JP6386561B2 - Nylon blend composition with improved moisture absorption rate and shrinkage rate, nylon fiber produced therefrom and method for producing the same - Google Patents

Nylon blend composition with improved moisture absorption rate and shrinkage rate, nylon fiber produced therefrom and method for producing the same Download PDF

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JP6386561B2
JP6386561B2 JP2016536797A JP2016536797A JP6386561B2 JP 6386561 B2 JP6386561 B2 JP 6386561B2 JP 2016536797 A JP2016536797 A JP 2016536797A JP 2016536797 A JP2016536797 A JP 2016536797A JP 6386561 B2 JP6386561 B2 JP 6386561B2
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ドン−フン ヒュン
ドン−フン ヒュン
ス−ジョン イ
ス−ジョン イ
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ジーエス カルテックス コーポレイション
ジーエス カルテックス コーポレイション
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/08Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
    • C08G69/14Lactams
    • C08G69/16Preparatory processes
    • C08G69/18Anionic polymerisation
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/08Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
    • C08G69/14Lactams
    • C08G69/24Pyrrolidones or piperidones
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C08L77/02Polyamides derived from omega-amino carboxylic acids or from lactams thereof
    • 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
    • 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
    • D01F6/78Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
    • D01F6/80Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyamides
    • 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
    • D01F6/88Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/90Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyamides

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  • Chemical Kinetics & Catalysis (AREA)
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  • Polymers & Plastics (AREA)
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  • Textile Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
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  • Artificial Filaments (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Polyamides (AREA)

Description

本発明は、吸湿率及び収縮率が改善されたナイロンブレンド組成物、それから製造されるナイロン系繊維及びその製造方法に関する。   The present invention relates to a nylon blend composition having improved moisture absorption and shrinkage, a nylon fiber produced therefrom, and a method for producing the same.

ナイロン6は、通常、優れた強度、弾性回復率、染色性などの特性を持っているが、ナイロン6を含むほとんどの合成繊維は吸湿率が低いという欠点がある。天然繊維であるコットンは吸湿率が高く従来の合成繊維に比べ肌触りが良好であるが、マイクロファイバーへの加工が不可能で、優れた肌触りの発現が不可能であり紫外線遮断性が非常に不足しているうえ、価格が高価であるため、これに代わる革新的なナイロン合成繊維の出現が求められてきた。   Nylon 6 usually has properties such as excellent strength, elastic recovery rate, and dyeability, but most synthetic fibers including nylon 6 have a drawback of low moisture absorption. Cotton, which is a natural fiber, has a high moisture absorption rate and feels better than conventional synthetic fibers, but it cannot be processed into microfibers, cannot produce an excellent feel, and has an extremely poor UV blocking property. In addition, since the price is expensive, the emergence of innovative nylon synthetic fibers has been demanded.

古くから合成繊維を研究する人々は、従来の合成繊維の長所をそのまま維持しながら、高い吸湿率と優れたフィット感というコットンの長所を同時に生かすことができる新合成繊維の研究を重ねてきた。そのような努力の結実の中で最も注目されてきたのは、ナイロン4(2−ピロリドン単量体が単独重合された樹脂)と言える。   Synthetic fiber researchers have long been researching new synthetic fibers that can take advantage of the advantages of cotton, such as high moisture absorption and excellent fit, while maintaining the advantages of conventional synthetic fibers. It can be said that nylon 4 (a resin in which a 2-pyrrolidone monomer is homopolymerized) has attracted the most attention as a result of such efforts.

このようなナイロン4は、構造において繰り返し単位当たりの親油性炭素数が少ないため、吸湿率が高く強度が優れているという強みにより、1973年コットンの代わりになる夢の合成繊維として登場したが、融点が265℃であるのに対し、熱分解温度が260℃で、紡糸加工耐熱性が非常に劣悪であるという技術的な問題点がある。   Nylon 4 like this appeared as a dream synthetic fiber to replace cotton in 1973 due to its strength of high moisture absorption and strength due to its low lipophilic carbon number per repeating unit in the structure, While the melting point is 265 ° C., the thermal decomposition temperature is 260 ° C., and there is a technical problem that the heat resistance of the spinning process is very poor.

このようなナイロン4とナイロン6の物性を相互補完することができるナイロンブレンド組成物の製造が求められているのが実情である。   In fact, there is a demand for production of a nylon blend composition capable of complementing the physical properties of nylon 4 and nylon 6.

本発明は、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%;及びナイロン6樹脂5重量%〜30重量%を含む吸湿率及び収縮率が改善された繊維製造用のナイロンブレンド組成物などを提供することにその目的がある。   The present invention has improved moisture absorption and shrinkage, including 70% to 95% by weight resin polymerized with 2-pyrrolidone and 5 to 7 carbon lactams; and 5% to 30% by weight nylon 6 resin. The object is to provide a nylon blend composition or the like for fiber production.

