WO2012091504A2 - Polyurethane elastic fiber and method for manufacturing same - Google Patents

Polyurethane elastic fiber and method for manufacturing same Download PDF

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Publication number
WO2012091504A2
WO2012091504A2 PCT/KR2011/010343 KR2011010343W WO2012091504A2 WO 2012091504 A2 WO2012091504 A2 WO 2012091504A2 KR 2011010343 W KR2011010343 W KR 2011010343W WO 2012091504 A2 WO2012091504 A2 WO 2012091504A2
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WIPO (PCT)
Prior art keywords
prepolymer
diisocyanate
polyurethane elastic
glycol
elastic yarn
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PCT/KR2011/010343
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French (fr)
Korean (ko)
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WO2012091504A3 (en
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정호영
강연수
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주식회사 효성
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Publication of WO2012091504A2 publication Critical patent/WO2012091504A2/en
Publication of WO2012091504A3 publication Critical patent/WO2012091504A3/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
    • D01F6/58Monocomponent 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
    • 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

Definitions

  • the present invention relates to a method for producing a polyurethane elastic yarn that is environmentally friendly and harmless to the human body.
  • Elastic fibers are widely used in stretch fabric materials or industrial materials such as legwear, innerwear, sportswear, etc. because of their excellent stretch properties.
  • polyurethane elastic yarns are used in combination with various materials, such as nylon or polyester yarns, as well as natural fibers such as cotton or wool, semisynthetic fibers, and the like.
  • the present invention has been made to solve the above problems, to provide a polyurethane elastic yarn that is environmentally friendly and safe to human body by not using an organic solvent in the manufacturing process.
  • Method for producing a polyurethane elastic yarn the step of preparing a first prepolymer by reacting a polyisocyanate, ester or ester-based polyol; Reacting an isocyanate with a bifunctional or polyfunctional alcohol comprising —COOH or —SO 3 H, to prepare a second prepolymer; Preparing a third prepolymer by chain-extending the reaction product of the first prepolymer and the second prepolymer; And neutralizing the third prepolymer to prepare a dispersion.
  • the present invention provides a method for producing a polyurethane elastic yarn without using a conventional organic solvent.
  • a polyurethane elastic yarn is produced by drying it by a dry process.
  • Method for producing a polyurethane elastic yarn the step of preparing a first prepolymer by reacting a polyisocyanate, ester or ester-based polyol; Reacting an isocyanate with a bifunctional or polyfunctional alcohol comprising —COOH or —SO 3 H, to prepare a second prepolymer; Preparing a third prepolymer by chain-extending the reaction product of the first prepolymer and the second prepolymer; And neutralizing the third prepolymer to prepare a dispersion.
  • aromatic, aliphatic and alicyclic diisocyanates or mixtures thereof may be used.
  • tolylene-2,4-diisocyanate, tolylene-2,6-diisocyanate, meta-phenylene diisocyanate, biphenylene-4,4'- diisocyanate methylenebis ((4-phenyl Isocyanate), 4-chloro-1,3-phenylene diisocyanate, naphthalene-1,5-diisocyanate, tetramethylene-1,4-diisocyanate, hexamethylene-1,6-diisocyanate, decamethylene-1, 10-diisocyanate, cyclohexylene-1,4-diisocyanate, methylenebis (4-cyclohexyl isocyanate), tetrahydronaphthylene diisocyanate, isophorone diiso
  • isophorone diisocyanate hexamethylene-1,6-diisocyanate, cyclohexylene-1,4-diisocyanate, 4 , 4'-methylenebis (cyclohexyl isocyanate) and the like can be used.
  • polyester polyols examples include polyester polyols and polyether polyols.
  • Suitable polyester polyols are preferably obtained by condensation of a dicarboxylic acid compound with a diol compound, wherein the dicarboxylic acid compound is succinic acid, glutaric acid, adipic acid, subberic acid, azelanic acid.
  • Sebacic acid dodecanedicarboxylic acid, hexahydrophthalic acid, isophthalic acid, terephthalic acid, ortho-phthalic acid, tetrachlorophthalic acid, 1,5-naphthalenedicarboxylic acid, fumaric acid, maleic acid, itaconic acid, citraconic acid, mesaconic acid And tetrahydrophthalic acid.
  • the diol compound include ethylene glycol, propylene glycol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1.5-pentanediol, and 1,6-hexane.
  • Suitable polyether polyols include polyethylene glycol, polypropylene glycol, polytetramethylene glycol, and the like. The molecular weight of the polyols varies from 400 to 10,000, but the suitable molecular weight is about 400 to 3,000.
  • the polyol used in the present invention may be at least one selected from the group consisting of ether polyols such as polytetramethylene ether glycol, polypropylene glycol, and the like.
  • the molecular weight of the polyol used in the present invention may be about 500 to 4000.
  • Anionic chain extenders and cationic chain extenders may be used as the ionic chain extender for self-emulsifying the prepolymer, and as the anionic chain extender, a compound including a carboxyl group or a sulfonate group may be used. , 2,2-dimethylolpropionic acid, 2,2-dimethylolbutanoic acid, polypropylene glycol with sodium sulfonate group, 2,4-diamino-5-methylbenzenesulfonic acid and the like can be used.
  • tertiary amine diols and diamine compounds for example, methyl diethanolamine may be used.
  • the ionic chain extender may include 0.5 to 25% by weight, preferably 2 to 7% by weight based on the total polyurethane.
