KR970010727B1 - Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property - Google Patents

Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property Download PDF

Info

Publication number
KR970010727B1
KR970010727B1 KR1019940038735A KR19940038735A KR970010727B1 KR 970010727 B1 KR970010727 B1 KR 970010727B1 KR 1019940038735 A KR1019940038735 A KR 1019940038735A KR 19940038735 A KR19940038735 A KR 19940038735A KR 970010727 B1 KR970010727 B1 KR 970010727B1
Authority
KR
South Korea
Prior art keywords
compound
mol
polymer
molecular weight
diisocyanate
Prior art date
Application number
KR1019940038735A
Other languages
Korean (ko)
Other versions
KR960023324A (en
Inventor
임대우
이재철
이흥우
연원희
기영철
임태환
한영화
김영길
Original Assignee
제일합섬 주식회사
박홍기
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 제일합섬 주식회사, 박홍기 filed Critical 제일합섬 주식회사
Priority to KR1019940038735A priority Critical patent/KR970010727B1/en
Publication of KR960023324A publication Critical patent/KR960023324A/en
Application granted granted Critical
Publication of KR970010727B1 publication Critical patent/KR970010727B1/en

Links

Classifications

    • 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
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • 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
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/07Addition of substances to the spinning solution or to the melt for making fire- or flame-proof filaments
    • 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
    • D02YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
    • D02GCRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
    • D02G3/00Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
    • D02G3/22Yarns or threads characterised by constructional features, e.g. blending, filament/fibre
    • D02G3/32Elastic yarns or threads ; Production of plied or cored yarns, one of which is elastic
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Artificial Filaments (AREA)

Abstract

A diol compound 1 mole consisting of 90-95 mole % of a high molecula weight diol and of 5-10 mole % of a low molecular weight diol is preliminary polymerized with a diisocyanate compound in the ratio of 1.25-2.5 mol, and is mixed with a solvent for producing the solution of the preliminary polymer. Then using the preliminary polymer in the ratio of 60-98 mole %, subjecting an isocyanate of its tip to the chain growth, a diamine compound is obtained in a viscosity of 500-4,000 poise suitable for spinning, having a monoamine compound chain stopped using a diamine compound in the ratio of 1-30 mole % from among the total amount.

Description

내열성 및 내염소성이 우수한 폴리우레탄계 탄성섬유의 제조방법.Method for producing a polyurethane-based elastic fiber excellent in heat resistance and chlorine resistance.

본 발명은 탄성섬유의 고유한 물성을 유지하면서도 제반물성이 우수한 폴리우레탄계 탄성섬유의 제조방법에 관한 것이다.The present invention relates to a method for producing a polyurethane-based elastic fiber having excellent physical properties while maintaining the inherent physical properties of the elastic fiber.

폴리우레탄계 탄성섬유는 탄성과 탄성회복력이 우수하여 스타킹이나 여성용 속옷류 및 수영복등의 신축성직물에 많이 이용되고 있다. 그러나, 폴리우레탄계 탄성섬유의 경우 내광성이 취약하여 햇빛에 노출시 변색되는 단점을 가지고 있으며, 대기중의 NOx가스 및 산소등에 의해 산화반응이 일어나서 탄성섬유의 고유물성인 탄력성이 감소하게 되는 단점이 있었다. 특히, 대기중에시의 변색현상 및 탄력성 감소현상은 탄성사를 다량 함유하는 스타킹등의 경우와 같이 외부노출 부분으로 사용시 급격하게 나타난다.Polyurethane-based elastic fibers are excellent in elasticity and elastic recovery power is widely used in stretch fabrics, such as stockings, women's underwear and swimwear. However, polyurethane-based elastic fibers have a disadvantage in that they are discolored when exposed to sunlight due to poor light resistance, and the elasticity, which is inherent in elastic fibers, is reduced due to oxidation reaction caused by NO x gas and oxygen in the atmosphere. there was. In particular, the phenomenon of discoloration and decrease in elasticity in the air occurs rapidly when used as an external exposure part, as in the case of stockings containing a large amount of elastic yarn.