しかし、本発明が解決しようとする技術的課題は、以上で言及した課題に制限されず、言及されていない他の課題は、以下の記載から当業者に明確に理解されるだろう。   However, the technical problems to be solved by the present invention are not limited to the problems mentioned above, and other problems not mentioned will be clearly understood by those skilled in the art from the following description.

本発明は、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%;及びナイロン6樹脂5重量%〜30重量%を含む吸湿率及び収縮率が改善された繊維製造用のナイロンブレンド組成物を提供する。   The present invention has improved moisture absorption and shrinkage, including 70% to 95% by weight resin polymerized with 2-pyrrolidone and 5 to 7 carbon lactams; and 5% to 30% by weight nylon 6 resin. A nylon blend composition for fiber manufacture is provided.

前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂は、ナイロン4,6樹脂とすることができる。   The resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms may be a nylon 4,6 resin.

前記2−ピロリドンまたは前記炭素数5〜7のラクタムは、バイオマスから得られるものとすることができる。   The 2-pyrrolidone or the lactam having 5 to 7 carbon atoms can be obtained from biomass.

前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂の重量平均分子量が50kg/mol〜200kg/molであることができる。   The resin obtained by polymerizing the 2-pyrrolidone and the lactam having 5 to 7 carbon atoms may have a weight average molecular weight of 50 kg / mol to 200 kg / mol.

本発明の一実施例として、前記ナイロンブレンド組成物から製造される吸湿率及び収縮率が改善されたナイロン系繊維を提供する。   As an embodiment of the present invention, there is provided a nylon-based fiber with improved moisture absorption and shrinkage, which is produced from the nylon blend composition.

前記ナイロン系繊維の吸湿率が5%〜10%であることができる。   The nylon fiber may have a moisture absorption rate of 5% to 10%.

前記ナイロン系繊維の収縮率が10%〜40%であることができる。   The shrinkage ratio of the nylon fiber may be 10% to 40%.

前記ナイロン系繊維の強度が3g/d〜5g/dであることができる。   The nylon fiber may have a strength of 3 g / d to 5 g / d.

本発明の一実施例で、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%、及びナイロン6樹脂5重量%〜30重量%を溶融ブレンドした後、紡糸して製造されることを特徴とする吸湿率及び収縮率が改善されたナイロンブレンド組成物の製造方法を提供する。   In one embodiment of the present invention, 70 wt.% To 95 wt.% Of a resin polymerized with 2-pyrrolidone and 5 to 7 carbon lactam, and 5 wt. And a method for producing a nylon blend composition with improved moisture absorption and shrinkage.

前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂は、ナイロン4,6樹脂とすることができる。   The resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms may be a nylon 4,6 resin.

前記溶融ブレンドは230℃〜270℃で行うことができる。   The melt blending can be performed at 230 ° C to 270 ° C.

前記紡糸段階は、140℃〜180℃で熱固定の過程を経ることができる。   The spinning step may be performed through a heat setting process at 140 ° C to 180 ° C.

本発明に係るナイロンブレンド組成物は、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%;及びナイロン6樹脂5重量%〜30重量%を含むことにより、紡糸加工性に優れ、高吸湿率を維持しながらも、低収縮率及び高強度の特性を有し、繊維の断面が均一な特性を示すものであって、産業用および衣料用製品を製造するための後加工時の収縮不均一現象がなく、形態の安定性に優れて、産業用および衣料用繊維材料として非常に有用であることが確認できた。   The nylon blend composition according to the present invention comprises 70% to 95% by weight of a resin polymerized with 2-pyrrolidone and a lactam having 5 to 7 carbon atoms; and 5% to 30% by weight of a nylon 6 resin. Produces industrial and apparel products with excellent spinning processability, high moisture absorption, low shrinkage and high strength, and uniform fiber cross-section. Therefore, it was confirmed that there was no shrinkage non-uniformity phenomenon during post-processing, excellent shape stability, and very useful as a fiber material for industrial and clothing.

図1は、本発明の一実施例により製造された繊維の断面を光学顕微鏡で測定したものである。FIG. 1 is a cross-sectional view of a fiber manufactured according to an embodiment of the present invention, measured with an optical microscope.

本発明者らは、ナイロンブレンド組成物について研究していた中、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂及びナイロン6樹脂を一定の重量比で溶融ブレンドすることにより、紡糸加工性、吸湿率及び収縮率、強度など繊維物性に優れたナイロンブレンド組成物を製造することができることを確認して、本発明を完成した。   While the inventors of the present invention have been studying a nylon blend composition, spinning is performed by melt-blending a resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms and a nylon 6 resin at a constant weight ratio. It was confirmed that a nylon blend composition excellent in fiber properties such as processability, moisture absorption and shrinkage, and strength could be produced, and the present invention was completed.

