 내부는 온도 존(zone)을 4구역으로 나눌 수 있고, 각 온도 존의 온도범위는 200 내지 270℃, 바람직하게는 220 내지 250℃로 설정할 수 있다. 상기 온도범위가 200℃ 미만인 경우는 미연신사의 균제도가 좋아지나 방사시 정전기 발생 가능성이 높고, 연신공정에서 작업성이 떨어진다. 또한, 상기 온도범위가 270℃를 초과할 경우, 연신공정에서 연신배율을 향상시킬 수는 있으나, 미연신사의 냉각 고화가 어려워져 미연신사의 균제도가 저하되고, 연신시 연신사절횟수가 증가하여 품질이 떨어질 수 있다. The inside of the extruder can be divided into four zones, and the temperature range of each temperature zone can be set to 200 to 270 ° C, preferably 220 to 250 ° C. When the temperature range is less than 200 ° C, the uniformity of the non-drawn yarn is good, but there is a high possibility of occurrence of static electricity during spinning, and the workability in the stretching process is low. If the temperature range is higher than 270 캜, the stretching magnification can be improved in the stretching step, but cooling and solidification of the unstretched yarn becomes difficult to lower the uniformity of the unstretched yarn, and the number of stretch- Can fall.
상기 방사 시 방사노즐은 60홀 내지 400홀인 것이 사용하여 본 발명의 공정성이 향상된 고강도 폴리에틸렌 섬유를 제조할 수 있다.The spinning nozzle for spinning may be from 60 to 400 holes to produce a high strength polyethylene fiber having improved processability of the present invention.
상기와 같이 제조되는 미연신사는 다단연신롤러를 사용하여 연신단계를 실시할 수 있다.The non-drawn yarn produced as described above can be subjected to the stretching step using a multi-stage stretching roller.
본 발명의 공정성이 향상된 고강도 폴리에틸렌 섬유는 3단 연신공정으로 연신하는 것이 바람직한 것으로 1단 연신온도는 60~100℃, 2단 연신온도는 80~120℃, 3단 연신온도는 100~120℃인 것이 바람직할 것이다.It is preferable that the high-strength polyethylene fiber with improved processability of the present invention is stretched by a three-stage stretching process, wherein the stretching temperature is from 60 to 100 占 폚, the stretching temperature is from 80 to 120 占 폚 and the stretching temperature is from 100 to 120 占 폚 Lt; / RTI >
상기 2단 연신온도는 상기 1단 연신온도 보다 높은 온도에서 연신하는 것이 바람직하며, 3단 연신온도 역시 상기 2단 연신온도 보다 높은 온도에서 연신하는 것이 바람직할 것이다.Preferably, the two-step stretching temperature is higher than the first-step stretching temperature, and the third-step stretching temperature is also preferably higher than the second-step stretching temperature.
상기 1단 연신온도와 2단 연신온도 범위아래에서는 연신할 경우 섬유에 충분한 열이 공급되지 않음으로써 연신이 불균일하게 형성되어 롤러표면에서 사절발생율이 증가되고, 모우 발생 빈도가 높아질수 있으며, 1단 연신온도와 2단 연신온도범위를 넘어서는 경우에는 롤러표면에서 섬유의 용융현상이 발생되어 롤러표면사절 및 모우발생율이 높아져 섬유품질이 저하될 수 있다.Under the first stage stretching temperature and the second stage stretching temperature range, sufficient heat is not supplied to the fibers when the stretching is carried out, so that the stretching is non-uniformly formed to increase the yarn forming rate at the roller surface, If the stretching temperature and the two-stage stretching temperature range are exceeded, the melt of the fibers may occur on the surface of the rollers, resulting in an increase in the number of times the surface of the rollers is cut and the number of the rollers is increased.
상기 3단 연신은 섬유 열고정 및 섬유의 수축을 방지하기 위해 실시되는 것으로 실질적으로 연신은 1단, 2단 연신에서 실시되는 것이 바람직할 것이다.The three-step stretching is carried out in order to fix the fiber heat and to prevent the fiber from shrinking, and it is preferable that the stretching is practically carried out in the first-stage and second-stage stretching.