  • Neutralizing agents are used to convert the ionic groups into salts in order to enable the dispersion of the anionic or cationic groups covalently bonded in the main chain of the polyurethane for self-emulsification.
  • Such neutralizing agents include, when anionic, sodium hydroxide, potassium hydroxide, lithium hydroxide, ammonia, trimethylamine, triethylamine, triisopropylamine, tributylamine, N, N-dimethylcyclohexylamine, N, N-dimethylaniline , N-methylmorpholine, N-methylpiperazine, N-methylpyrrolidine, N-methylpiperidine, and the like, and in the case of cationic acid, phosphoric acid, hydrochloric acid, acetic acid, formic acid, malic acid Will be used. It can be used more than 80% stoichiometrically with respect to the ionic group.
  • the isocyanate and polyol are reacted at a ratio of 1.1: 1 to 4.0: 1 to form polyisocyanate.
  • the prepolymer may be further polymerized by reaction with a chain extender after it is dispersed in water.
  • a chain extender at least one selected from the group consisting of polyamines and lower alcohols may be used.
  • the polyamine include hydrazine, ethylenediamine, piperazine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, N, N, N-tris (2-aminoethyl) amine, N- (2-piperazinoethyl) ethylenediamine, N, N'-bis (2-aminoethyl) piperazine, N, N, N'-tris (2-aminoethyl) ethylenediamine, N- [N- (2 -Aminoethyl) -2-aminoethyl] -N '-(2-aminoethyl) piperazine, N- (2-aminoethyl) -N
  • Lower alcohols used at this time include ethylene glycol (EG), propylene glycol (Propylene Glycol: PG), diethylene glycol (Diethylene Glycol: DEG), dipropylene glycol (DPG), butylene glycol (Butylene) Glycol: 1,4BD)).
  • EG ethylene glycol
  • Propylene Glycol: PG propylene glycol
  • DEG diethylene glycol
  • DPG dipropylene glycol
  • butylene glycol butylene glycol
  • the dispersion is an aqueous ionic hydrophilic polyurethane dispersion, by adding a viscosity modifier to the dispersion to adjust the viscosity, by performing a dry spinning process using the dispersion can be produced an environmentally friendly and harmless polyurethane elastic yarn. .
  • Polyurethane elastic yarn produced by the above method can be used as it is, or covered with polyamide fibers and the like can be suitably used in thin knitted fabrics such as stockings, tights, socks.
  • the first prepolymer was prepared by reacting 4,4'-methylene diphenyl diisocyanate with polytetramethylene ether glycol (molecular weight 1800).
  • a second prepolymer was prepared using 2,2-dimethylolpropionic acid and 4,4'-methylene diphenyl diisocyanate.
  • the first prepolymer and the second prepolymer were reacted, and a third prepolymer was prepared using ethylenediamine (EDA) as a chain extender.
  • EDA ethylenediamine
  • a dispersion was prepared while adding deionized water, and the dispersion was added with a thickening agent BYK ® -428 to 250 cps. It was adjusted to (40 °C), and the 20 denier polyurethane elastic yarn was prepared through a dry process using the dispersion. And the physical properties were evaluated and shown in Table 1.
  • polyurethane elastic yarn was manufactured in the same manner as in Example 1 except that the viscosity of the dispersion was adjusted to 180 cps (40 ° C.). And the physical properties were evaluated and shown in Table 1.
  • a capping ratio (CR) of 1.55 and polyol polytetramethylene ether glycol (molecular weight 1800) was used, and 4,4'-diphenylmethane diisocyanate was mixed and prepared.
  • Ethylenediamine was used as the chain extender and diethylamine was used as the chain terminator.
  • the ratio of the chain extender to the chain terminator was 10: 1, and the amine used was prepared at a total concentration of 7 mol%, and dimethylacetamide was used as a solvent to obtain a polyurethaneurea spinning stock solution.
  • the spinning stock solution obtained as described above was prepared in a polyurethane elastic yarn through a dry spinning process, and the physical properties thereof are shown in Table 1 below.

Abstract

Provided is a method for manufacturing an eco-friendly polyurethane elastic fiber which is harmless to the human body, by providing a method for manufacturing a polyurethane elastic fiber, which does not use an organic solvent, according to a process of dry-weaving of an aqueous, ionic, and hydrophilic polyurethane dispersion liquid.

Description

폴리우레탄 탄성사 및 이의 제조방법Polyurethane elastic yarn and its manufacturing method
본 발명은 친환경적이고 인체에 무해한 폴리우레탄 탄성사의 제조방법에 관한 것이다.The present invention relates to a method for producing a polyurethane elastic yarn that is environmentally friendly and harmless to the human body.
탄성 섬유는 우수한 신축 특성으로 인하여 레그웨어, 이너웨어, 스포츠 웨어 등의 신축성 직물 재료 또는 산업 자재 재료로 폭넓게 사용되고 있다.Elastic fibers are widely used in stretch fabric materials or industrial materials such as legwear, innerwear, sportswear, etc. because of their excellent stretch properties.
이러한 탄성 섬유 중에서, 특히 폴리우레탄 탄성사는 다양한 소재, 예컨대 나일론사나 폴리에스테르사와 같은 합성 섬유뿐만 아니라, 면이나 울 등의 천연 섬유, 반합성 섬유 등과 조합되어 그 용도가 점차 광범위하게 사용되고 있다.Among these elastic fibers, in particular, polyurethane elastic yarns are used in combination with various materials, such as nylon or polyester yarns, as well as natural fibers such as cotton or wool, semisynthetic fibers, and the like.