以下に本発明を詳細に説明する。   The present invention is described in detail below.

本発明は、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%;及びナイロン6樹脂5重量%〜30重量%を含む吸湿率及び収縮率が改善されたナイロンブレンド組成物を提供する。   The present invention has improved moisture absorption and shrinkage, including 70% to 95% by weight resin polymerized with 2-pyrrolidone and 5 to 7 carbon lactams; and 5% to 30% by weight nylon 6 resin. A nylon blend composition is provided.

前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂において、炭素数5〜7のラクタムとしては、ピペリドン(piperidone)、カプロラクタム(caprolactam)、エナントールラクタム(enantholactam)などが挙げられるが、これらに限定されず、好ましくは、ε−カプロラクタムを使用することができる。   In the resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms, examples of the lactam having 5 to 7 carbon atoms include piperidone, caprolactam, enantholactam and the like. However, it is not limited thereto, and preferably ε-caprolactam can be used.

前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂は、ナイロン4,6樹脂とすることができ、ナイロン4,6樹脂は、炭素数5〜7のラクタムとしてε−カプロラクタムを使用して製造され、ナイロン4(2−ピロリドン単量体が単独重合された樹脂)の劣悪な紡糸加工性及び耐熱性を改善して製造したものである。   The resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms may be a nylon 4,6 resin, and the nylon 4,6 resin uses ε-caprolactam as a lactam having 5 to 7 carbon atoms. Nylon 4 (resin in which 2-pyrrolidone monomer is homopolymerized) is manufactured with improved poor spinning processability and heat resistance.

例えば、本発明に係る2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂は、2−ピロリドンおよび炭素数5〜7のラクタムを含む単量体をアニオン重合してナイロン4,6共重合体を製造した後、前記ナイロン4,6共重合体内の未反応単量体および触媒を水で精製し、前記精製された水のイオン交換を通じてpHを制御し、前記pH制御された水を濃縮して前記未反応単量体を回収することにより製造することができる。   For example, a resin in which 2-pyrrolidone and a lactam having 5 to 7 carbon atoms according to the present invention are polymerized is obtained by anionic polymerization of a monomer containing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms to co-polymerize nylon 4 and 6. After producing the polymer, the unreacted monomer and catalyst in the nylon 4,6 copolymer are purified with water, the pH is controlled through ion exchange of the purified water, and the pH-controlled water is removed. It can manufacture by concentrating and collect | recovering the said unreacted monomers.

前記ナイロン6樹脂は、炭素数6つのε−カプロラクタムが重合された樹脂を言い、(C10CONH)の化学構造を有する。 The nylon 6 resin is a resin in which ε-caprolactam having 6 carbon atoms is polymerized, and has a chemical structure of (C 5 H 10 CONH) n .

本発明に係る2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂(例えば、ナイロン4,6樹脂)とナイロン6樹脂は、別途の反応性相溶化剤(compatibilizing agent)がなくても、相互間の混練性に優れた特徴がある。すなわち、前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂と、前記ナイロン6樹脂を含むナイロンブレンド組成物は、単一溶融温度(Tm)及び単一結晶化温度(Tc)を有する。   The resin in which 2-pyrrolidone and a lactam having 5 to 7 carbon atoms according to the present invention are polymerized (for example, nylon 4,6 resin) and nylon 6 resin are not required to have a separate reactive compatibilizing agent. , It has a characteristic of excellent kneadability between each other. That is, the resin blended with 2-pyrrolidone and a lactam having 5 to 7 carbon atoms and the nylon blend composition including the nylon 6 resin have a single melting temperature (Tm) and a single crystallization temperature (Tc). Have.

すなわち、本発明に係るナイロンブレンド組成物は、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%;及びナイロン6樹脂5重量%〜30重量%を含むことが好ましいが、これに限定されない。この時、ピロリドン及び炭素数5〜7のラクタムが重合された樹脂の重量比が上記の範囲未満である場合には吸湿率が低下する問題があり、ピロリドン及び炭素数5〜7のラクタムが重合された樹脂の重量比が上記の範囲を超える場合には、紡糸安定性が落ちて紡糸条件を設定するのに困難があり、収縮率が高くなり、強度が落ちる問題がある。   That is, the nylon blend composition according to the present invention includes 70% to 95% by weight of resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms; and 5% to 30% by weight of nylon 6 resin. However, it is not limited to this. At this time, if the weight ratio of the resin in which pyrrolidone and a lactam having 5 to 7 carbon atoms are polymerized is less than the above range, there is a problem that the moisture absorption rate is lowered, and the pyrrolidone and the lactam having 5 to 7 carbon atoms are polymerized. When the weight ratio of the resin is more than the above range, there is a problem that spinning stability is lowered and it is difficult to set spinning conditions, the shrinkage ratio is increased, and the strength is lowered.