또한, 내열성이 취약하여 폴리에스테르 섬유등 타소재와 혼방하여 사용시 130℃정도의 고온염색이 불가능하여 용도에 제한이 따른다. 뿐만아니라, 폴리우레탄계 탄성섬유틀 수영복으로 적용시 수영장 물속에 포함된 염소에 의해 손상되어 섬유의 강도가 저하되고 변색현상이 발생하는등 각종 문제가 야기되고 있다.In addition, the heat resistance is poor, when blended with other materials such as polyester fiber, when used at high temperature of about 130 ℃ is impossible due to restrictions on use. In addition, when applied as a polyurethane-based elastic fiber swimsuit, various problems are caused, such as damage to the chlorine contained in the pool water to reduce the strength of the fiber and discoloration phenomenon.

상술한 문제점중 산화방지롤 위해서는 일본특개평 1-204920호에 기재된 바와 같이 수소화 m-페닐렌디아민(HmPD)과 수소화 p-페닐렌디아민(HpPD) 및 테트라클로로-p-자이렌디아민을 40/40/20의 비율로 사용하여 제조한 폴리알켄에테르글리콜과 t-알킬디이소시아네이트(TMXDI)를 반응시켜 얻은 예비 중합물에 산화방지제로서 1,1비스(2-메틸-4-히드록시-5-t-부틸페놀)부탄올을 중합체 중량의 1% 정도를 투입하는 방법, 일본특개소 63-126915호에 기재된 바와 같이 페놀류의 산화방지제를 투입하는 방법, 일본특개소 60-21187호에 기재된 바와 같이 힌더스아민계 화합물을 중합물의 0.3∼10중량% 첨가하여 신화방지성능을 향상시키는 방법과 미국특허 제4548975호에 기재된 바와 같이 2,4,6-트리(2,6-디메틸-4-t-부틸-3-히드록시벤질)이소시누레이트(상품명 아녹스 1790) 또는 p-크레졸, 디사이클로펜타디엔 및 이소부탄 응측물(윙스테이-L)을 사용하는 방법등이 공지되어 있다.Among the above-mentioned problems, for the antioxidant roll, hydrogenated m-phenylenediamine (HmPD), hydrogenated p-phenylenediamine (HpPD) and tetrachloro-p-xylenediamine as described in Japanese Patent Application Laid-Open No. 1-204920 are used. 1,1bis (2-methyl-4-hydroxy-5-t) as an antioxidant to a prepolymer obtained by reacting polyalkeneetherglycol prepared at a ratio of 40/20 with t-alkyl diisocyanate (TMXDI). -Butylphenol) butanol A method of adding about 1% of the weight of the polymer, a method of adding an antioxidant of phenols as described in Japanese Patent Application Laid-Open No. 63-126915, as described in Japanese Patent Application Laid-Open No. 60-21187 A method for improving the anti-myxing performance by adding 0.3 to 10% by weight of an amine compound and 2,4,6-tri (2,6-dimethyl-4-t-butyl- as described in U.S. Pat. 3-hydroxybenzyl) isocinurate (tradename Anox 1790) or p-cresol, Methods of using dicyclopentadiene and isobutane condensate (wingstay-L) and the like are known.

또한, 일본특개소 61-47749호에 언급된 안정제를 사용하는 방법 즉, 3관능성 페놀 화합물과 유기 디이소시아네이트로부터 합성한 폴리우레탄계 화합물의 1그램중에 1×10-4몰 이상의 하이드록시기를 가진 분자량 1,000∼50,000의 범위의 안정제를 첨가하는 방법이 공지되어 있다. 그리나, 상술한 방법들은 산화방지성은 다소간 향상되나 만족스러운 수준이 아니며, 폴리우레탄 섬유의 고유한 물성인 탄성율파 탄성회복율을 저하시키는 결점을 지니고 있다.In addition, the method using the stabilizer mentioned in Japanese Patent Laid-Open No. 61-47749, that is, a molecular weight having a hydroxyl group of 1 × 10 -4 mol or more in 1 gram of a polyurethane-based compound synthesized from a trifunctional phenol compound and an organic diisocyanate It is known to add stabilizers in the range of 1,000 to 50,000. However, the above-mentioned methods are somewhat improved but not satisfactory oxidation resistance, and has the drawback of lowering the elastic modulus and elastic recovery rate, which is the inherent properties of polyurethane fibers.