본 발명에 따른 고강도 폴리에틸렌 섬유 표면의 마디는 상기 분자량분포지수와 용융지수가 제어된 폴리에틸렌 수지의 사용 및 상기와 같은 연신단계로 마디가 형성되는 것으로 추정되는 것으로 1,2단 연신단계에서 마디가 형성되며, 3단 연신단계에서 형성된 마디가 고정되는 것으로 추정된다.The nodes of the surface of the high-strength polyethylene fiber according to the present invention are presumed to be formed by the use of the polyethylene resin whose molecular weight distribution index and melt index are controlled and the step of stretching as described above. And it is presumed that the nodes formed in the three-step stretching step are fixed.
상기와 같은 연신단계에서의 전체 연신비(DR)를 6 내지 10인 것이 바람직한 것으로 상기 전체 연신비(DR)가 6보다 낮으면 폴리에틸렌 섬유의 강도가 낮아지고, 10보다 높으면 연신 중 사절 발생이 심하여 폴리에틸렌 섬유의 품질이 저하될 수 있다.When the total draw ratio DR is lower than 6, the strength of the polyethylene fibers is lowered. When the total draw ratio DR is higher than 10, the filament is more likely to occur during drawing, May be deteriorated.
상기와 같이 분자량분포지수와 용융지수가 제어된 폴리에틸렌 수지의 사용 및 연신단계로 형성되는 본 발명에 따른 공정성이 향상된 고강도 폴리에틸렌 섬유는 강도가 12 내지 16g/d이고, 모노섬도는 0.5 내지 2.5이며, 가닥 수가 60 내지 400으로 우수한 물성을 가질 수 있다. As described above, the high-strength polyethylene fiber having improved processability according to the present invention formed by using and stretching the polyethylene resin whose molecular weight distribution index and melt index are controlled has a strength of 12 to 16 g / d, a mono-fineness of 0.5 to 2.5, And the number of strands is 60 to 400. [
상기 고강도 폴리올레핀 섬유는 또한 광범위한 다른 유형의 물품들에 사용될 수도 있다. The high strength polyolefin fibers may also be used in a wide variety of other types of articles.
비제한적인 예시는, 예를 들면, 냉장 유닛(예, 냉장고, 냉동고, 자동 판매기 등)을 위한 절연 물질들; 자동차 부품(예, 전면 또는 후면 시트, 헤드레스트, 암레스트, 도너 패널, 후면 선반/패키지 트레이, 스티어링 휠 및 내장 트림, 대쉬보드 등); 건축 패널 및 부품(예, 지붕, 벽 공동, 언더 플로어 등); 의류(예, 코트, 셔츠, 바지, 장갑, 앞치마, 작업복, 신발, 부츠, 모자, 양말 라이너 등); 가구 및 침구(예, 침낭, 이불 등); 유체 저장/이송 시스템(예, 액체/기체탄화수소, 액체 질소, 산소, 수소, 또는 원유의 파이프 또는 탱크); 극한 환경(예, 수중 또는 우주); 음식 및 음료 제품(예, 컵, 컵 홀더, 접시 등); 용기 및 병; 등을 포함한다. Non-limiting examples include, for example, insulating materials for refrigeration units (e.g., refrigerators, freezers, vending machines, etc.); Automotive parts (eg, front or back sheet, headrest, arm rest, donor panel, rear shelf / package tray, steering wheel and interior trim, dashboard, etc); Architectural panels and components (eg roofs, wall joints, underfloor, etc.); Clothing (eg, coat, shirt, trousers, gloves, apron, work clothes, shoes, boots, hats, sock liner etc); Furniture and bedding (eg, sleeping bags, comforters, etc.); Fluid storage / transfer systems (eg, liquid / gas hydrocarbons, liquid nitrogen, oxygen, hydrogen, or crude oil pipes or tanks); Extreme environments (eg underwater or universe); Food and beverage products (eg cups, cup holders, plates, etc.); Containers and bottles; And the like.