폴리우레탄 탄성사의 제조에 있어서, 유기 용매를 사용하여 폴리머를 용해시킨 후 유기 용매를 고온에서 건조시키는 방법이 일반적으로 사용되어 왔다.  그러나, 이러한 유기 용매가 대기 중에 방출되는 과정, 또는 제조된 탄성사에 일정량이 잔류하여 환경적 또는 인체에 유해한 문제점이 있을 수 있었다.In the production of polyurethane elastic yarns, a method of dissolving a polymer using an organic solvent and then drying the organic solvent at a high temperature has generally been used. However, there may be a problem that the organic solvent is released into the atmosphere, or a certain amount of the elastic yarn produced to be harmful to the environment or human body.
본 발명은 상기의 문제를 해결하고자 안출된 것으로, 제조 과정에서 유기 용매를 사용하지 않음으로 인해 친환경적이고 인체에 안전한 폴리우레탄 탄성사를 제공하고자 한다.The present invention has been made to solve the above problems, to provide a polyurethane elastic yarn that is environmentally friendly and safe to human body by not using an organic solvent in the manufacturing process.
본 발명에 따른 폴리우레탄 탄성사의 제조방법은, 폴리이소시아네이트와, 에스테르 또는 에스테르계 폴리올을 반응시켜 제1 예비중합체를 제조하는 단계; -COOH 또는 -SO3H를 포함하는 2관능성 또는 다관능성 알코올과, 이소시아네이트를 반응시켜 제2 예비중합체를 제조하는 단계; 상기 제1 예비중합체 및 제2 예비중합체의 반응 생성물을 쇄연장 반응시켜 제3 예비중합체를 제조하는 단계; 및 상기 제3 예비중합체를 중화시켜 분산액을 제조하는 단계를 포함한다.Method for producing a polyurethane elastic yarn according to the invention, the step of preparing a first prepolymer by reacting a polyisocyanate, ester or ester-based polyol; Reacting an isocyanate with a bifunctional or polyfunctional alcohol comprising —COOH or —SO 3 H, to prepare a second prepolymer; Preparing a third prepolymer by chain-extending the reaction product of the first prepolymer and the second prepolymer; And neutralizing the third prepolymer to prepare a dispersion.
본 발명의 제조방법에 의하면, 제조 과정에서 유기 용매를 사용하지 않음으로 인해 친환경적이고 인체에 안전한 폴리우레탄 탄성사를 수득할 수 있다.According to the production method of the present invention, it is possible to obtain a polyurethane elastic yarn that is environmentally friendly and safe for human body by not using an organic solvent in the manufacturing process.
본 발명은 기존의 유기 용제를 사용하지 않고 폴리우레탄 탄성사를 제조하는 방법을 제공한다.  특히, 수성 이온성 블록 우레탄 그룹을 형성시킴으로써, 수성 이온성 친수성 폴리우레탄 분산액을 제조하고, 이를 건식 공정에 의해 물을 건조시킴으로써 폴리우레탄 탄성사를 제조한다.The present invention provides a method for producing a polyurethane elastic yarn without using a conventional organic solvent. In particular, by forming an aqueous ionic block urethane group, an elastic ionic hydrophilic polyurethane dispersion is prepared and a polyurethane elastic yarn is produced by drying it by a dry process.
본 발명의 일 실시예에 따른 폴리우레탄 탄성사의 제조방법은, 폴리이소시아네이트와, 에스테르 또는 에스테르계 폴리올을 반응시켜 제1 예비중합체를 제조하는 단계; -COOH 또는 -SO3H를 포함하는 2관능성 또는 다관능성 알코올과, 이소시아네이트를 반응시켜 제2 예비중합체를 제조하는 단계; 상기 제1 예비중합체 및 제2 예비중합체의 반응 생성물을 쇄연장 반응시켜 제3 예비중합체를 제조하는 단계; 및 상기 제3 예비중합체를 중화시켜 분산액을 제조하는 단계를 포함한다.Method for producing a polyurethane elastic yarn according to an embodiment of the present invention, the step of preparing a first prepolymer by reacting a polyisocyanate, ester or ester-based polyol; Reacting an isocyanate with a bifunctional or polyfunctional alcohol comprising —COOH or —SO 3 H, to prepare a second prepolymer; Preparing a third prepolymer by chain-extending the reaction product of the first prepolymer and the second prepolymer; And neutralizing the third prepolymer to prepare a dispersion.