또한, 내광성을 향상시키기 위해서는 일본특개소 61-47819호에 기재된 바와 같이 페놀계 화합물을 0.1∼10중량% 함유시킴으로서 일광견뢰도를 향상시키는 방법, 일본특개소 57-176260호에 기재된 바와 같이 염소계 표백제를 사용하여 변색방지성을 향상시키는 방법, 미국특허 제5081258호에 지재된 바와 같이 비스벤조트리아졸우레아계 화합물을 사용하여 광안정성을 향상시키는 방법과 일본특개소56-11948호에 기재된 바와 같이 폴리우레탄 중합체에 페놀계 화합물을 0.1∼10중량% 투입하여 일광견뢰도를 향상시키는 방법이 알려져 있다.In addition, in order to improve light resistance, a method of improving daylight fastness by containing 0.1 to 10% by weight of a phenolic compound as described in Japanese Patent Laid-Open No. 61-47819, and a chlorine bleach as described in Japanese Patent Laid-Open No. 57-176260 Method for improving the discoloration resistance by using a method of improving photostability using a bisbenzotriazole urea-based compound as described in US Pat. No. 5,258,582 and polyurethane as described in Japanese Patent Application Laid-Open No. 56-11948. It is known to add 0.1 to 10% by weight of a phenolic compound into the polymer to improve daylight fastness.

그리고, 일본특개평 5-5217호에는 알로파네이트 결합을 가진 폴리에테르계 폴리우레탄과 알로파네이트결합을 가지지 않는 폴리에테르계 또는 폴리카보네이트계 폴리우레탄을 복합방사하는 방법이 기재되어 있으나, 복합방사 공정을 행하여야 하는 등의 제조상의 각종 문제를 안고 있다.Japanese Patent Laid-Open No. 5-5217 discloses a method of composite spinning a polyether-based polyurethane having an allophanate bond and a polyether-based or polycarbonate-based polyurethane having no allophanate bond. There are various manufacturing problems, such as the need to perform a process.

뿐만아니라, 내열성을 향상시키기 위해서는 내열성 향상제를 투입하거나, 고분자 디올화합물의 일부분을 에틸렌글리콜, 디에틸렌글리콜, 프로필렌글리콜, 1,4-부탄디올등의 저분자량 디올화합물로 대체하는 방법이 공지되어있으며, 일본특공평4-74457호에는 폴리테트라메틸렌글리콜을 과잉의 4,4'-디페닐메탄디이소시아네이트와 반응시킨 후 1,2-프로필렌디아민과 디에틸렌아민으로 쇄성장시킨 폴리머를 방사하여 제조한 탄성사를 일정함 온도에서 가열처리하여 탄성회복을 향상시키는 방법이 기재되어 있으나, 이러한 방법으로 제조시에는 탄성사의 가열처리 공정이 추가됨으로써 작업이 어려울 뿐만아니라 내열성의 향상정도가 미미하였다.In addition, in order to improve the heat resistance, a method of adding a heat resistance enhancer or replacing a portion of the polymer diol compound with a low molecular weight diol compound such as ethylene glycol, diethylene glycol, propylene glycol, 1,4-butanediol, and the like is known. Japanese Unexamined Patent Publication No. 4-74457 discloses an elastic yarn prepared by reacting polytetramethylene glycol with an excess of 4,4'-diphenylmethane diisocyanate and spinning a polymer chain-grown with 1,2-propylenediamine and diethyleneamine. The method of improving the elastic recovery by heating at a constant temperature is described, but the manufacturing process by this method is not only difficult to work due to the addition of the heat treatment process of the elastic yarn, the degree of improvement of heat resistance was insignificant.