前記2−ピロリドンまたは前記炭素数5〜7のラクタムは、バイオマスから得られるものとすることができる。   The 2-pyrrolidone or the lactam having 5 to 7 carbon atoms can be obtained from biomass.

具体的には、前記2−ピロリドンは微生物発酵によって生産されたグルタミン酸またはグルタミン酸ナトリウムを出発物質とし、グルタミン酸デカルボキシラーゼ(GAD)を触媒として用いて4−アミノ酪酸を製造した後、そこから触媒または脱水剤を用いて2−ピロリドンを得ることができる。   Specifically, the 2-pyrrolidone is produced by producing 4-aminobutyric acid using glutamic acid or sodium glutamate produced by microbial fermentation as a starting material and using glutamic acid decarboxylase (GAD) as a catalyst, and then catalyst or dehydration therefrom. 2-pyrrolidone can be obtained using an agent.

前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂の重量平均分子量が50kg/mol〜200kg/molであることができる。この時、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂の重量平均分子量が50kg/mol未満の場合、繊維製品の機械的物性が低下する問題があり、ナイロン4,6樹脂の重量平均分子量が200kg/molを超える場合、繊維紡糸時の粘度が高く流動性が悪いという問題がある。   The resin obtained by polymerizing the 2-pyrrolidone and the lactam having 5 to 7 carbon atoms may have a weight average molecular weight of 50 kg / mol to 200 kg / mol. At this time, when the weight average molecular weight of the resin in which 2-pyrrolidone and a lactam having 5 to 7 carbon atoms are polymerized is less than 50 kg / mol, there is a problem that the mechanical properties of the fiber product are deteriorated. When the weight average molecular weight exceeds 200 kg / mol, there is a problem that the viscosity during fiber spinning is high and the fluidity is poor.

前記ナイロンブレンド組成物は、必要に応じて様々な安定化剤、滑剤、離型剤、顔料、染料、難燃剤、強化剤、酸化防止剤、帯電防止剤、導電性添加剤、EMI遮蔽剤、結晶核剤、抗菌剤、消臭剤や潤滑剤などからなる群から選択された1種以上を物性、外観、成形性に影響を与えない範囲内でさらに含むことができる。   The nylon blend composition includes various stabilizers, lubricants, mold release agents, pigments, dyes, flame retardants, reinforcing agents, antioxidants, antistatic agents, conductive additives, EMI shielding agents, as required. One or more selected from the group consisting of crystal nucleating agents, antibacterial agents, deodorants, lubricants, and the like can be further included within a range that does not affect physical properties, appearance, and moldability.

また、本発明は、前記ナイロンブレンド組成物から製造される吸湿率及び収縮率が改善されたナイロン系繊維を提供する。   The present invention also provides a nylon fiber with improved moisture absorption and shrinkage produced from the nylon blend composition.

前記ナイロン系繊維の吸湿率が5%〜10%であることができる。   The nylon fiber may have a moisture absorption rate of 5% to 10%.

前記ナイロン系繊維の収縮率が10%〜40%であることができる。   The shrinkage ratio of the nylon fiber may be 10% to 40%.

前記ナイロン系繊維の強度が3g/dから5g/dであることができる。   The nylon fiber may have a strength of 3 g / d to 5 g / d.

つまり、本発明に係るナイロンブレンド組成物から製造されるナイロン系繊維は、紡糸加工性に優れ、高吸湿率を維持しながらも、低収縮率及び高強度の特性を有し、繊維の断面が均一な特性を示すものであって、産業用および衣料用製品を製造するための後加工時の不均一現象がなく、形態の安定性に優れ、産業用および衣料用繊維材料として非常に有用である。   That is, the nylon fiber produced from the nylon blend composition according to the present invention is excellent in spinning processability, maintains a high moisture absorption rate, and has a low shrinkage rate and a high strength property, and the fiber cross section is low. It exhibits uniform characteristics, has no unevenness during post-processing to produce industrial and garment products, has excellent form stability, and is very useful as a textile material for industrial and garment applications. is there.

また、本発明は、2−ピロリドンおよび炭素数5〜7のラクタムが重合された樹脂70重量%〜95重量%;及びナイロン6樹脂5重量%〜30重量%を溶融ブレンドした後、紡糸して製造されることを特徴とする吸湿性及び紡糸加工性に優れながら、収縮率が改善されたナイロン系繊維の製造方法を提供する。前記2−ピロリドン及び炭素数5〜7のラクタムが重合された樹脂としては、炭素数5〜7のラクタムとしてε−カプロラクタムを使用したナイロン4,6樹脂が挙げられる。   In the present invention, 70 wt% to 95 wt% of a resin in which 2-pyrrolidone and a lactam having 5 to 7 carbon atoms are polymerized; and 5 wt% to 30 wt% of nylon 6 resin are melt-blended and then spun. Provided is a method for producing a nylon fiber having an improved shrinkage rate while being excellent in hygroscopicity and spinning processability. Examples of the resin obtained by polymerizing 2-pyrrolidone and a lactam having 5 to 7 carbon atoms include nylon 4,6 resin using ε-caprolactam as a lactam having 5 to 7 carbon atoms.

