KR101396107B1 - Polyurethaneurea elastic fiber with improved heat setting property and manufacturing method thereof - Google Patents

Polyurethaneurea elastic fiber with improved heat setting property and manufacturing method thereof Download PDF

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KR101396107B1
KR101396107B1 KR1020120119886A KR20120119886A KR101396107B1 KR 101396107 B1 KR101396107 B1 KR 101396107B1 KR 1020120119886 A KR1020120119886 A KR 1020120119886A KR 20120119886 A KR20120119886 A KR 20120119886A KR 101396107 B1 KR101396107 B1 KR 101396107B1
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mol
polyurethane
elastic yarn
chain
butylamine
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KR1020120119886A
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KR20140053666A (en
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이재명
진중성
강연수
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주식회사 효성
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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
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/70Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes
    • 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
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • 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
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/83Chemically modified polymers
    • C08G18/833Chemically modified polymers by nitrogen containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L75/00Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
    • C08L75/04Polyurethanes
    • 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
    • D01D5/04Dry spinning methods
    • 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
    • D01D5/06Wet spinning methods
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2331/00Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products
    • D10B2331/10Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyurethanes
    • 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
    • D10B2401/061Load-responsive characteristics elastic

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Textile Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Artificial Filaments (AREA)

Abstract

본 발명은, 폴리(테트라메틸렌 에테르)글리콜; 방향족, 지방족 및 지환족 디이소시아네이트 중에서 선택된 1종 또는 2종 이상의 유기 디이소시아네이트; 쇄연장제; 및 n-부틸아민을 포함하는 쇄종지제; 를 포함하는 열세트성이 향상된 폴리우레탄우레아 탄성사를 제공한다.The present invention relates to poly (tetramethylene ether) glycol; One or more organic diisocyanates selected from aromatic, aliphatic and alicyclic diisocyanates; Chain extenders; And n-butylamine; To provide a polyurethane urea elastic yarn with improved heat set properties.

Description

열세트성이 향상된 폴리우레탄우레아 탄성사 및 그 제조 방법{POLYURETHANEUREA ELASTIC FIBER WITH IMPROVED HEAT SETTING PROPERTY AND MANUFACTURING METHOD THEREOF}TECHNICAL FIELD [0001] The present invention relates to a polyurethane-urea elastic yarn having improved heat set properties, and a method for producing the same.

본 발명은 열세트성이 우수한 폴리우레탄우레아 탄성사의 제조 방법에 관한 것으로, 더욱 상세하게는 쇄종지제로 부틸아민을 사용하여, 열에 민감한 상대사의 열적 취하가 발생하는 문제를 개선할 수 있고, 물성 경시에 따른 변화를 최소화 할 수 있는 열세트성이 향상된 폴리우레탄우레아 탄성사 및 그 제조 방법에 관한 것이다.
The present invention relates to a process for producing a polyurethane-urea elastic yarn excellent in heat setting property, and more particularly, to a process for producing a polyurethaneurea elastic yarn excellent in heat setting property by using butylamine as a chain endbearing agent, To a polyurethane-urea elastic yarn having improved heat setting properties and a method for producing the same.

일반적으로, 폴리우레탄우레아는 폴리올과 과량의 디이소시아네이트 화합물을 반응시켜 예비 중합체(prepolymer)를 얻고, 이 예비 중합체에 적절한 반응을 통해 폴리우레탄우레아 섬유의 방사원액을 만든 후 방사시켜 탄성사를 얻는다.Generally, a polyurethane urea is obtained by reacting a polyol with an excess of a diisocyanate compound to obtain a prepolymer, and a spinning solution of the polyurethane-urea fiber is prepared by appropriately reacting with the prepolymer, followed by spinning to obtain a elastic yarn.

이러한 폴리우레탄우레아 탄성사는 높은 탄성을 갖는 고유의 특징 때문에 다양한 용도로 활발하게 사용되고 있으며, 그 용도 범위의 확대에 따라 기존의 섬유에 새로운 부가적인 특성이 계속하여 요구되고 있다.These polyurethane-urea elastic yarns are actively used for various purposes because of their inherent characteristics with high elasticity, and as the range of use thereof is expanded, new additional characteristics are continuously required in existing fibers.

일반적으로 탄성사는 시간 경시에 따른 후중합 과정으로 인해 원사의 강도 및 모듈러스 등의 물성 상승이 발현되는 반면에, 원사의 신도 및 Max DR 등의 물성이 감소되는 현상이 발생할 수 있다.In general, the elastic yarn exhibits an increase in strength and modulus of the yarn due to the polymerization process after a lapse of time, while the physical properties such as elongation and Max DR of the yarn may be reduced.