내염소성을 향상시키기 위한 방법으로는 일본특개소 60-36560호에 기재된 바와 같이 폴리테트라메틸렌글리콜과 과잉의 4,4'-디페닐메탄디이소시아네이트를 예비중합후 아민으로 쇄연장 및 쇄정지시킨 후 이 중합물에 제 3 급 질소함유 우레탄 폴리머를 첨가함으로써 내염소성을 향상시키는 방법, 일본특개소 56-107010호에 언급된 바와 같이 폴리에스테르글리콜과 4,4'-디페닐메탄디이소시아네이트를 예비중합후 아민을 사용하여 쇄연장시켜서 일정한 점도의 폴리머를 제조후 방사전에 지방산 금속계 화합물을 첨가시킴으로시 내염소성을 증가시키는 방법, 미국특허 제4,837,292호에 언급된 바와 같이 폴리(펜타-1,5-카보네이트)디올과 폴리(헥산-l,6-카보네이트)디올의 혼합물로서 합성한 특별한 폴리카보네이트 소프트세그먼트를 함유한 폴리우레탄 중합물을 합성함으로써 내염소성을 향상시키는 방법, 일본특개소 57-29609호에 언급된 바와 같이 폴리테트라메틸렌에테르글리콜과 p,p'-메틸렌디페닐디이소시아네이트를 반응시킨 후 디에틸아민과 에틸렌디아민 및 1, 3-사이클로헥실렌디아민을 사용하여 쇄연장을 시킨 중합물에 평균입경 0.01∼1마이크로의 산화아연을 1∼3중량% 사용하여 내염소성을 부여하는 방법, 일본특개소 62-574호에 언급된 바와 같이 폴리테트라메틸렌글리콜과 4,4'-디페닐메탄디이소시아네이트를 반응시켜시 예비중합물을 얻은 후 1,2-프로필렌디아민을 첨가하여 쇄연장을 시킨 후 모노에탄올아민을 가하여 중합을 완료후 디비닐벤젠과 메틸기 또는 에틸기를 치환기로 가진 페놀을 부가중합하며 얻은 고분자형 산화방제를 첨가하며 내염소성과 내광성을 부여하는 방법등이 있다.As a method for improving chlorine resistance, polytetramethylene glycol and excess 4,4'-diphenylmethane diisocyanate are prepolymerized as described in Japanese Patent Application Laid-Open No. 60-36560, followed by chain extension and chain stop with amine. Method for improving chlorine resistance by adding a tertiary nitrogen-containing urethane polymer to the polymer, after prepolymerization of polyester glycol and 4,4'-diphenylmethane diisocyanate as mentioned in Japanese Patent Laid-Open No. 56-107010 A method of increasing the chlorine resistance by adding a fatty acid metal compound before spinning after producing a polymer having a constant viscosity by chain extension using an amine, as described in US Pat. No. 4,837,292. Polyurethane polymer containing a special polycarbonate soft segment synthesized as a mixture of diol and poly (hexane-l, 6-carbonate) diol. Method for improving chlorine resistance by synthesizing, as mentioned in Japanese Patent Laid-Open No. 57-29609, after reacting polytetramethylene ether glycol with p, p'-methylenediphenyl diisocyanate, diethylamine and ethylenediamine and 1, A method of imparting chlorine resistance to a polymer obtained by chain extension using 3-cyclohexylenediamine using 1 to 3% by weight of zinc oxide having an average particle diameter of 0.01 to 1 micro, as mentioned in Japanese Patent Laid-Open No. 62-574. Likewise, when polytetramethylene glycol is reacted with 4,4'-diphenylmethane diisocyanate to obtain a prepolymer, 1,2-propylenediamine is added for chain extension, and monoethanolamine is added to complete the polymerization. There is a method of adding chlorine resistance and light resistance by adding a polymer type oxidation inhibitor obtained by addition polymerization of phenol having a benzene and a methyl group or an ethyl group as a substituent.