前記溶融ブレンドは230℃〜270℃で行われることができる。この時、溶融ブレンドは230℃〜270℃で行われることにより、前記ナイロン4,6樹脂とナイロン6樹脂を混練性に優れるように安定していて効果的にブレンドすることができる利点がある。   The melt blending may be performed at 230 ° C to 270 ° C. At this time, the melt blending is performed at 230 ° C. to 270 ° C., so that the nylon 4, 6 resin and the nylon 6 resin are stable and effectively blended so as to be excellent in kneadability.

前記紡糸段階は、140℃〜180℃で熱固定の過程を経ることが、製造されるナイロン系繊維の収縮率を向上させるために好ましいが、これに限定されない。   In the spinning step, it is preferable to go through a heat setting process at 140 ° C. to 180 ° C. in order to improve the shrinkage rate of the manufactured nylon fiber, but is not limited thereto.

以下、本発明の理解を助けるために好ましい実施例を提示する。しかし、下記の実施例は、本発明をより容易に理解するために提供されるものであるだけで、下記の実施例により本発明の内容が限定されるのではない。   Hereinafter, preferred examples will be presented to help understanding of the present invention. However, the following examples are provided only for easier understanding of the present invention, and the contents of the present invention are not limited by the following examples.

[実施例]
実施例1
[Example]
Example 1

(1)2−ピロリドン及びε−カプロラクタムが重合された樹脂(ナイロン4,6樹脂)の製造   (1) Production of resin (nylon 4, 6 resin) in which 2-pyrrolidone and ε-caprolactam are polymerized

単量体として2−ピロリドン25.5gとε−カプロラクタム79.1g、アルカリ性触媒として水酸化カリウム(KOH)8.4g、CO開始剤1.76g及びイソシアネート系化合物として1,6‐ヘキサメチレンジイソシアネート(1,6−hexamethylene diisocyanate)0.32gを添加してアニオン重合してナイロン4,6共重合体を製造した。ナイロン4,6共重合体内の未反応単量体として2−ピロリドンとε−カプロラクタム及びアルカリ性触媒として水酸化カリウム(KOH)を水で精製した。精製された水のイオン交換を通じてKを除去してpHを制御した。pH制御された水を逆浸透膜および蒸留によって濃縮して未反応単量体として2−ピロリドンとε−カプロラクタムを回収することにより、ナイロン4,6樹脂(Mw=140kg/mol)を最終製造した。 25.5 g 2-pyrrolidone and 79.1 g ε-caprolactam as monomers, 8.4 g potassium hydroxide (KOH) as an alkaline catalyst, 1.76 g CO 2 initiator and 1,6-hexamethylene diisocyanate as an isocyanate compound Nylon 4,6 copolymer was manufactured by adding 0.32 g of (1,6-hexaethylene diisocynate) and anionic polymerization. 2-Pyrrolidone and ε-caprolactam as unreacted monomers in the nylon 4,6 copolymer and potassium hydroxide (KOH) as an alkaline catalyst were purified with water. The pH was controlled by removing K + through ion exchange of purified water. Nylon 4,6 resin (Mw = 140 kg / mol) was finally produced by concentrating the pH-controlled water by reverse osmosis membrane and distillation to recover 2-pyrrolidone and ε-caprolactam as unreacted monomers. .

(2)ナイロンブレンド組成物の製造   (2) Production of nylon blend composition

上記(1)で製造したナイロン4,6樹脂4.75kgとナイロン6樹脂(KN−138/Kolon)0.25kgを混合し、これを235℃で溶融ブレンドしてナイロンブレンド組成物を製造した。ナイロンブレンド組成物を紡糸圧100kgf、延伸比1.15、熱固定温度175℃の条件下で36ホール(hole)紡糸機で紡糸加工して繊維原糸を最終製造した。   4.75 kg of nylon 4,6 resin produced in the above (1) and 0.25 kg of nylon 6 resin (KN-138 / Kolon) were mixed and melt blended at 235 ° C. to produce a nylon blend composition. The nylon blend composition was spun with a 36-hole spinning machine under the conditions of a spinning pressure of 100 kgf, a draw ratio of 1.15, and a heat setting temperature of 175 ° C. to finally produce a fiber yarn.

製造された繊維の断面を光学顕微鏡で測定した結果を図1に示した。その結果、繊維の断面が均一に形成されたことが確認された。   The result of measuring the cross section of the produced fiber with an optical microscope is shown in FIG. As a result, it was confirmed that the cross section of the fiber was formed uniformly.