특히, 생산 시기가 다른 원사를 혼합하여 사용하는 경우, 원단의 세트 정도의 차이 및 원단의 줄(streak)를 유발시키는 문제점이 있었다.
Particularly, when yarns having different production periods are mixed and used, there is a problem that the difference in the degree of the set of the fabric and the streak of the fabric are caused.

본 발명은 상술한 문제점을 해소하기 위한 것으로, 열세트성이 우수하고 경시에 따른 물성 변화가 적은 폴리우레탄우레아 탄성사를 제조함으로서, 원단의 줄(streak) 발생 억제 및 품위를 향상시키는데 그 주된 목적이 있다.
Disclosure of Invention Technical Problem [8] The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to provide a polyurethane-urea elastic yarn excellent in heat setting property and little change in physical properties with time, have.

본 발명의 일면은, 폴리(테트라메틸렌 에테르)글리콜; 방향족, 지방족 및 지환족 디이소시아네이트 중에서 선택된 1종 또는 2종 이상의 유기 디이소시아네이트; 쇄연장제; 및 n-부틸아민을 포함하는 쇄종지제; 를 포함하는 열세트성이 향상된 폴리우레탄우레아 탄성사를 제공한다.One aspect of the present invention relates to a poly (tetramethylene ether) glycol; One or more organic diisocyanates selected from aromatic, aliphatic and alicyclic diisocyanates; Chain extenders; And n-butylamine; To provide a polyurethane urea elastic yarn with improved heat set properties.

본 발명의 다른 면은, 폴리올과 디이소시아네이트를 1차 중합하여 예비 중합체를 수득하는 단계; 상기 예비 중합체를 유기 용매에 용해 시키고 쇄연장제 및 쇄종지제를 첨가하여 2차 중합을 수행하여 방사원액을 수득하는 단계; 및 상기 방사원액을 건식 또는 습식방사 시켜 폴리우레탄우레아 탄성사를 수득하는 단계; 를 포함하며, 상기 디이소시아네이트는 방향족, 지방족 및 지환족 디이소시아네이트 중에서 선택된 1종 또는 2종 이상의 유기 디이소시아네이트를 포함하며, 상기 쇄종지제는 n-부틸아민을 포함하는 열세트성이 향상된 폴리우레탄우레아 탄성사의 제조 방법을 제공한다.Another aspect of the present invention relates to a process for producing a prepolymer, comprising the steps of: first polymerizing a polyol and a diisocyanate to obtain a prepolymer; Dissolving the prepolymer in an organic solvent, adding a chain extender and a chain terminator to perform a secondary polymerization to obtain a spinning solution; And dry or wet spinning the spinning solution to obtain a polyurethane-urea elastic yarn; Wherein the diisocyanate comprises one or more organic diisocyanates selected from aromatic, aliphatic and alicyclic diisocyanates, and the chain terminator comprises at least one polyisocyanate selected from the group consisting of polyurethane A process for producing urea elastic yarn is provided.

본 발명의 일 실시 예에서, 상기 쇄종지제는 n-부틸아민의 함량이 10 내지 80 몰%을 포함할 수 있다.
In one embodiment of the present invention, the chain terminator may comprise 10 to 80 mol% of n-butylamine.

본 발명의 일 실시 예에 따르면 쇄종지제로 n-부틸아민을 사용함으로써, 저온에서도 열세트성이 우수하도록 하여 열에 민감한 섬유 등과 교편직한 원단을 낮은 온도에서 열세팅을 실시함으로써 열에 민감한 섬유가 열에 의해 취화되지 않도록 하고, 경시변화에 따른 원사 물성 변화가 적어 교편직물에 변부 말림이나 줄(streak)가 발생하지 않도록 하는 효과가 있다.
According to one embodiment of the present invention, by using n-butylamine as the chain terminator, heat setting is performed at low temperature at a low temperature by performing heat setting at a low temperature so as to fabricate a fabric that is sensitive to heat and sensitive to heat, So that there is an effect that there is little change in the physical properties of the yarn due to a change over time, and no curling or streaking occurs in the knitting fabric.

이하, 본 발명의 바람직한 실시 예들을 설명한다. 그러나, 본 발명의 실시 예는 여러 가지 다른 형태로 변형될 수 있으며, 본 발명의 범위가 이하 설명하는 실시 형태로 한정되는 것은 아니다. Hereinafter, preferred embodiments of the present invention will be described. However, the embodiments of the present invention can be modified into various other forms, and the scope of the present invention is not limited to the embodiments described below.