그러나, 상기의 방법들로 제조한 폴리우레탄 탄성체의 경우 내염소성을 다소간 향상시키거나 만족스러운 수준이 아니고 폴리우레탄 탄성체의 고유한 물성인 탄성회복율을 저하시키거나 또는 강도저하를 초래하는 문제점이 있었다.However, in the case of the polyurethane elastomer produced by the above methods, there is a problem that the chlorine resistance is somewhat improved or not satisfactory, and the elastic recovery rate, which is inherent in the polyurethane elastomer, is reduced or the strength is decreased.

따라서, 본 발명의 목적은 상기의 제반결점을 해소하여 폴리우레탄 탄성섬유의 고유한 물성을 유지하면서도 내열성 및 내염소성이 우수한 폴리우레탄 탄성섬유의 제조방법을 제공하는데 있다.Accordingly, an object of the present invention is to provide a method for producing a polyurethane elastic fiber excellent in heat resistance and chlorine resistance while maintaining the inherent physical properties of the polyurethane elastic fiber by eliminating the above-mentioned drawbacks.

상기한 목적뿐만아니라 용이하게 표출되는 또 다른 목적을 달성하기 위하여 본 발명에서는 수평균 분자량1,000∼3,000의 고분자량 디올과 수평균 분자량 50∼500의 저분자량 디올을 과입의 디이소시아네이트와 예비중합하고 용제와 일정비율로 혼합하여 예비중합물의 용액을 제조한 후, 말단의 이소시아네이트를 디아민 화합물을 적당량 사용하여 쇄성장시켜 방사에 적당한 점도를 얻은 다음, 모노아민 화합물을 사용하여 말단을 봉쇄시킨 후, 내열성 향상기능을 갖는 화합물과 내염소성 화합물을 첨가함으로서 탄성사의 고유한 물성을 유지하면서도 내열성 및 내염소성을 현저히 향상시킨 폴리우레탄계 탄성섬유를 얻을 수 있었다.In order to achieve the above object as well as another easily expressed object, in the present invention, a high molecular weight diol having a number average molecular weight of 1,000 to 3,000 and a low molecular weight diol having a number average molecular weight of 50 to 500 is prepolymerized with a diisocyanate of a charge and a solvent. After mixing in a constant ratio to prepare a solution of the prepolymer, the terminal isocyanate is chain-grown using an appropriate amount of diamine compound to obtain a suitable viscosity for spinning, and then the terminal is blocked using a monoamine compound to improve heat resistance. By adding a compound having a function and a chlorine resistant compound, it was possible to obtain a polyurethane-based elastic fiber that significantly improved heat resistance and chlorine resistance while maintaining the inherent physical properties of the elastic yarn.

본 발명을 더욱 상세히 설명하면 다음과 같다.The present invention is described in more detail as follows.