또한, 폴리올레핀 섬유는, 일반적으로 신체의 일부에 대하여 맞게 되는 형상을 갖는 임의의 용품을 포함하는 것을 의미하는 "의복"에 사용될 수 있다. 이러한 용품의 예는, 제한 없이, 의류(예를 들어, 셔츠, 바지, 청바지, 슬랙스, 스커트, 코트, 액티브웨어, 운동복, 에어로빅, 및 체육복, 수영복, 사이클링 저지 또는 반바지, 수영복/욕실 수트(bathing suit), 레이스 수트, 땀복, 바디수트 등); 신발류(예를 들어, 신발, 양말, 부츠 등); 보호용 의류(예를 들어, 소방관 코트), 의류 액세서리(예를 들어, 벨트, 브라 스트랩, 사이드 패널, 장갑, 양말, 레깅스, 정형외과 교정기(orthopedic brace)등), 속옷(예를 들어, 언더웨어, t-셔츠 등), 압박 옷, 걸치는 옷(예를 들어, 킬트 샅바, 토가, 판초, 망토, 숄등)을 포함한다.In addition, the polyolefin fibers can be used in "garments " which means that they include any article having a shape that is generally adapted to a portion of the body. Examples of such items include, but are not limited to, clothing (e.g., shirts, trousers, jeans, slacks, skirts, coats, activewear, sportswear, aerobics and gym clothes, swimwear, cycling jerseys or shorts, bathing suit, lace suit, sweat suit, body suit, etc.); Footwear (for example, shoes, socks, boots, etc.); (E.g., undergarment, undergarment, undergarment, undergarment, undergarment, undergarment, undergarment, t-shirts, etc.), compression garments, and hanging garments (e.g., kilt nappa, toga, poncho, cloak, shawl, etc.).
이하 본 발명에 따른 실시예로 공정성이 향상된 고강도 폴리에틸렌 섬유를 제조하였다. 본 발명이 이들 실시예에 한정되는 것은 아니다.Hereinafter, high-strength polyethylene fibers having improved processability were prepared according to the present invention. But the present invention is not limited to these examples.
실시예 1 내지 5, 비교예 1 내지 5Examples 1 to 5 and Comparative Examples 1 to 5
용융지수가 0.6 내지 2 g/10min이고, 분자량분포지수가 5 내지 10인 폴리에틸렌 수지를 압출기에 투입하여 용융 폴리머를 압출시키고, 냉각 장치를 이용하여 냉각시킨 다음, 방사유제 부여 장치를 이용하여 방사유제를 부착하고, 유제가 부착된 미연신사를 권취하였으며, 상기 미연신사를 연신 및 열처리를 행하였다. 그 이후, 교락 장치 및 와인더를 이용하여 권취하여 본 발명에 따른 공정성이 향상된 고강도 폴리에틸렌 섬유를 제조하였다.A polyethylene resin having a melt index of 0.6 to 2 g / 10 min and a molecular weight distribution index of 5 to 10 is put into an extruder to extrude the molten polymer and cooled using a cooling device, And an unstiffened yarn with an emulsion was wound thereon, and the unstretched yarn was subjected to stretching and heat treatment. Thereafter, a high strength polyethylene fiber with improved processability according to the present invention was produced by winding using an interlocking device and a winder.
상기 연신은 다단연신롤러를 사용하여 3단 연신으로 연신하였으며, 1단 연신온도는 약 70±3℃, 2단 연신온도는 약 92±3℃, 3단 연신온도는 약 105±3℃에서 연신하였다.The stretching was performed by a three-stage stretching using a multi-stage stretching roller. The stretching was carried out at a stretching temperature of about 70 占 폚, a stretching temperature of about 92 占 폚 of about 3 占 폚, and a stretching temperature of about 105 占Respectively.
각각의 실시예, 비교예에서 중량평균분자량, 분자량분포지수, 용융지수, 용융지수비, 전체 연신비(DR)은 하기 표 3,4의 조건과 같으며 그 외 방사조건은 동일하게 실시하였다. The weight average molecular weight, the molecular weight distribution index, the melt index, the melt index ratio, and the total draw ratio (DR) were the same as in Tables 3 and 4 and the other spinning conditions were the same in the respective Examples and Comparative Examples.
도 1은 실시예 1의 폴리에틸렌 섬유 SEM 사진으로 일정간격으로 마디가 형성되는 것을 알 수 있다.FIG. 1 is a SEM photograph of a polyethylene fiber of Example 1 showing that nodes are formed at regular intervals.
◈ 측정방법◈ Measurement method
상기 실시예 1 내지 5, 비교예 1 내지 5의 강도, 모우발생빈도, 내절단성 인덱스 및 레벨, 내절단력 등을 측정하였다.The strength, the occurrence frequency, the index of cut resistance, the level and the breaking strength of the examples 1 to 5 and the comparative examples 1 to 5 were measured.