상기 프리폴리머의 제조에 사용되는 이소시아네이트로는 방향족, 지방족 및 지환족 디이소시아네이트 또는 이들의 혼합물이 사용될 수 있다. 예를 들면, 톨릴렌-2,4-디이소시아네이트, 톨릴렌-2,6-디이소시아네이트, 메타-페닐렌 디이소시아네이트, 비페닐렌-4,4'-디이소시아네이트, 메틸렌비스((4-페닐 이소시아네이트), 4-클로로-1,3-페닐렌 디이소시아네이트, 나프탈렌-1,5-디이소시아네이트, 테트라메틸렌-1,4-디이소시아네이트, 헥사메틸렌-1,6-디이소시아네이트, 데카메틸렌-1,10-디이소시아네이트, 시클로헥실렌-1,4-디이소시아네이트, 메틸렌비스(4-시클로헥실 이소시아네이트), 테트라히드로나프틸렌 디이소시아네이트, 이소포론 디이소시아네이트, 4,4'-메틸렌비스(시클로헥실 이소시아네이트) 또는 이들 중 2이상의 혼합물로 이루어진 그룹 중에서 선택된 것이 사용될 수 있다.  바람직하게는 이소포론 디이소시아네이트, 헥사메틸렌-1,6-디이소시아네이트, 시클로헥실렌-1,4-디이소시아네이트, 4,4'-메틸렌비스(시클로헥실 이소시아네이트) 등이 사용될 수 있다.  As the isocyanate used in the preparation of the prepolymer, aromatic, aliphatic and alicyclic diisocyanates or mixtures thereof may be used. For example, tolylene-2,4-diisocyanate, tolylene-2,6-diisocyanate, meta-phenylene diisocyanate, biphenylene-4,4'- diisocyanate, methylenebis ((4-phenyl Isocyanate), 4-chloro-1,3-phenylene diisocyanate, naphthalene-1,5-diisocyanate, tetramethylene-1,4-diisocyanate, hexamethylene-1,6-diisocyanate, decamethylene-1, 10-diisocyanate, cyclohexylene-1,4-diisocyanate, methylenebis (4-cyclohexyl isocyanate), tetrahydronaphthylene diisocyanate, isophorone diisocyanate, 4,4'-methylenebis (cyclohexyl isocyanate) Or those selected from the group consisting of two or more of these mixtures may be used. Preferably isophorone diisocyanate, hexamethylene-1,6-diisocyanate, cyclohexylene-1,4-diisocyanate, 4 , 4'-methylenebis (cyclohexyl isocyanate) and the like can be used.
상기 프리폴리머의 제조에 사용되는 폴리올로는 폴리에스터 폴리올 또는 폴리에테르 폴리올을 예로 들 수 있다.  적절한 폴리에스터 폴리올로는 디카르복실산 화합물과 디올 화합물의 축합반응에 의하여 수득되는 것이 바람직하며, 여기에서 디카르복실산 화합물로는 숙신산, 글루타르산, 아디프산, 수베린산, 아젤란 산, 세바스산, 도데칸디카르복실산, 헥사히드로프탈산, 이소프탈산, 테레프탈산, 오르토-프탈산, 테트라클로로프탈산, 1,5-나프탈렌디카르복실산, 푸마르산, 말레인산, 이타콘산, 시트라콘산, 메사콘산, 테트라히드로프탈산 등을 예로 들 수 있으며, 디올 화합물로는 에틸렌글리콜, 프로필렌글리콜, 1,3-프로판디올, 1,3-부탄디올, 1,4-부탄디올, 1.5-펜탄디올, 1,6-헥산디올, 네오펜틸글리콜, 디에틸렌글리콜, 디프로필렌글리콜, 트리에틸렌글리콜, 테트라에틸렌글리콜, 디부틸렌글리콜, 2-메틸-1,3-펜탄디올, 2,2,4-트리메틸-1,3-펜탄디올, 1,4-시클로헥산디메탄올 등을 예로들 수 있다.  또한, 적절한 폴리에테르 폴리올로는 폴리에틸렌글리콜, 폴리프로필렌글리콜, 폴리테트라메틸렌글리콜 등을 예로 들 수 있다.  폴리올의 분자량은 400 내지 10,000으로 다양하나, 적당한 분자량으로는 400 내지 3,000 정도이다.  또한 본 발명에 사용되는 폴리올은 폴리테트라메틸렌에테르 글리콜, 폴리프로필렌 글리콜, 등의 ether계 폴리올으로 이루어진 군으로부터 선택되는 적어도 하나일 수 있다. 본 발명에서 사용하는 폴리올의 분자량은 약 500 내지 4000 일 수 있다. Examples of the polyol used to prepare the prepolymer include polyester polyols and polyether polyols. Suitable polyester polyols are preferably obtained by condensation of a dicarboxylic acid compound with a diol compound, wherein the dicarboxylic acid compound is succinic acid, glutaric acid, adipic acid, subberic acid, azelanic acid. , Sebacic acid, dodecanedicarboxylic acid, hexahydrophthalic acid, isophthalic acid, terephthalic acid, ortho-phthalic acid, tetrachlorophthalic acid, 1,5-naphthalenedicarboxylic acid, fumaric acid, maleic acid, itaconic acid, citraconic acid, mesaconic acid And tetrahydrophthalic acid. Examples of the diol compound include ethylene glycol, propylene glycol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1.5-pentanediol, and 1,6-hexane. Diol, neopentyl glycol, diethylene glycol, dipropylene glycol, triethylene glycol, tetraethylene glycol, dibutylene glycol, 2-methyl-1,3-pentanediol, 2,2,4-trimethyl-1,3- Pentanediol, 1,4-cyclohexanedimethane Or all. Suitable polyether polyols include polyethylene glycol, polypropylene glycol, polytetramethylene glycol, and the like. The molecular weight of the polyols varies from 400 to 10,000, but the suitable molecular weight is about 400 to 3,000. In addition, the polyol used in the present invention may be at least one selected from the group consisting of ether polyols such as polytetramethylene ether glycol, polypropylene glycol, and the like. The molecular weight of the polyol used in the present invention may be about 500 to 4000.