수평균 분자량 1,000∼3,000의 고분자량 디올화합물 90∼95몰%와 수평균분자량 50∼500의 저분자량 디올화합물 5∼10몰%로 구성되는 디올화합물 l몰에 대하여 디이소시아네이트 화합물 1.25∼2.5몰 비율로 예비중합후 용제를 적당량 혼합하여 예비중합물의 용액을 제조한 후, 디아민 화합물을 예비중합물의 60∼98몰% 사용하여 말단의 이소시아네이트를 쇄성장시켜서 방사에 적당한 점도인 500∼4,000포이즈(poise)가 되도록한 다음, 모노아민 화합물을 쇄성장제인 디아민 화합물 사용량의 1∼30몰% 사용하며 쇄정지를 시킨 후, 접도안정제를 사용하여 방사에 적당한 점도를 유지하면서 내열성 향상첨가제를 폴리머 고형분에 대하여 0.01∼1중량%에 첨가하고, 내염소성 향상제를 폴리머 고형분에 내하여 0.01∼3중량% 첨가하여 중합물을 얻고, 이를 방사하므로서 탄성 중합체의 고유한 물성을 유지하면서도 내열성과 내염소성을 현저히 향상시킨 탄성섬유를 제조하였다.Diisocyanate compound 1.25-2.5 molar ratio with respect to 1 mol of diol compounds which consist of 90-95 mol% of high molecular weight diol compounds of the number average molecular weight 1,000-3,000, and 5-10 mol% of the low molecular weight diol compounds of the number average molecular weight 50-500. After prepolymerization, a suitable amount of the solvent was mixed to prepare a solution of the prepolymer, and then a terminal isocyanate was chain-grown using 60 to 98 mol% of the diamine compound to produce a 500 to 4,000 poise having a viscosity suitable for spinning. Then, the monoamine compound was used for 1-30 mol% of the diamine compound used as the chain growth agent and the chain was stopped. Then, the heat resistance improving additive was added with respect to the polymer solids while maintaining the viscosity suitable for spinning using the anti-corrosive stabilizer. It is added to -1% by weight, and the chlorine resistance enhancer is added to the polymer solids to add 0.01 to 3% by weight to obtain a polymer, which is spun in elasticity. While maintaining the inherent physical properties of the material it was produced elastic fibers which significantly improves the heat-resistance and chlorine resistance.

탄성중합체중 소프트세그먼트(soft segment)의 역할을 하는 고분자량의 디올화합물로서는 폴리옥시프로필렌글리콜, 폴리옥시에틸렌글리콜, 폴리옥시테트라메틸렌글리콜, 폴리옥시펜타메틸렌글리콜등의 폴리에스테르화합물, 폴리에틸렌아디페이트, 폴리부틸렌아디페이트, 폴리네오펜칠아디페이트, 폴리헥사메틸렌아디페이트, 폴리카프로락튼등의 폴리에스테르계 화합물, 폴리부틸렌카보네이트, 폴리헥사메닐렌카보네이트 등의 폴리카보네이트 화합물 모두가 사용이 가능하지만, 폴리에테르계 화합물이 폴리테트라메틸렌에테르글리콜 화합물이 탄성체의 물성을 고려시 가장 바람직하다.Examples of high molecular weight diol compounds that act as soft segments in elastomers include polyester compounds such as polyoxypropylene glycol, polyoxyethylene glycol, polyoxytetramethylene glycol, polyoxypentamethylene glycol, polyethylene adipate, Although polyester-based compounds, such as polybutylene adipate, poly neopentyl adipate, polyhexamethylene adipate, and polycaprolacton, polycarbonate compounds, such as polybutylene carbonate and polyhexamenylene carbonate, can all be used, The polyether compound is most preferably the polytetramethylene ether glycol compound in consideration of the physical properties of the elastomer.

또한, 본 발명에 사용되는 고분자량 디올화합물은 수평균 분자량 1,000∼3,000의 화합물이 바람직하며, 수평군 분자량 1,500∼2,500의 화합물이 특히 바람직하다.In addition, the high molecular weight diol compound used in the present invention is preferably a compound having a number average molecular weight of 1,000 to 3,000, and particularly preferably a compound having a horizontal group molecular weight of 1,500 to 2,500.

한편, 내열성을 향상시키기 위하여 사용되는 저분자량의 디올화합물로서는 에틸렌글리콜, 디에틸렌클리클, 프로필렌글리콜, 디프로필렌글리콜, 1,4-부탄디올등의 화합물이 있는데, 폴리우레탄 중합체의 가교도를 증가시켜서 내열성을 부여하기 위해서는 분자량 50∼500의 글리클 화합물이 가장 좋다.On the other hand, low molecular weight diol compounds used to improve heat resistance include compounds such as ethylene glycol, diethylene clecle, propylene glycol, dipropylene glycol, 1,4-butanediol, and heat resistance by increasing the degree of crosslinking of the polyurethane polymer. In order to impart the most, a glycle compound having a molecular weight of 50 to 500 is the best.