상기 내절단성 인덱스 및 레벨, 내절단력은 상기 실시예 1 내지 5와 비교예 1 내지 5의 폴리에틸렌 섬유로 편물을 제조한 후 측정하였다.The index of cut resistance, level and endurance were measured after knitting with the polyethylene fibers of Examples 1 to 5 and Comparative Examples 1 to 5.
실시예들의 모우 발생 빈도, 내절단성 레벨, 내절단력은 표 3, 비교예들의 모우 발생 빈도, 내절단성 레벨, 내절단력은 표 4에 나타내었다.Table 3 shows the blade occurrence frequency, cutting resistance level and cutting strength of the examples. Table 3 shows the blade occurrence frequency, cutting strength level and cutting strength of the comparative examples.
* 용융지수 측정 : ASTM D1238dp 의거하여 측정하였으며 측정온도는 190℃이며 추 무게는 고하중용융지수는 21.6kg, 용융지수는 2.16kg으로 정의 하였으며, 측정 중 프리히팅 5분, 프리러닝 3분 진행하였으며, 10회 측정한 값을 평균값으로 정의하였다. * Measurement of melt index: Measured according to ASTM D1238dp. The measurement temperature was 190 ° C, and the weight was defined as 21.6 kg of high-load melt index and 2.16 kg of melt index. Preheating was performed for 5 minutes and free run for 3 minutes , And the value measured 10 times was defined as an average value.
* 강도 측정방법 : 만능시험기 UTM(Universal Testing Mechine, INSTRON社)을 사용하여 ASTM D-2256에 의거하여 측정하였으며 측정 온도 20℃, 상대습도 65%하에서 300mm/min의 속도로 10회 측정한 값을 강도에 대해 평균 값으로 정의하였다. * Strength measurement method: Measured according to ASTM D-2256 using a universal testing machine UTM (Universal Testing Mechine, INSTRON), and measured 10 times at a rate of 300 mm / min under a relative humidity of 65% The intensity was defined as the mean value.
강도는 만능시험기에 섬유를 파지하고 상기의 속도로 하중을 주어 인장하면 응력-변형 곡선이 나타나게 되는데, 인장하는 섬유가 절단될 때의 하중을 데니어(denier)로 나눈 값 g/d로 정의하였다. Strength is defined as the value of g / d divided by the denier, when the tensile fibers are cut, by holding the fibers in an universal testing machine and applying tensile load at the above speed to yield a stress-strain curve.
* 모우 발생 빈도(공정 안정성 평가) : 총 생산된 원사에 대하여 100,000m 당 측정되는 모우 개수에 따라 발생 빈도를 평가하였다.* Frequency of occurrence of moth (process stability evaluation): The frequency of occurrence was evaluated according to the number of moths per 100,000 m of total produced yarn.
* 내절단성 인덱스 및 레벨 : 직물 혹은 편물의 내절단성 평가 방법은 EN388 규격에 의거하여 제조된 장치인 Mesdan사 Glove cut tester를 사용했다. 측정은 러버 지지체 위에 필터페이퍼가 감싸진 알루미늄 호일을 붙이고 대조 샘플 및 테스트 샘플을 위치한 후 테스트 전 대조 샘플과 테스트 샘플을 측정하여 5회 측정하여 아래와 같이 평가하여 인덱스를 계산하였다.* Index and level of cut resistance: Mesdan Yarn cut tester, a device manufactured in accordance with EN388 standard, was used to evaluate the cut resistance of fabric or knitted fabric. The measurement was performed by placing an aluminum foil wrapped with a filter paper on a rubber support, placing the control sample and the test sample, measuring the control sample and the test sample five times before the test, and evaluating the index as follows.