프리폴리머의 자기유화를 위한 이온성 쇄연장제로는 음이온성 쇄연장제와 양이온성 쇄연장제가 사용될 수 있는 데, 음이온성 쇄연장제로는 카르복실기 또는 설포네이트기를 포함하는 화합물이 사용될 수 있으며, 예를 들면, 2,2-디메틸올프로피온산, 2,2-디메틸올부탄온산, 나트륨설포네이트기가 달린 폴리프로필렌 글리콜, 2,4-디아미노-5-메틸벤젠술폰산 등이 사용될 수 있다.  또한, 양이온성 쇄연장제로는 3급 아민 디올(diol) 및 디아민(diamine) 화합물로, 예를 들면 메틸디에탄올아민 등을 사용할 수 있다.  상기 이온성 쇄연장제는 전체 폴리우레탄에 대하여 0.5 내지 25중량%, 바람직하게는 2 내지 7중량%가 포함될 수 있다.  자기유화를 위하여 상기 폴리우레탄의 주쇄 중에 공유결합된 음이온성기 또는 양이온성기를 수분산이 가능하도록하기 위해 이온기를 염(salt)으로 변환시키기는 중화제(neutralizing agents)가 사용된다.  이러한 중화제로는 음이온성일 경우, 수산화나트륨, 수산화칼륨, 수산화리튬, 암모니아, 트리메틸아민, 트리에틸아민, 트리이소프로필아민, 트리부틸아민, N,N-디메틸시클로헥실아민, N,N-디메틸아닐린, N-메틸몰포린, N-메틸피페라진, N-메틸피롤리딘, N-메틸피페리딘 등을 예로 들 수 있으며, 양이온성일 경우에는 인산, 염산, 아세트산, 포름산, 말산 등 산 종류를 사용하게 된다.  이는 상기 이온성기에 대하여 화학양론적으로 80% 이상 사용될 수 있다.  상기 이소시아네이트와 폴리올은 1.1 : 1 내지 4.0 : 1의 비율로 반응되어 폴리이소시아네이트를 형성한다.Anionic chain extenders and cationic chain extenders may be used as the ionic chain extender for self-emulsifying the prepolymer, and as the anionic chain extender, a compound including a carboxyl group or a sulfonate group may be used. , 2,2-dimethylolpropionic acid, 2,2-dimethylolbutanoic acid, polypropylene glycol with sodium sulfonate group, 2,4-diamino-5-methylbenzenesulfonic acid and the like can be used. As the cationic chain extender, tertiary amine diols and diamine compounds, for example, methyl diethanolamine may be used. The ionic chain extender may include 0.5 to 25% by weight, preferably 2 to 7% by weight based on the total polyurethane. Neutralizing agents are used to convert the ionic groups into salts in order to enable the dispersion of the anionic or cationic groups covalently bonded in the main chain of the polyurethane for self-emulsification. Such neutralizing agents include, when anionic, sodium hydroxide, potassium hydroxide, lithium hydroxide, ammonia, trimethylamine, triethylamine, triisopropylamine, tributylamine, N, N-dimethylcyclohexylamine, N, N-dimethylaniline , N-methylmorpholine, N-methylpiperazine, N-methylpyrrolidine, N-methylpiperidine, and the like, and in the case of cationic acid, phosphoric acid, hydrochloric acid, acetic acid, formic acid, malic acid Will be used. It can be used more than 80% stoichiometrically with respect to the ionic group. The isocyanate and polyol are reacted at a ratio of 1.1: 1 to 4.0: 1 to form polyisocyanate.
상기 프리폴리머는 물에 분산된 후, 쇄연장제와의 반응으로 더 고분자화될 수 있다.  상기 쇄연장제로는 폴리아민 및 저급 알코올류로 이루어진 군으로부터 선택되는 적어도 하나를 사용될 수 있다. 상기 폴리아민의 예로는 히드라진, 에틸렌디아민, 피페라진, 디에틸렌트리아민, 트리에틸렌테트라민, 테트라에틸렌펜타민, 펜타에틸렌헥사민, N,N,N-트리스(2-아미노에틸)아민, N-(2-피페라지노에틸)에틸렌디아민, N,N'-비스(2-아미노에틸)피페라진, N,N,N'-트리스(2-아미노에틸)에틸렌디아민, N-[N-(2-아미노에틸)-2-아미노에틸]-N'-(2-아미노에틸)피페라진,N-(2-아미노에틸)-N'-(2-피페라지노에틸)에틸렌디아민, N,N-비스(2-아미노에틸)-N-(2-피페라지노에틸)아민, N,N-비스(2-피페라지노에틸)아민, 구아니딘,멜라민, N-(2-아미노에틸)-1,3-프로판디아민, 3,3'-디아미노벤지딘, 2,4,6-트리아미노피리미딘, 디프로필렌트리아민, 테트라프로필렌펜타민, 트리프로필렌테트라민, N,N-비스(6-아미노헥실)아민, N,N'-비스(3-아미노프로필)에틸렌디아민, 2,4-비스(4'-아미노벤질)아닐린, 1,4-부탄디아민, 1,6-헥산디아민, 1,8-옥탄디아민, 1,10-데칸디아민, 2-메틸펜타메틸렌디아민, 1,12-도데칸디아민, 이소포론디아민(또는 1-아미노-3-아미노메틸-3,5,5-트리메틸-시클로헥산), 비스(4-아미노시클로헥실)메탄(또는 비스(아미노시클로헥산-4-일)-메탄) 등을 예로 들 수 있다.  이때 사용되는 저급 알코올류로서는 에틸렌글리콜(Ethylene Glycol : EG), 프로필렌 글리콜(Propylene Glycol: PG), 디에틸렌 글리콜(Diethylene Glycol : DEG), 디프로필렌 글리콜(Dipropylene Glycol:DPG), 부틸렌글리콜(Butylene Glycol : 1,4BD))등이 있다.The prepolymer may be further polymerized by reaction with a chain extender after it is dispersed in water. As the chain extender, at least one selected from the group consisting of polyamines and lower alcohols may be used. Examples of the polyamine include hydrazine, ethylenediamine, piperazine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, N, N, N-tris (2-aminoethyl) amine, N- (2-piperazinoethyl) ethylenediamine, N, N'-bis (2-aminoethyl) piperazine, N, N, N'-tris (2-aminoethyl) ethylenediamine, N- [N- (2 -Aminoethyl) -2-aminoethyl] -N '-(2-aminoethyl) piperazine, N- (2-aminoethyl) -N'-(2-piperazinoethyl) ethylenediamine, N, N- Bis (2-aminoethyl) -N- (2-piperazinoethyl) amine, N, N-bis (2-piperazinoethyl) amine, guanidine, melamine, N- (2-aminoethyl) -1, 3-propanediamine, 3,3'-diaminobenzidine, 2,4,6-triaminopyrimidine, dipropylenetriamine, tetrapropylenepentamine, tripropylenetetramine, N, N-bis (6-aminohexyl ) Amine, N, N'-bis (3-aminopropyl) ethylenediamine, 2,4-bis (4'-aminobenzyl) aniline, 1,4-part Tandiamine, 1,6-hexanediamine, 1,8-octanediamine, 1,10-decanediamine, 2-methylpentamethylenediamine, 1,12-dodecanediamine, isophoronediamine (or 1-amino-3- Aminomethyl-3,5,5-trimethyl-cyclohexane), bis (4-aminocyclohexyl) methane (or bis (aminocyclohexane-4-yl) -methane) and the like. Lower alcohols used at this time include ethylene glycol (EG), propylene glycol (Propylene Glycol: PG), diethylene glycol (Diethylene Glycol: DEG), dipropylene glycol (DPG), butylene glycol (Butylene) Glycol: 1,4BD)).
상기 분산액은 수성 이온성 친수성 폴리우레탄 분산액으로, 상기 분산액에 점도 조절제를 더 가하여 점도를 조절할 수 있으며, 상기 분산액을 이용하여 건식 방사 공정을 수행함으로써 친환경적이고 인체에 무해한 폴리우레탄 탄성사를 제조할 수 있다. The dispersion is an aqueous ionic hydrophilic polyurethane dispersion, by adding a viscosity modifier to the dispersion to adjust the viscosity, by performing a dry spinning process using the dispersion can be produced an environmentally friendly and harmless polyurethane elastic yarn. .
상기 방법으로 제조된 폴리우레탄 탄성사는 그대로 사용되거나, 폴리아미드 섬유 등에 커버링 되어 스타킹, 타이즈, 양말 등의 얇은 편직물에 적합하게 사용될 수 있다.Polyurethane elastic yarn produced by the above method can be used as it is, or covered with polyamide fibers and the like can be suitably used in thin knitted fabrics such as stockings, tights, socks.
본 발명을 이하 실시예를 통하여 더욱 상세히 설명하며, 다만, 본 발명은 하기 실시예에 한정되는 것은 아니다.The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to the following examples.
[실시예 1]Example 1
4,4‘-메틸렌 디페닐 디이소시아네이트와 폴리테트라메틸렌 에테르 글리콜(분자량 1800)을 반응시켜 제1 예비중합체를 준비하였다.  2,2-디메틸올프로피온산 및 4,4‘-메틸렌 디페닐 디이소시아네이트를 이용하여 제2 예비중합체를 준비하였다.  상기 제1 예비중합체 및 제2 예비중합체를 반응시키고, 쇄연장제로서 에틸렌디아민(EDA)을 사용하여 제3 예비중합체를 제조하였다.  상기 제3 예비중합체를 트리에틸렌테트라민를 첨가하여 2시간 동안 중화시킨 후 탈이온수(Deionized water)를 부가하면서 분산액을 제조하고, 상기 분산액 점도조절제(thickening agent) BYK ®-428 를 가하여 점도를 250 cps(40℃)로 조절하였고, 상기 분산액을 이용하여 건식 공정을 통하여 20데니어 폴리우레탄 탄성사를 제조하였다. 그리고 그 물성을 평가하여 표 1에 나타내었다.The first prepolymer was prepared by reacting 4,4'-methylene diphenyl diisocyanate with polytetramethylene ether glycol (molecular weight 1800). A second prepolymer was prepared using 2,2-dimethylolpropionic acid and 4,4'-methylene diphenyl diisocyanate. The first prepolymer and the second prepolymer were reacted, and a third prepolymer was prepared using ethylenediamine (EDA) as a chain extender. After neutralizing the third prepolymer for 2 hours by adding triethylenetetramine, a dispersion was prepared while adding deionized water, and the dispersion was added with a thickening agent BYK ® -428 to 250 cps. It was adjusted to (40 ℃), and the 20 denier polyurethane elastic yarn was prepared through a dry process using the dispersion. And the physical properties were evaluated and shown in Table 1.
[실시예 2]Example 2
4,4‘-메틸렌 디페닐 디이소시아네이트 대신, 4,4‘-메틸렌 디페닐 디이소시아네이트와 4,4'-디시클로헥실메탄 디이소시아네이트(H12MDI)의 50:50 혼합물을 사용한 것, 분산액의 점도를 110 cps(40℃)로 조절한 것을 제외하고는 실시예 1과 동일한 방법으로 폴리우레탄 탄성사를 제조하였다. 그리고 그 물성을 평가하여 표 1에 나타내었다.Instead of 4,4'-methylene diphenyl diisocyanate, using a 50:50 mixture of 4,4'-methylene diphenyl diisocyanate and 4,4'-dicyclohexylmethane diisocyanate (H12MDI), the viscosity of the dispersion Polyurethane elastic yarn was manufactured in the same manner as in Example 1, except that it was adjusted to 110 cps (40 ° C.). And the physical properties were evaluated and shown in Table 1.