본 발명의 실시 예는 당해 기술분야에서 평균적인 지식을 가진 자에게 본 발명을 더욱 완전하게 설명하기 위해서 제공되는 것이다.Embodiments of the present invention are provided to more fully describe the present invention to those skilled in the art.

덧붙여, 명세서 전체에서 어떤 구성요소를 '포함'한다는 것은 특별히 반대되는 기재가 없는 한 다른 구성요소를 제외하는 것이 아니라 다른 구성요소를 더 포함할 수 있다는 것을 의미한다.In addition, to include an element throughout the specification does not exclude other elements unless specifically stated otherwise, but may include other elements.

본 발명의 일 실시 형태에 따른 탄성사는 과량의 디이소시아네이트에 고분자량의 폴리올을 1차 중합시켜 예비 중합체를 얻는다.In the elastic yarn according to one embodiment of the present invention, a prepolymer is obtained by first polymerizing an excess of diisocyanate with a high molecular weight polyol.

다음으로, 상기 예비 중합체를 유기 용매에 용해시킨 후, 그 용액에 쇄연장제 및 쇄종지제를 첨가하여 2차 중합을 수행하여 방사원액을 제조한다. 이때, 쇄연장제 및 쇄종지제는 전부 한번에 또는 2개 이상의 단계로 첨가될 수 있다.Next, after dissolving the prepolymer in an organic solvent, a chain lengthener and a chain terminator are added to the solution, and a secondary polymerization is carried out to prepare a spinning solution. At this time, the chain extender and the chain extender may be added all at once or in two or more stages.

다음으로, 상기 방사원액을 건식 또는 습식 방사시켜 폴리우레탄우레아 탄성사를 제조한다.Next, the spinning stock solution is dry-spun or wet-spun to produce a polyurethane-urea elastic yarn.

본 실시 예에 사용되는 디이소시아네이트는 방향족, 지방족 및 지환족 디이소시아네이트 중에서 선택된 1종 또는 2종 이상의 유기 디이소시아네이트로서, 예컨대 4,4'-디테닐메탄디이소시아네이트, 2,4'-디페닐메탄디이소시아네이트, 1,5'-나프탈렌디이소시아네이트, 1,4'-페닐렌디이소시아네이트, 헥사메틸렌 디이소시아네이트, 1,4'-시클로헥산디이소시아네이트, 4,4'-디시클로헥실 메탄디이소시아네이트, 이소포론디이소시아네이트 등이 있다.The diisocyanate used in this embodiment is one or more organic diisocyanates selected from aromatic, aliphatic and alicyclic diisocyanates, and examples thereof include 4,4'-ditenylmethane diisocyanate, 2,4'-diphenylmethane Diisocyanate, 1,5'-naphthalene diisocyanate, 1,4'-phenylene diisocyanate, hexamethylene diisocyanate, 1,4'-cyclohexane diisocyanate, 4,4'-dicyclohexylmethane diisocyanate, isophorone Diisocyanate, and the like.

일반적으로 2,4'-MDI는 입체 구조를 가지고 있어 하드 세그먼트(hard segment) 내의 분자간 수소 결합 또는 분자 내 수소 결합이 약화됨으로써, 소프트 세그먼트(soft segment)의 함량이 증가하는 것과 동일한 효과를 나타내므로, 이에 소프트 도메인(soft domain)이 많이 형성되어 세트성이 우수한 탄성사를 수득할 수 있다.In general, the 2,4'-MDI has a stereostructure, and exhibits the same effect as increasing the content of the soft segment by weakening the intermolecular hydrogen bond or the intramolecular hydrogen bond in the hard segment , And a lot of soft domains are formed thereon, so that an elastic yarn having excellent set property can be obtained.