<내절단성 인덱스><Cutting resistance index>
SequenceSequence CControl specimenCControl specimen TTest specimenTTest specimen CControl specimenCControl specimen IIndexIIndex
1One C1 C 1 T1 T 1 C2 C 2 i1i1
22 C2 C 2 T2 T 2 C3 C 3 i2i2
33 C3 C 3 T3 T 3 C4 C 4 i3i3
44 C4 C 4 T4 T 4 C5 C 5 i4i4
55 C5 C 5 T5 T 5 C6 C 6 i5i5
[내절단성 인덱스(I) 수식]
Figure PCTKR2018011217-appb-I000001
[Cutting resistance index (I) formula]
Figure PCTKR2018011217-appb-I000001
<내절단성 레벨><Cutting resistance level>
내절단성 indexCutting resistance index >1.2> 1.2 >2.5> 2.5 >5> 5 >10> 10 >20> 20
내절단성 LevelCutting resistance level 1One 22 33 44 55
* 내절단력(N) : 직물 혹은 편물의 내절단력 평가 방법은 ISO13997 규격에 의거하여 제조된 장치인 Satara사 STM610 모델을 사용했다. 절단은 힘의 범위가 시료 표면에 수직인 칼날에 적용될 때, 20mm의 칼날질에 재료를 자를 때 필요한 내절단력으로 측정하며 측정 순서는 시료와 칼날 사이를 일정한 힘이 점진적으로 가해지며 5초 이내에 자르기를 시작하고 5mm와 50mm 사이의 절단 길이로 적어도 15개 기록이 얻어질 때까지 다른 힘으로 시험을 반복하여 평가한다. 내절단력은 5mm에서 15mm, 15mm에서 30mm, 30mm에서 50mm 범위에서 얻어지며, 보정계수 C와 절단 길이를 곱한 값을 그래프화 하여 절단길이 20mm일 때의 힘을 내절단력으로 측정한다. * Cutting force (N): The method of evaluating the cutting force of a fabric or a knitted fabric was a model STM610 of Satara, manufactured according to the ISO13997 standard. Cutting is measured by the cutting force required when cutting the material to a blade quality of 20 mm when the range of force is applied to the blade perpendicular to the surface of the sample. The measuring sequence is a gradual application of a constant force between the sample and the blade. And repeat the test with different forces until at least 15 records with a cut length between 5 mm and 50 mm are obtained. The cutting force is obtained in the range of 5 mm to 15 mm, 15 mm to 30 mm, and 30 mm to 50 mm, and the value obtained by multiplying the correction factor C by the cutting length is plotted and the force at a cutting length of 20 mm is measured by the cutting force.
<내절단력 보정계수><Cutting Force Correction Factor>
C = K/lC = K / l
C는 보정계수, l은 5.0N 네오프렌상 절단동작길이 mm, K=20C is a correction coefficient, l is 5.0N neoprene phase cutting operation length mm, K = 20
구분division 실시예 1Example 1 실시예 2Example 2 실시예 3Example 3 실시예 4Example 4 실시예 5Example 5
중량평균분자량(g/mol)Weight average molecular weight (g / mol) 250000250000 250000250000 250000250000 110000110000 130000130000
분자량분포지수Molecular weight distribution index 7.67.6 7.87.8 7.67.6 5.85.8 7.87.8
용융지수(g/10min)The melt index (g / 10 min) 0.90.9 0.750.75 0.90.9 1.21.2 1.21.2
용융지수비(HLMI/MI)Melt index ratio (HLMI / MI) 3131 3838 3131 2626 3838
연신비(DR)Drawing Ratio (DR) 88 7.87.8 88 8.88.8 7.57.5
섬도(De)The island (De) 400400 425425 200200 390390 400400
강도(g/d)Strength (g / d) 15.215.2 15.515.5 15.115.1 15.815.8 14.314.3
모우 발생 빈도(개/10만m)Frequency of occurrence of mow (100,000 m / person) 44 88 44 88 88
내절단성 레벨Cutting resistance level 33 33 33 33 33
내절단력(N)Cutting force (N) 10.410.4 10.410.4 11.611.6 9.49.4 8.28.2
구분division 비교예 1Comparative Example 1 비교예 2Comparative Example 2 비교예 3Comparative Example 3 비교예 4Comparative Example 4 비교예 5Comparative Example 5
중량평균분자량(g/mol)Weight average molecular weight (g / mol) 250000250000 130000130000 8000080000 330000330000 330000330000
분자량분포지수Molecular weight distribution index 8.28.2 8.58.5 5.85.8 8.28.2 1010
용융지수(g/10min)The melt index (g / 10 min) 0.90.9 2.22.2 5.05.0 0.60.6 0.40.4
용융지수비(HLMI/MI)Melt index ratio (HLMI / MI) 4646 5252 3535 4343 8080
연신비(DR)Drawing Ratio (DR) 7.17.1 7.57.5 8.58.5 66 44