[실시예 3]Example 3
4,4‘-메틸렌 디페닐 디이소시아네이트 대신, 4,4‘-메틸렌 디페닐 디이소시아네이트와 이소포론 디이소시아네이트(IPDI)의 50:50 혼합물을 사용한 것, 쇄연장제로 1,4-부탄디올을 사용한 것, 분산액의 점도를 180 cps(40℃)로 조절한 것을 제외하고는 실시예 1과 동일한 방법으로 폴리우레탄 탄성사를 제조하였다. 그리고 그 물성을 평가하여 표 1에 나타내었다.Using a 50:50 mixture of 4,4'-methylene diphenyl diisocyanate and isophorone diisocyanate (IPDI) instead of 4,4'-methylene diphenyl diisocyanate, using 1,4-butanediol as chain extender , The polyurethane elastic yarn was manufactured in the same manner as in Example 1 except that the viscosity of the dispersion was adjusted to 180 cps (40 ° C.). And the physical properties were evaluated and shown in Table 1.
비교예 1Comparative Example 1
캡핑비(CR) 1.55, 폴리올은 폴리테트라메틸렌에테르 글리콜(분자량 1800)을 사용하였고, 4,4’-디페닐메탄디이소시아네이트를 혼합하여 조제하였다.  사슬연장제로는 에틸렌디아민을, 사슬종결제로는 디에틸아민을 사용하였다.  사슬연장제와 사슬종결제의 비율은 10:1로 하였고, 사용된 아민은 총 농도 7몰%로 조제되었으며, 용매로는 디메틸아세트아마이드를 사용하여 폴리우레탄우레아 방사원액을 얻었다.  위와 같이 수득한 방사 원액을 건식 방사 공정을 통하여 폴리우레탄 탄성사를 제조하였고, 그 물성을 평가하여 표 1에 나타내었다.As a capping ratio (CR) of 1.55 and polyol, polytetramethylene ether glycol (molecular weight 1800) was used, and 4,4'-diphenylmethane diisocyanate was mixed and prepared. Ethylenediamine was used as the chain extender and diethylamine was used as the chain terminator. The ratio of the chain extender to the chain terminator was 10: 1, and the amine used was prepared at a total concentration of 7 mol%, and dimethylacetamide was used as a solvent to obtain a polyurethaneurea spinning stock solution. The spinning stock solution obtained as described above was prepared in a polyurethane elastic yarn through a dry spinning process, and the physical properties thereof are shown in Table 1 below.
인장강도 및 신도의 측정Tensile Strength and Elongation Measurement
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.Using an automatic elongation measuring device (MEL machine, Textechno Co., Ltd.), measure the sample length as 10cm and tensile speed 100cm / min. At this time, the strength and elongation at break are measured, and the load on the yarn (200% modulus) at 200% elongation of the yarn is also measured.
상기 실시예 1 내지 4 및 비교예 1에 있어서 폴리우레탄 탄성사의 분산액 점도, 입자 크기, 특정 와인딩 속도에서의 강도 및 신도 등의 물성을 측정한 결과를 하기 표 1에 표시하였다.In Examples 1 to 4 and Comparative Example 1, the results of measuring physical properties such as dispersion viscosity, particle size, strength and elongation at a specific winding speed of the polyurethane elastic yarn are shown in Table 1 below.
표 1
구분 실시예1 실시예2 실시예3 비교예1
이소시아네이트 4,4-MDI   100% 4,4-MDI   50%H12MDI   50% 4,4-MDI   50%IPDI   50% 4,4-MDI   100%
폴리올 PTMG PTMG PTMG PTMG
쇄연장제 EDA EDA 1,4-Butandiol EDA
분산액 점도(CPS@40℃) 250 110 180 -
입자크기 <60 <40 <100 -
와인딩 속도(m/min) 150 150 150 850
강도(g/De) 12.5 10.5 7.5 1.1
신도(%) 250 340 410 520
Table 1
division Example 1 Example 2 Example 3 Comparative Example 1
Isocyanate 4,4-MDI 100% 4,4-MDI 50% H12MDI 50% 4,4-MDI 50% IPDI 50% 4,4-MDI 100%
Polyol PTMG PTMG PTMG PTMG
Chain extender EDA EDA 1,4-Butandiol EDA
Dispersion Viscosity (CPS @ 40 ℃) 250 110 180 -
Particle size <60 <40 <100 -
Winding speed (m / min) 150 150 150 850
Strength (g / De) 12.5 10.5 7.5 1.1
Elongation (%) 250 340 410 520
상기 표 1을 참조하면, 비교예 1의 기존 유기 용매를 사용하여 제조된 탄성사와 비교하여 다양한 이소시아네이트를 변화하여 유사한 수준의 물성을 나타내는 친환경적 탄성사를 제조할 수 있었다.Referring to Table 1, it was possible to produce an environmentally friendly elastic yarn showing a similar level of physical properties by varying various isocyanates compared to the elastic yarn prepared using the conventional organic solvent of Comparative Example 1.