고분자량 디올화합물과 저분자량이 디올화합물의 전체 사용량은 디이소시아네이트 화합물에 대하여 40∼80몰%가 적당하며, 40몰%미만에서는 중합물의 강도는 향상되나 신도 및 탄성회복율이 저하되어 탄성중합체로서의 고유한 물성의 저하를 초래하여 80몰%를 초과하여 사용시는 신도와 탄성회복율은 향상되나 강도가 저하되어 탄성섬유의 사용에 제약을 받는다.The total amount of the high molecular weight diol compound and the low molecular weight diol compound is 40 to 80 mole% with respect to the diisocyanate compound, and below 40 mole%, the strength of the polymer is improved, but the elongation and elastic recovery rate are lowered, thereby inherent as an elastomer. When it is used in excess of 80 mol%, the elongation and elastic recovery rate are improved, but the strength is lowered and the use of elastic fibers is restricted.

또한, 고분자량 디올화합물(A)과 저분자량 디올화합물(B)의 사용몰비 A/B는 1∼20이 적당하며, 1미만에서는 탄성섬유로서의 고유한 물성의 저하를 초래하고 20을 초과하면 내열성의 향상정도가 미미하다.In addition, the molar ratio A / B of the high molecular weight diol compound (A) and the low molecular weight diol compound (B) is suitably in the range of 1 to 20. If the molar ratio is less than 1, the intrinsic physical properties of the elastic fiber are lowered. The degree of improvement is minimal.

쇄성장제인 아민화합물과 결합하여 하드세그먼트(Hard Segment)의 역할을 하는 디미소시아네이트 화합물로서는 p-페닐디이소시아네이트, m-페닐렌디이소시아네이트, 2,4 트리렌디이소시아네이트, 2,6-토리렌디이소시아네이트, 1 클로로 1,2 페닐렌디이소시아네이트, 1,5 나프탈렌디이소시아네이트, 1,4 페닐렌디이소시아네이트, 클로로페닐렌, 2,4' 디이소시아네이트, 메틸렌비스 4. 페닐디이소시아네이트, 헥사메틸렌디이소시아네이트, 폴리메틸렌폴리페닐디이소시아네이트, 메틸사이클로헥시렌 디이소시아네이트, 파라페닐디이소시아네이트, 파라페닐렌 디이소시아네이트, 4,4' 디페닐 이소프로필리딘 디이소시아네이트, 3,3' 디메틸 4,4' 디페닐디이소시아네이트, 3,3' 디메톡시 4,4' 디페닐 디이소시아네이트, 4,4'디페닐메탄디이소시아네이트 등의 화합물이 있는데, 디올 화합물과의 반응성과 탄성체의 물성을 고려시 4,4' 디페닐메탄 디이소시아네이트 화합물이 가장 바람직하다.Examples of dimisocyanate compounds which combine with an amine compound which is a chain growth agent and act as a hard segment include p-phenyl diisocyanate, m-phenylene diisocyanate, 2,4 trienedi isocyanate and 2,6-torylene diisocyanate. , 1 chloro 1,2 phenylene diisocyanate, 1,5 naphthalene diisocyanate, 1,4 phenylene diisocyanate, chlorophenylene, 2,4 'diisocyanate, methylene bis 4. phenyl diisocyanate, hexamethylene diisocyanate, polymethylene Polyphenyl diisocyanate, methylcyclohexylene diisocyanate, paraphenyl diisocyanate, paraphenylene diisocyanate, 4,4 'diphenyl isopropylidine diisocyanate, 3,3' dimethyl 4,4 'diphenyl diisocyanate, 3 , 3 'dimethoxy 4,4' diphenyl diisocyanate, and 4,4 'diphenylmethane diisocyanate. The 4,4 'diphenylmethane diisocyanate compound is most preferred in consideration of the reactivity with the diol compound and the physical properties of the elastomer.