본 발명에서 사용 가능한 폴리올은 폴리테트라메틸렌에테르 글리콜, 폴리프로필렌 글리콜, 폴리카보네이트디올 및 이들의 조합으로 구성된 군에서 선택되는 적어도 1종 이상을 예시할 수 있으나, 본 발명이 이에 한정되는 것은 아니다. 상기 폴리올의 분자량은 500 내지 8000일 수 있으며, 더 바람직하게는 1200 내지 3000일 수 있다.The polyol usable in the present invention may be at least one selected from the group consisting of polytetramethylene ether glycol, polypropylene glycol, polycarbonate diol, and combinations thereof, but the present invention is not limited thereto. The molecular weight of the polyol may be from 500 to 8000, and more preferably from 1200 to 3000. [

상기 쇄연장제에 사용되는 디아민류는 에틸렌디아민, 1,2-디아미노프로판, 1,3-디아미노프로판, 1,4-디아미노부탄, 2,3-디아미노부탄, 1,5-디아미노펜탄, 1,6-헥사메틸렌디아민 및 1,4-씨클로헥산디아민 등에서 선택된 1종 또는 2종 이상의 혼합물을 예시할 수 있으며, 본 발명이 이에 한정되는 것은 아니다.The diamines used in the chain extender may be selected from the group consisting of ethylenediamine, 1,2-diaminopropane, 1,3-diaminopropane, 1,4-diaminobutane, 2,3-diaminobutane, Aminopentane, 1,6-hexamethylenediamine, 1,4-cyclohexanediamine, and the like, and the present invention is not limited thereto.

한편, 폴리우레탄우레아의 분자량을 조절하기 위해 쇄종지제를 사용하게 되는데, 이 쇄종지제로 종래와 같이 디에틸아민 만을 사용하는 경우, 방사 과정 중 높은 열량에 따른 후중합의 증가 및 원사 시산 후 시간 경시에 후중합 과정으로 인해 원사의 강도 및 모듈러스 등의 물성 상승이 발현되는 반면 원사의 신도 및 Max DR, 세트성 등의 물성은 감소할 수 있다.On the other hand, a chain terminator is used to control the molecular weight of the polyurethaneurea. When diethylamine alone is used as the chain terminator, an increase in post polymerization and a post- The physical properties such as yarn elongation, Max DR, and set properties can be reduced while the post-polymerization process over time causes increase in the physical properties such as strength and modulus of the yarn.

또한, 생산 시기가 다른 원사를 혼합 사용할 경우 원단의 세트 정도 차이 및 원단의 줄(streak)을 유발시킬 수 있다.In addition, when mixed yarns having different production periods are used, the difference in the set of the fabric and the streak of the fabric can be caused.

이에, 본 실시 형태에서는, 쇄종지제로서 n-부틸아민을 사용하며, 이에 상기 n-부틸아민이 후중합에 따른 물성의 변화를 최소화하여 열세트성을 향상시키므로, 낮은 온도에서 열세팅을 실시하여도 상대사의 열적 취하가 일어나지 않아 종래보다 원단의 태를 향상시킬 수 있고, 열세팅 후의 가공지에서는 변무 말림이 발생하는 것을 방지할 수 있다.Thus, in the present embodiment, n-butylamine is used as the chain terminator, and the n-butylamine improves the heat setting property by minimizing the change of physical properties due to the post polymerization, so that the heat setting is performed at a low temperature The thermal decoupling of the opponent yarn does not occur, so that the state of the fabric can be improved as compared with the conventional method, and occurrence of curling in the processed paper after the heat setting can be prevented.

이때, 상기 쇄종지제는 전체 쇄종지제에 대하여 바람직하게 n-부틸아민 10 내지 80 몰%을 포함할 수 있다.At this time, the chain terminator may preferably include 10 to 80 mol% of n-butylamine with respect to the full-chain terminator.

상기 쇄종지제의 사용량이 10 몰% 미만인 경우 과량의 디에틸아민으로 인해 후중합의 촉진을 제어할 수 없게 되며, 쇄종지제의 사용량이 80 몰%를 초과하는 경우 과도한 후중합 억제로 인해 낮은 모듈러스 및 방사를 위한 폴리머 점도 상승이 억제되는 점이 우려될 수 있다.If the amount of the chain terminator used is less than 10 mol%, the promotion of the post polymerization may not be controlled due to excessive diethylamine. If the amount of the chain terminator used exceeds 80 mol%, excessive polymerization may be inhibited It may be feared that the polymer viscosity rise for modulus and radiation is suppressed.

또한, 본 발명에서는 자외선, 대기 스모그, 스판덱스 가공에 수반되는 열처리 과정 등에 의한 폴리우레탄우레아의 변색과 물성 저하를 방지하기 위해, 방사원액에 입체장애 페놀계 화합물, 벤조퓨란-온계 화합물, 세미카바자이드계 화합물, 벤조 트리아졸계 화합물, 중합체성 3급 아민 안정제 등을 적절히 조합하여 첨가할 수 있다.In addition, in the present invention, in order to prevent discoloration and deterioration of physical properties of polyurethane-urea by heat treatment accompanying ultraviolet rays, atmospheric smog, and spandex processing, it is preferable to add a phenolic compound, a benzofuran- Based compound, a benzotriazole-based compound, a polymeric tertiary amine stabilizer, and the like.