섬도(De)The island (De) 430430 430430 410410 260260 850850
강도(g/d)Strength (g / d) 13.213.2 12.112.1 12.212.2 14.114.1 8.58.5
모우 발생 빈도(개/10만m)Frequency of occurrence of mow (100,000 m / person) 2626 1515 1616 3232 6060
내절단성 레벨Cutting resistance level 22 22 22 22 1One
내절단력(N)Cutting force (N) 6.26.2 3.53.5 3.83.8 7.87.8 2.62.6
표 3 및 표 4에서와 같이 용융지수가 0.6 내지 2g/10min이고, 용융지수비(HLMI/MI)가 20 내지 40의 범위로 조절된 폴리에틸렌 수지로 형성된 실시예 1 내지 5는 모두 모우 발생 빈도가 10이하로 공정 안정성이 매우 우수하나, 용융지수비가 40을 초과하는 비교예 1 내지 5는 모우 발생 빈도가 15~60으로 공정 안정성이 매우 낮은 것을 알 수 있다.또한, 본 발명에 따른 실시예 1 내지 5는 강도가 비교예 1 내지 5에 비해 매우 우수하며, 내절단성 레벨 및 내절단력 역시 비교예 1 내지 5 보다 우수한 것을 알 수 있다.As shown in Tables 3 and 4, in Examples 1 to 5 formed from a polyethylene resin having a melt index of 0.6 to 2 g / 10 min and a melt index ratio (HLMI / MI) of 20 to 40, 10, the process stability is excellent. However, in Comparative Examples 1 to 5, in which the melt index ratio exceeds 40, it is found that the processability is very low due to the occurrence frequency of moths of 15 to 60. In addition, To 5 are superior in strength to those of Comparative Examples 1 to 5, and that the cutting resistance level and the cutting strength are also superior to those of Comparative Examples 1 to 5.

Claims (8)

  1. 폴리에틸렌 수지로 형성되어 주요 반복 단위가 에틸렌인 폴리에틸렌 섬유로서, 1. A polyethylene fiber which is formed of a polyethylene resin and whose main repeating unit is ethylene,
    상기 폴리에틸렌 수지는 용융지수가 0.6 내지 2g/10min이고, 용융지수비(HLMI/MI)가 20 내지 40인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유.Wherein the polyethylene resin has a melt index of 0.6 to 2 g / 10 min and a melt index ratio (HLMI / MI) of 20 to 40. The high-
  2. 제1항에 있어서, The method according to claim 1,
    상기 폴리에틸렌 섬유의 표면에 다수의 마디부가 형성되는 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유.Wherein a plurality of nodules are formed on a surface of the polyethylene fiber.
  3. 제1항에 있어서, The method according to claim 1,
    상기 폴리에틸렌 수지는 분자량 분포지수가 5 내지 10인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유.Wherein said polyethylene resin has a molecular weight distribution index of 5 to 10. &lt; Desc / Clms Page number 24 &gt;
  4. 제1항에 있어서,The method according to claim 1,
    상기 폴리에틸렌 섬유의 강도가 12 내지 16g/d인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유.Wherein the polyethylene fiber has a strength of 12 to 16 g / d.
  5. 제1항에 있어서,The method according to claim 1,
    상기 폴리에틸렌 섬유는 모우 발생이 100,000m 당 10개 이하인 것을 특징으로 하는 공정성이 향상된 고강도 폴리에틸렌 섬유.Wherein said polyethylene fibers have ten or less per 100,000 m of hair growth.
  6. 제1항 내지 제5항 중 어느 한 항의 폴리에틸렌 섬유를 포함하는 것을 특징으로하는 물품.An article comprising the polyethylene fiber of any one of claims 1 to 5.
  7. 제6항에 있어서,The method according to claim 6,
    상기 폴리에틸렌 물품은 내절단성 규격에 의한 레벨(Level)이 3 이상인 것을 특징으로 하는 물품.Characterized in that the polyethylene article has a level of 3 or more according to the cutting resistance standard.
  8. 제6항에 있어서,The method according to claim 6,
    상기 폴리에틸렌 물품은 내절단력이 4.0N 이상인 것을 특징으로 하는 물품.Wherein the polyethylene article has a breaking strength of 4.0 N or more.
PCT/KR2018/011217 2018-01-05 2018-09-21 High-strength polyethylene fiber having improved processability WO2019135466A1 (en)

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KR102178478B1 (en) * 2019-07-01 2020-11-16 주식회사 휴비스 High-strength polyethylene fiber having improved evenness, and manufacturing method thereof
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