実施例2   Example 2

ナイロン4,6樹脂4kgとナイロン6樹脂1kgとを混合したことを除いては、実施例1と同様にした。   Example 1 was repeated except that 4 kg of nylon 4,6 resin and 1 kg of nylon 6 resin were mixed.

実施例3   Example 3

ナイロン4,6樹脂3.5kgとナイロン6樹脂1.5kgとを混合したことを除いては、実施例1と同様にした。   The same procedure as in Example 1 was performed except that 3.5 kg of nylon 4,6 resin and 1.5 kg of nylon 6 resin were mixed.

実施例4   Example 4

ナイロン4,6樹脂4kgとナイロン6樹脂1kgとを混合し、熱固定温度160℃の条件下で実施したことを除いては、実施例1と同様に実施した。   The same procedure as in Example 1 was conducted except that 4 kg of nylon 4,6 resin and 1 kg of nylon 6 resin were mixed and the test was carried out at a heat setting temperature of 160 ° C.

比較例1   Comparative Example 1

実施例1の(1)で製造したナイロン4,6樹脂5kgを単独で使用し、熱固定温度160℃の条件下で実施した。   5 kg of the nylon 4,6 resin produced in (1) of Example 1 was used alone, and was carried out under the condition of a heat setting temperature of 160 ° C.

比較例2   Comparative Example 2

ナイロン6樹脂(KN−138/Kolon)5kgを単独で使用したことを除いては、実施例1と同様に実施した。     The same operation as in Example 1 was conducted except that 5 kg of nylon 6 resin (KN-138 / Kolon) was used alone.

実験例   Experimental example

1.吸湿率測定   1. Moisture absorption measurement

実施例1〜4のナイロンブレンド組成物及び比較例1〜2によるナイロン樹脂を紡糸加工した繊維の吸湿率を測定したく、繊維10gずつをそれぞれ用意して、105℃のオーブンに35分間入れておく。オーブンから取り出した後、乾燥した繊維の重量を量って以下の式を使用して吸湿率を計算した。   In order to measure the moisture absorption rate of the fibers obtained by spinning the nylon blend compositions of Examples 1 to 4 and Comparative Examples 1 and 2, 10 g of each fiber was prepared and placed in an oven at 105 ° C. for 35 minutes. deep. After removal from the oven, the dried fibers were weighed and the moisture absorption was calculated using the following formula:

吸湿率(Moisture Regain)(%)=(繊維の重量−乾燥した繊維の重量)/乾燥した繊維の重量×100   Moisture Retention (%) = (weight of fiber−weight of dried fiber) / weight of dried fiber × 100

2.沸水収縮率測定   2. Boiling water shrinkage measurement

実施例1〜4のナイロンブレンド組成物及び比較例1〜2によるナイロン樹脂を紡糸加工した繊維の沸水収縮率を測定したく、原糸をそれぞれ約1m程度採取して両端を結んで50cmの長さになるようにし、一定の初荷重(原糸の太さの0.1%)を付与した後、恒温恒湿で24時間保管した。この時の原糸の長さを収縮前原糸の長さと定義し、初荷重を維持したまま、沸水(90〜95℃)で30分浸した後、水気を拭き取って恒温恒湿で24時間保管した後、原糸の長さを測定して収縮後の原糸の長さと定義した。   In order to measure the boiling water shrinkage of the nylon blend composition of Examples 1 to 4 and the nylon resin spun by Comparative Examples 1 and 2, about 1 m of each raw yarn was sampled, and both ends were tied to a length of 50 cm. Then, after applying a certain initial load (0.1% of the thickness of the raw yarn), it was stored at constant temperature and humidity for 24 hours. The length of the raw yarn at this time is defined as the length of the original yarn before shrinkage. After maintaining the initial load, soaked in boiling water (90-95 ° C) for 30 minutes, wiped off moisture and stored at constant temperature and humidity for 24 hours. Then, the length of the raw yarn was measured and defined as the length of the original yarn after shrinkage.

以下の式を使用して沸水収縮率を計算した。   The boiling water shrinkage was calculated using the following formula:

沸水収縮率(%)=(収縮前の原糸の長さ−収縮後の原糸の長さ)/収縮前の原糸の長さ×100   Boiling water shrinkage rate (%) = (length of raw yarn before shrinkage−length of raw yarn after shrinkage) / length of raw yarn before shrinkage × 100

3.強度測定   3. Strength measurement

実施例1〜4のナイロンブレンド組成物及び比較例1〜2によるナイロン樹脂を紡糸加工した繊維の強度を測定したく、繊維を捻れ数及びその他の原形変化が生じないように採取して(100mm)、繊維を引張強度試験機(Universal tensile test machine(Instron社))のクランプに固定し、引張速度200mm/minの十分な力を加えて切断させて引張強度を測定した。   In order to measure the strength of the fibers obtained by spinning the nylon blend compositions of Examples 1 to 4 and the nylon resins according to Comparative Examples 1 and 2, the fibers were collected so that the number of twists and other original changes did not occur (100 mm ), The fiber was fixed to a clamp of a tensile strength tester (Universal tensile test machine (Instron)), and the tensile strength was measured by applying a sufficient force at a tensile speed of 200 mm / min.