나아가, 본 발명의 폴리우레탄우레아 탄성사는 필요시 상기 성분 외에도 이산화티탄, 마그네슘 스테아레이트 등과 같은 첨가제, 산화방지제, 염색성 향상제, 열산화안정제, 항균제, 광안정제 또는 대전방지제 등을 더 포함할 수 있다. 이러한 기타 첨가제의 첨가 방법에는 특별한 제한이 없으며, 적정 혼합과 같은 통상의 방법을 사용할 수 있다.
Further, the polyurethane-urea elastic yarn of the present invention may further contain additives such as titanium dioxide, magnesium stearate and the like, an antioxidant, a dyeability-improving agent, a thermal oxidation stabilizer, an antibacterial agent, a light stabilizer or an antistatic agent. There is no particular limitation on the method of adding these other additives, and conventional methods such as proper mixing can be used.

이하에서 실시예 및 비교예를 들어 본 발명에 대해 상세히 설명하기로 한다.
Hereinafter, the present invention will be described in detail with reference to Examples and Comparative Examples.

실시예 1:Example 1:

캡핑비(CR) 1.65, 2,4'-디페닐메탄디이소시아네이트 5몰% 함량과 4,4'-디페닐메탄디이소시아네이트 95몰% 함량으로 조제하였다. 쇄연장제는 상기 언급한 에틸렌디아민과 1,2-디아미노 프로판을, 쇄종지제는 디에틸아민과 n-부틸아민을 사용하였다. 쇄연장제와 쇄종지제의 비율은 12.5:1로 하였으며, 에틸렌디아민과 1,2-디아미노 프로판의 비율은 80몰%과 20몰%로, n-부틸아민과 디에틸아민의 비율은 10몰%과 90몰%로 하였다. 사용된 아민은 총 농도 7몰%로 조제되었으며, 용제로는 디메틸아세트아마이드를 사용하였다.A capping ratio (CR) of 1.65, a content of 5 mol% of 2,4'-diphenylmethane diisocyanate and a content of 4,4'-diphenylmethane diisocyanate of 95 mol%. The chain extender used was the above-mentioned ethylenediamine and 1,2-diaminopropane, and the chain terminator used was diethylamine and n-butylamine. The ratio of the chain extender and the chain terminator was 12.5: 1, the ratio of ethylenediamine to 1,2-diaminopropane was 80 mol% and 20 mol%, the ratio of n-butylamine and diethylamine was 10 Mol% and 90 mol%, respectively. The amine used was adjusted to a total concentration of 7 mol%, and dimethylacetamide was used as the solvent.

상기 중합물의 고형분 대비 첨가제로서 에틸렌비스(옥시에틸렌)비스-(3-(5-t-부틸-4-히드록시-m-토일)-프로피오네이트) 1.5중량%, 5,7-디-t-부틸-3-(3,4-디메틸페닐)-3H-벤조퓨란-2-온 0.5중량%, 1,1,1',1'-테트라메틸-4,4'-(메틸렌-디-p-페닐렌)디세미카바지드 1중량%, 폴리(N,N-디에틸-2-아미노에틸 메타크릴레이트) 1중량%, 이산화티탄 0.1중량%를 첨가 혼합하여 폴리우레탄우레아 방사원액을 얻었다. As a solid preparation of the additive polymer of ethylene bis (oxyethylene) bis - (3- (5- t-butyl-4-hydroxy-m-weekends) -propionate), 1.5% by weight, 5,7-di-t 0.5% by weight of 1,1,1 ', 1'-tetramethyl-4,4' - (methylene-di- p -tert-butylphenyl) 1% by weight of poly (N, N-diethyl-2-aminoethyl methacrylate) and 0.1% by weight of titanium dioxide were added and mixed to obtain a polyurethane urea spinning stock solution.

위와 같이 수득한 방사 원액을 건식 방사에 의해, 900m/min의 속도로 20 데니아의 폴리우레탄우레아 탄성사를 제조하고, 그 물성을 평가하여 하기 표 1 및 표 2에 나타내었다.
Polyurethane-urea elastic yarn of 20 denier was produced at a speed of 900 m / min by dry spinning the fiber stock solution obtained as described above, and physical properties thereof were evaluated and shown in the following Tables 1 and 2.