Claims (8)

  1. 폴리이소시아네이트와, 에스테르 또는 에스테르계 폴리올을 반응시켜 제1 예비중합체를 제조하는 단계;Reacting the polyisocyanate with an ester or ester polyol to prepare a first prepolymer;
    -COOH 또는 -SO3H를 포함하는 2관능성 또는 다관능성 알코올과, 이소시아네이트를 반응시켜 제2 예비중합체를 제조하는 단계;Reacting an isocyanate with a bifunctional or polyfunctional alcohol comprising —COOH or —SO 3 H, to prepare a second prepolymer;
    상기 제1 예비중합체 및 제2 예비중합체의 반응 생성물을 쇄연장 반응시켜 제3 예비중합체를 제조하는 단계; 및Preparing a third prepolymer by chain-extending the reaction product of the first prepolymer and the second prepolymer; And
    상기 제3 예비중합체를 중화시켜 분산액을 제조하는 단계를 포함하는, 폴리우레탄 탄성사의 제조방법.Neutralizing the third prepolymer, thereby preparing a dispersion.
  2. 제1항에 있어서,The method of claim 1,
    상기 폴리이소시아네이트는 4,4’-디페닐메탄디이소시아네이트, 2,4’-디페닐메탄디이소시아네이트 1,5’-나프탈렌디이소시아네이트, 1,4’-페닐렌디이소시아네이트, 헥사메틸렌 디이소시아네이트, 1,4’-시클로헥산디이소시아네이트, 4,4’-디시클로헥실메탄디이소시아네이트, 또는 이소포론디이소시아네이트 이루어진 군으로부터 선택되는 적어도 하나인 것을 특징으로 하는, 폴리우레탄 탄성사의 제조방법.The polyisocyanate is 4,4'-diphenylmethane diisocyanate, 2,4'-diphenylmethane diisocyanate 1,5'-naphthalene diisocyanate, 1,4'-phenylene diisocyanate, hexamethylene diisocyanate, 1, At least one selected from the group consisting of 4'-cyclohexane diisocyanate, 4,4'- dicyclohexyl methane diisocyanate, or isophorone diisocyanate.
  3. 제1항에 있어서,The method of claim 1,
    상기 폴리올은 디카르복실산 화합물과 디올 화합물의 축합반응에 의하여 수득된 폴리올, 폴리에틸렌글리콜, 폴리프로필렌글리콜 및 폴리테트라메틸렌글리콜로 이루어진 군으로부터 선택되는 적어도 하나인 것을 특징으로 하는, 폴리우레탄 탄성사의 제조방법.The polyol is at least one selected from the group consisting of polyol, polyethylene glycol, polypropylene glycol and polytetramethylene glycol obtained by the condensation reaction of a dicarboxylic acid compound and a diol compound, the production of polyurethane elastic yarn Way.
  4. 제1항에 있어서,The method of claim 1,
    상기 쇄연장 반응에 있어서 쇄연장제로 폴리아민 및 저급 알코올류로 이루어진 군으로부터 선택된 적어도 하나를 사용하고, 상기 폴리아민으로는 에틸렌디아민, 1,2-디아미노프로판, 1,3-디아미노프로판, 1,4-디아미노부탄, 2,3-디아미노부탄, 1,5-디아미노펜탄, 1,6-헥사메틸렌디아민 및 1,4-씨클로헥산디아민으로 이루어진 군으로부터 선택된 적어도 하나, 저급 알코올류로는 에틸렌글리콜(Ethylene Glycol : EG), 프로필렌 글리콜(Propylene Glycol: PG), 디에틸렌 글리콜(Diethylene Glycol : DEG), 디프로필렌 글리콜(Dipropylene Glycol:DPG) 및 부틸렌글리콜(Butylene Glycol : 1,4BD))로 이루어진 군으로부터 선택되는 적어도 하나인 것을 특징으로 하는, 폴리우레탄 탄성사의 제조방법.In the chain extension reaction, at least one selected from the group consisting of polyamines and lower alcohols is used as a chain extender, and as the polyamine, ethylenediamine, 1,2-diaminopropane, 1,3-diaminopropane, 1, At least one lower alcohol selected from the group consisting of 4-diaminobutane, 2,3-diaminobutane, 1,5-diaminopentane, 1,6-hexamethylenediamine and 1,4-cyclochlorodiamine Ethylene Glycol (EG), Propylene Glycol (PG), Diethylene Glycol (DEG), Dipropylene Glycol (DPG) and Butylene Glycol (1,4BD) At least one selected from the group consisting of, Polyurethane elastic yarn manufacturing method.
  5. 제1항에 있어서,The method of claim 1,
    상기 분산액은 수성 이온성 친수성 폴리우레탄 분산액인 것을 특징으로 하는, 폴리우레탄 탄성사의 제조방법.The dispersion is a method of producing a polyurethane elastic yarn, characterized in that the aqueous ionic hydrophilic polyurethane dispersion.
  6. 제1항에 있어서,The method of claim 1,
    상기 분산액에 점도 조절제를 더 가하는 것을 특징으로 하는, 폴리우레탄 탄성사의 제조방법.Method for producing a polyurethane elastic yarn, characterized in that further adding a viscosity modifier to the dispersion.
  7. 제1항에 있어서,The method of claim 1,
    상기 분산액을 이용하여 건식 방사 공정을 수행하는 것을 특징으로 하는, 폴리우레탄 탄성사의 제조방법.Method for producing a polyurethane elastic yarn, characterized in that to perform a dry spinning process using the dispersion.
  8. 제1항 내지 제7항 중 어느 한 항의 방법으로 제조된 폴리우레탄 탄성사.Polyurethane elastic yarn produced by the method of any one of claims 1 to 7.
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