上記のような吸湿率、収縮率及び強度の測定結果を下記の表1にまとめて記載した。   The measurement results of the moisture absorption rate, shrinkage rate, and strength as described above are summarized in Table 1 below.

上記の表1に示すように、実施例1〜4によるナイロンブレンド組成物から製造された繊維は、5.0%〜7.4%の吸湿率を持つため、高吸湿率を維持していることが確認できた。また、上記の表1に示すように、実施例1〜4によるナイロンブレンド組成物から製造された繊維は、14%〜35%の収縮率を持つため、低収縮率の特性を有することが確認できた。また、上記の表1に示すように、実施例1〜4によるナイロンブレンド組成物から製造された繊維は、3.5g/dから4.11g/dの強度を持つため、高強度の特性を有することが確認できた。   As shown in Table 1 above, the fibers produced from the nylon blend compositions according to Examples 1 to 4 have a moisture absorption rate of 5.0% to 7.4%, and thus maintain a high moisture absorption rate. I was able to confirm. In addition, as shown in Table 1 above, the fibers manufactured from the nylon blend compositions according to Examples 1 to 4 have a shrinkage ratio of 14% to 35%, and thus have low shrinkage characteristics. did it. In addition, as shown in Table 1 above, the fibers manufactured from the nylon blend compositions according to Examples 1 to 4 have a strength of 3.5 g / d to 4.11 g / d, and thus have high strength characteristics. It was confirmed that it had.

それに対して、比較例1によるナイロン4,6樹脂から製造された繊維は、45%の高収縮率を持つため、低収縮率の特性が低下を確認することができ、比較例2によるナイロン6樹脂から製造された繊維は4.5%の低吸湿率を持つため、高吸湿率を維持しないことが確認できた。   On the other hand, since the fiber manufactured from the nylon 4,6 resin according to Comparative Example 1 has a high shrinkage rate of 45%, it can be confirmed that the characteristic of the low shrinkage rate is lowered. Since the fiber manufactured from the resin has a low moisture absorption of 4.5%, it was confirmed that the high moisture absorption was not maintained.

したがって、本発明に係るナイロンブレンド組成物から製造された繊維は、紡糸加工性に優れ、高吸湿率を維持しながらも、低収縮率及び高強度特性を有し、繊維の断面が均一な特性を示すものであって、産業用および衣料用製品の製造のための後加工時の収縮不均一現象がなく、形態安定性に優れ、産業用および衣料用繊維材料として非常に有用である。   Therefore, the fiber manufactured from the nylon blend composition according to the present invention has excellent spinning processability, maintains a high moisture absorption rate, has a low shrinkage rate and a high strength property, and has a uniform cross section of the fiber. In other words, there is no shrinkage non-uniformity phenomenon during post-processing for the production of industrial and clothing products, it is excellent in form stability, and is very useful as a fiber material for industrial and clothing.

前述した本発明の説明は例示のためであり、本発明の属する技術の分野における通常の知識を有する者にとって、本発明の技術的思想や必須的特徴を変更しない範囲内で他の具体的な形態に容易に変形可能であることが理解できるだろう。そのため、前述した実施例は全ての面で例示的なものであり、限定されないものと理解されるべきである。   The above description of the present invention is given for illustrative purposes only, and for those who have ordinary knowledge in the technical field to which the present invention pertains, other specific details can be used without departing from the technical idea and essential features of the present invention. It will be appreciated that the form can be easily transformed. Therefore, it should be understood that the above-described embodiments are illustrative in all aspects and are not limited.

Claims (12)