실시예 2: Example 2:

n-부틸아민과 디에틸아민의 비율 50몰%과 디에틸아민 50몰% 함량비로 폴리우레탄우레아 중합물을 제조한 것을 제외하고는 실시예 1과 동일하게 실시하여, 폴리우레탄우레아 탄성사를 제조하고, 그 물성을 평가하여 하기 표 1 및 표 2에 함께 나타내었다.
A polyurethane-urea elastic yarn was prepared in the same manner as in Example 1, except that a polyurethane-urea polymer was produced in a proportion of 50 mol% of n-butylamine and diethylamine and 50 mol% of diethylamine, The properties thereof were evaluated and are shown together in Tables 1 and 2 below.

실시예 3: Example 3:

n-부틸아민과 디에틸아민의 비율 80몰%과 디에틸아민 20몰% 함량비로 폴리우레탄우레아 중합물을 제조한 것을 제외하고는 실시예 1과 동일하게 실시하여, 폴리우레탄우레아 탄성사를 제조하고, 그 물성을 평가하여 하기 표 1 및 표 2에 함께 나타내었다.
A polyurethane urea elastic yarn was prepared in the same manner as in Example 1, except that a polyurethane urea polymer was produced in a proportion of 80 mol% of n-butylamine and diethylamine and 20 mol% of diethylamine, The properties thereof were evaluated and are shown together in Tables 1 and 2 below.

비교예 1: Comparative Example 1:

n-부틸아민을 첨가하지 않고, 900m/min의 속도로 20데니아 폴리우레탄우레아 탄성사를 제조한 것을 제외하고는 실시예 1과 동일조건으로 제조하였다.
except that n-butylamine was not added and 20 denier polyurethane-urea elastic yarn was produced at a speed of 900 m / min.

비교예 2: Comparative Example 2:

n-부틸아민을 100몰% 첨가하고, 900m/min의 속도로 20데니아 폴리우레탄우레아 탄성사를 제조한 것을 제외하고는 실시예 1과 동일조건으로 제조하였다.
except that n-butylamine was added in an amount of 100 mol% and 20 denier polyurethane-urea elastic yarn was produced at a rate of 900 m / min.

* 원사의 강신도 * The strength of yarn

자동 강신도 측정장치(MEL기, Textechno社)를 이용하여 시료길이 10cm, 인장속도 100cm/min로 하여 측정한다. 이 때 파단 시의 강력과 신도값이 측정되며, 원사 200% 신장 시 원사에 걸리는 하중(200% 모듈러스)도 측정된다. 또한 시간 경시에 따른 강신도를 측정하였다.
Measurement is made at a sample length of 10 cm and a tensile speed of 100 cm / min using an automatic power measuring device (MEL, Textechno). In this case, the strength and elongation at break are measured, and the load (200% modulus) applied to the yarn at 200% elongation is also measured. We also measured the strength over time.

* 원사의 열세트성 * Thermal set of yarns

초기 원사(L0)를 대기에 노출된 상태로 100% 신장(L1)한 후, 170℃에서 1분간 건열 처리하였다가 실온으로 냉각한 다음 원사의 길이(L2)를 측정하였다. 건열 처리한 원사를 이완된 상태로 100℃에서 30분간 습열 처리한 뒤 실온에서 건조하여 원사의 길이(L3)를 측정하여, 아래 식에 따라 원사의 건열세트성 및 Heat Set Efficiency(HSE)를 계산하였다.The initial yarn L0 was subjected to 100% elongation (L1) in a state exposed to the atmosphere, followed by dry heat treatment at 170 ° C for 1 minute, cooling to room temperature and measuring the length (L2) of the yarn. Dry heat treated yarn is heat treated at 100 ℃ for 30 minutes in a relaxed state and then dried at room temperature to measure the length (L3) of the yarn and calculate the heat set efficiency and heat setting efficiency (HSE) of the yarn according to the following formula Respectively.

건열세트성(%) = {(L2-L0)/(L1-L0)} X 100Dry heat setting property (%) = {(L2-L0) / (L1-L0)} X 100

HSE(%) = {(L3-L0)/(L1-L0)} X 100
HSE (%) = {(L3-L0) / (L1-L0)} X100

* Lab . 점도 경시율 * Lab . Viscosity aging rate

쇄연장제 및 서로 다른 쇄종지제의 종류 및 함량에 따라 조제된, 점도 2000 Poise 의 중합물은 실험실용 반응기에 700g 투입 후 더블 헬리컬(double helical) 형태의 교반기로 72시간 동안 8rpm의 속도로 교반하였다. 이때 실험실용 반응기에는 40도의 물이 통수되었으며, 점도 경시율 측정을 위해 24시간마다 점도를 측정하고, 72시간 후의 점도(V1)와 초기 점도(V0, 2000 Poise)의 차로 점도 경시율을 계산하였다.The polymer having a viscosity of 2000 Poise prepared according to the type and content of the chain extender and the different chain terminators was added to the laboratory reactor in an amount of 700 g and stirred at a speed of 8 rpm for 72 hours with a double helical type stirrer . At this time, 40 ° C. water was passed through the laboratory reactor, and the viscosity was measured every 24 hours to measure the viscosity retention rate. The viscosity retention rate was calculated by the difference between the viscosity (V1) and the initial viscosity (V0, 2000 Poise) .

점도경시율(Poise/hr) = (V1-V0)/72hr
Viscosity Loss Percentage (Poise / hr) = (V1-V0) / 72hr

* 환편 품위 평가 * Evaluation of recycled products

탄성사와 Nylon 원사를 사용하여 금용 사(社)의 직경 32인치, 28게이지, 96 피더(feeder)의 규격을 갖는 환편기를 이용해 환편물을 제작하였다. 이 환편물은 PET 원사 100데니어, 상기에 의해 제조된 탄성사 20 데니어를 사용하여 편직하였고, 탄성사의 함량은 전체 편물 중량 대비 8% 이다.Circular knitted fabrics were fabricated using elastic yarn and Nylon yarn using a circular knitting machine having a diameter of 32 inches, 28 gauge, and 96 feeders. The knitted fabric was knitted using PET yarn 100 denier and elastic yarn 20 denier manufactured by the above, and the content of elastic yarn was 8% to be.

교·편직된 PET/폴리우레탄우레아 탄성사로 만든 환편 원단을 프리세팅(Pre-setting)→염색→파이널세팅(Final-setting) 처리한 후, 5m의 환편 원단 품위를 평가하였으며, 평가 기준은 다음과 같다.The circular knitted fabrics made of cross-linked PET / polyurethane urea elastic yarn were subjected to pre-setting, dyeing and final-setting, and then evaluated for the quality of the circular knitted fabric of 5 m. same.

3mm 이상의 줄(streak) : -10점3mm or more streak: -10 points

2~3mm 이하의 줄(streak) : -5점Streak less than 2 ~ 3mm: -5 points

1mm 의 줄(streak) : -1점
1 mm streak: -1 point

강도
[g/d]
burglar
[g / d]
신도
[%]
Shindo
[%]
모듈러스
[g]
Modulus
[g]
HSE
[%]
HSE
[%]
Lab. 점도 경시율[P/hr]Lab. Viscosity over time [P / hr] 품위 점수
[점]
Grade point
[point]
실시예 1Example 1 1.181.18 503503 4.04.0 5656 5353 8484 실시예 2Example 2 1.201.20 512512 4.04.0 6060 5252 8787 실시예 3Example 3 1.181.18 515515 3.83.8 6767 5353 8686 비교예 1Comparative Example 1 1.201.20 495495 4.04.0 5050 5252 8080 비교예 2Comparative Example 2 1.231.23 545545 3.33.3 7272 2323 8787

경시시간Hourly Time 강도burglar 신도Shindo 200%M200% M HSE(%)HSE (%) 실시예1Example 1 0일0 days 1.181.18 503503 4.04.0 5656 10일10 days 1.201.20 506506 4.04.0 5656 30일30 days 1.191.19 505505 4.04.0 5656 실시예2Example 2 0일0 days 1.201.20 512512 4.04.0 6060 10일10 days 1.201.20 511511 4.14.1 5959 30일30 days 1.211.21 514514 4.04.0 6060 실시예3Example 3 0일0 days 1.181.18 515515 3.93.9 6767 10일10 days 1.171.17 515515 4.04.0 6666 30일30 days 1.191.19 518518 3.93.9 6666 비교예1Comparative Example 1 0일0 days 1.201.20 495495 4.04.0 5050 10일10 days 1.251.25 480480 4.24.2 4848 30일30 days 1.281.28 472472 4.34.3 4646 비교예2Comparative Example 2 0일0 days 1.231.23 545545 3.33.3 7272 10일10 days 1.221.22 543543 3.43.4 7070 30일30 days 1.221.22 548548 3.33.3 7171

본 발명은 상술한 실시 형태에 의해 한정되는 것이 아니며 첨부된 청구범위에 의해 한정하고자 한다.The present invention is not limited to the above-described embodiments but is intended to be limited by the appended claims.