2−ピロリドンおよび炭素数5〜7のラクタムがアルカリ触媒下でCO 開始剤およびイソシアネート系化合物を添加することによりアニオン重合された樹脂70重量%〜95重量%;および
ナイロン6樹脂5重量%〜30重量%を含む
吸湿率および収縮率が改善された繊維製造用のナイロンブレンド組成物。
2-pyrrolidone and 5- to 7-carbon lactam anionically polymerized by adding a CO 2 initiator and an isocyanate compound under an alkali catalyst ; and 70% to 95% by weight of nylon 6 resin; A nylon blend composition for producing fibers having improved moisture absorption and shrinkage, comprising 30% by weight.
前記2−ピロリドンおよび炭素数5〜7のラクタムがアルカリ触媒下でCO 開始剤およびイソシアネート系化合物を添加することによりアニオン重合された樹脂は、ナイロン4,6樹脂である請求項1に記載の吸湿率および収縮率が改善された繊維製造用のナイロンブレンド組成物。 The resin obtained by anionic polymerization of the 2-pyrrolidone and the lactam having 5 to 7 carbon atoms by adding a CO 2 initiator and an isocyanate compound under an alkali catalyst is a nylon 4,6 resin. A nylon blend composition for producing fibers with improved moisture absorption and shrinkage. 前記2−ピロリドンまたは前記炭素数5〜7のラクタムは、バイオマスから得られるものである請求項1または請求項2に記載の吸湿率および収縮率が改善された繊維製造用のナイロンブレンド組成物。 The nylon blend composition for fiber production with improved moisture absorption rate and shrinkage rate according to claim 1 or 2, wherein the 2-pyrrolidone or the lactam having 5 to 7 carbon atoms is obtained from biomass. 前記2−ピロリドンおよび炭素数5〜7のラクタムがアルカリ触媒下でCO 開始剤およびイソシアネート系化合物を添加することによりアニオン重合された樹脂の重量平均分子量が50 kg/mol〜200 kg/molである請求項1〜3のいずれか一項に記載の吸湿率および収縮率が改善された繊維製造用のナイロンブレンド組成物。 When the 2-pyrrolidone and the lactam having 5 to 7 carbon atoms are anionically polymerized by adding a CO 2 initiator and an isocyanate compound under an alkali catalyst, the weight average molecular weight is 50 kg / mol to 200 kg / mol. The nylon blend composition for fiber manufacture with improved moisture absorption rate and shrinkage rate according to any one of claims 1 to 3 . 請求項1〜4のいずれか一項に記載のナイロンブレンド組成物から製造される吸湿率および収縮率が改善されたナイロン系繊維。 A nylon-based fiber with improved moisture absorption and shrinkage produced from the nylon blend composition according to any one of claims 1 to 4 . 前記ナイロン系繊維の吸湿率が5%〜10%である請求項5に記載の吸湿率および収縮率が改善されたナイロン系繊維。 Nylon fiber moisture absorption and shrinkage is improved according to claim 5 moisture absorption of the nylon fibers is 5% to 10%. 前記ナイロン系繊維の収縮率が10%〜40%である請求項5に記載の吸湿率および収縮率が改善されたナイロン系繊維。 The nylon fiber having improved moisture absorption and shrinkage rate according to claim 5, wherein the shrinkage rate of the nylon fiber is 10% to 40%. 前記ナイロン系繊維の強度が3g/d〜5g/dである請求項5に記載の吸湿率および収縮率が改善されたナイロン系繊維。 6. The nylon fiber with improved moisture absorption and shrinkage rate according to claim 5, wherein the nylon fiber has a strength of 3 g / d to 5 g / d. 2−ピロリドンおよび炭素数5〜7のラクタムがアルカリ触媒下でCO 開始剤およびイソシアネート系化合物を添加することによりアニオン重合された樹脂70重量%〜95重量%、およびナイロン6樹脂5重量%〜30重量%を溶融ブレンドした後、紡糸して製造されることを特徴とする
吸湿率および収縮率が改善されたナイロン系繊維の製造方法。
2-pyrrolidone and a lactam having 5 to 7 carbon atoms are anionically polymerized by adding a CO 2 initiator and an isocyanate compound under an alkali catalyst , and 70% to 95% by weight of a nylon 6 resin and 5% by weight of a nylon 6 resin A method for producing a nylon-based fiber with improved moisture absorption and shrinkage, wherein 30% by weight is melt blended and then spun.
前記2−ピロリドンおよび炭素数5〜7のラクタムがアルカリ触媒下でCO 開始剤およびイソシアネート系化合物を添加することによりアニオン重合された樹脂は、ナイロン4、6樹脂であることを特徴とする請求項9に記載の吸湿率および収縮率が改善されたナイロン系繊維の製造方法。 The resin obtained by anionic polymerization of the 2-pyrrolidone and the lactam having 5 to 7 carbon atoms by adding a CO 2 initiator and an isocyanate compound under an alkali catalyst is a nylon 4 or 6 resin. Item 10. A method for producing a nylon fiber with improved moisture absorption rate and shrinkage rate according to Item 9. 前記溶融ブレンドは230℃〜270℃で行われる、請求項9または請求項10に記載の吸湿率および収縮率が改善されたナイロン系繊維の製造方法。 The method for producing a nylon fiber with improved moisture absorption and shrinkage rate according to claim 9 or 10, wherein the melt blending is performed at 230 ° C to 270 ° C. 前記紡糸段階は、140℃〜180℃で熱固定の過程を経ることを特徴とする請求項9〜11のいずれか一項に記載の吸湿率および収縮率が改善されたナイロン系繊維の製造方法。 The method for producing a nylon fiber with improved moisture absorption rate and shrinkage rate according to any one of claims 9 to 11, wherein the spinning step undergoes a heat setting process at 140 ° C to 180 ° C. .
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