따라서, 청구범위에 기재된 본 발명의 기술적 사상을 벗어나지 않는 범위 내에서 당 기술분야의 통상의 지식을 가진 자에 의해 다양한 형태의 치환, 변형 및 변경이 가능할 것이며, 이 또한 본 발명의 범위에 속한다고 할 것이다.It will be apparent to those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims. something to do.

Claims (4)

폴리(테트라메틸렌 에테르)글리콜;
방향족, 지방족 및 지환족 디이소시아네이트 중에서 선택된 1종 또는 2종 이상의 유기 디이소시아네이트;
쇄연장제; 및
쇄종지제를 포함하는 폴리우레탄우레아 탄성사에 있어서,
상기 쇄종지제로는 n-부틸아민과 디에틸아민을 10몰% 내지 80몰%, 20몰% 내지 90몰%의 함량 비율로 혼합하여 함께 사용하여서 된 것을 특징으로 하는 열세트성이 향상된 폴리우레탄우레아.
Poly (tetramethylene ether) glycol;
One or more organic diisocyanates selected from aromatic, aliphatic and alicyclic diisocyanates;
Chain extenders; And
In the polyurethane-urea elastic yarn comprising a chain ending agent,
Wherein the chain terminating agent is a mixture of n-butylamine and diethylamine in an amount of 10 mol% to 80 mol% and 20 mol% to 90 mol%, and is used together. The thermosetting polyurethane Urea.
삭제delete 폴리올과 디이소시아네이트를 1차 중합하여 예비 중합체를 수득하는 단계;
상기 예비 중합체를 유기 용매에 용해 시키고 쇄연장제 및 쇄종지제를 첨가하여 2차 중합을 수행하여 방사원액을 수득하는 단계; 및
상기 방사원액을 건식 또는 습식방사 시켜 폴리우레탄우레아 탄성사를 제조하는 방법에 있어서,
상기 쇄종지제로는 n-부틸아민과 디에틸아민을 10몰% 내지 80몰%, 20몰% 내지 90몰%의 함량 비율로 혼합하여 함께 사용하여서 되는 것을 특징으로 하는 열세트성이 향상된 폴리우레탄우레아 탄성사의 제조 방법.
Polymerizing a polyol and a diisocyanate to obtain a prepolymer;
Dissolving the prepolymer in an organic solvent, adding a chain extender and a chain terminator to perform a secondary polymerization to obtain a spinning solution; And
A method for producing a polyurethane-urea elastic yarn by dry or wet spinning the spinning solution,
Wherein the chain terminating agent is a mixture of n-butylamine and diethylamine in an amount of 10 mol% to 80 mol% and 20 mol% to 90 mol%, and is used together. The thermosetting polyurethane Method of manufacturing urea elastic yarn.
삭제delete
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018080063A1 (en) * 2016-10-24 2018-05-03 (주)효성 Polyurethaneurea elastic yarn having high elongation, and manufacturing method therefor

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CN104372438B (en) * 2014-11-19 2016-03-30 浙江华峰氨纶股份有限公司 The preparation method of the polyurethaneurea elastic fiber that unwinding is improved

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010113693A (en) * 1999-02-19 2001-12-28 메리 이. 보울러 Process for Melt Spinning Spandex Fibers
US20040068080A1 (en) 2002-10-04 2004-04-08 Hong Liu Spandex of a particular composition and process for making same
KR100710737B1 (en) 2001-07-24 2007-04-23 라디시스판덱스 코포레이션 Improved spandex compositions
KR20120077016A (en) * 2010-12-30 2012-07-10 주식회사 효성 Method of making polyurethaneurea elastic fiber modified by polydimethylsiloxane

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20010113693A (en) * 1999-02-19 2001-12-28 메리 이. 보울러 Process for Melt Spinning Spandex Fibers
KR100710737B1 (en) 2001-07-24 2007-04-23 라디시스판덱스 코포레이션 Improved spandex compositions
US20040068080A1 (en) 2002-10-04 2004-04-08 Hong Liu Spandex of a particular composition and process for making same
KR20120077016A (en) * 2010-12-30 2012-07-10 주식회사 효성 Method of making polyurethaneurea elastic fiber modified by polydimethylsiloxane

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018080063A1 (en) * 2016-10-24 2018-05-03 (주)효성 Polyurethaneurea elastic yarn having high elongation, and manufacturing method therefor

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