디이소시아네이트 화합물의 사용량은 디올화합물 1몰에 대하여 1.25∼2.5몰이 적당하며, 1.25몰 미만에서는 중합물의 신도는 우수하나, 강도가 저하되고 탄성회복력이 부족하고, 2.5몰을 초과하여 사용시는 강도와 탄성회복은 우수하나 신도가 불량하여 탄성중합체로서의 고유한 물성의 저하를 초래한다.Suitable amount of diisocyanate compound is 1.25 to 2.5 moles per 1 mole of diol compound, and less than 1.25 moles of polymer is excellent in elongation, but its strength is low and its elastic recovery ability is insufficient. The recovery is good but the elongation is poor resulting in the inherent degradation of physical properties as an elastomer.

디올화합물과 디이소시아네이트 화합물이 결합된 예비중합물은 디아민 화합물에 의해 쇄성장되며, 일정한분자량으로 쇄성장시킨 후 모노아민으로 쇄정지를 시킴으로서 적당한 분자량의 중합물을 얻을 수 있다. 예비중합물을 쇄성장시키는 디아민 화합물로서는 1,2 프로필렌디아민, 2,3 부틸렌디아민, 메틸이미노 비스프로필아민, 메타자이렌디아민, 2,5 디메틸피페라진, 2 메틸퍼페라진, 에틸렌디아민, 에타놀디아민, 테트라메틸렌디아민, 펜타메틸렌디아민, 헥사메틸렌디아민, 1 메틸 2,4 디아민벤젠, 1,2 사이크롤헥사디아민, 옥타메틸렌디아민, 파라페닐렌디아민등의 화합물이 사용된다.The prepolymer obtained by combining the diol compound and the diisocyanate compound is chain-grown by the diamine compound, and chain-grown at a constant molecular weight, followed by chain stopping with monoamine, thereby obtaining a polymer having an appropriate molecular weight. Examples of the diamine compound for chain-growing the prepolymer include 1,2 propylenediamine, 2,3 butylenediamine, methylimino bispropylamine, metaxylenediamine, 2,5 dimethylpiperazine, 2 methylperazine, ethylenediamine, Compounds such as ethanoldiamine, tetramethylenediamine, pentamethylenediamine, hexamethylenediamine, 1 methyl 2,4 diaminebenzene, 1,2 cyclohexadiamine, octamethylenediamine, paraphenylenediamine and the like are used.

그러나, 쇄성장 화합물중 중합물의 점도 안정성과 방사후 탄성사의 물성을 향상시키기 위해서는 선형디아민과 환형디아민을 적정비율로 혼합하여 사용하여 한다. 선형 디아민(C)과 환형디아민(D)의 사용몰비 C/D는 2∼20범위가 적당하며, C/D를 2미만으로 할 경우는 반응성이 불량하여 저분자량의 폴리머가 생상되므로 강도, 신도등 기계적인 물성의 저하를 초래하고, C/D가 20을 초과할 경우에는 반응속도가 지나치게 발라서 부반응물이 다량으로 발생되어 폴리머의 안정성이 저하되고 내열성도 저하된다.However, in order to improve the viscosity stability of the polymer in the chain growth compound and the properties of the elastic yarn after spinning, a mixture of linear diamines and cyclic diamines is used in an appropriate ratio. The molar ratio C / D of the linear diamine (C) and the cyclic diamine (D) is in the range of 2 to 20, and when the C / D is less than 2, the reactivity is poor and a low molecular weight polymer is produced, resulting in high strength and elongation. When mechanical properties are lowered, and the C / D exceeds 20, the reaction rate is excessively applied to generate a large amount of side reactions, thereby degrading the stability of the polymer and lowering the heat resistance.

반응속도를 적당히 유지하고 폴리머의 점도 안정성을 유지하며 방사한 탄성사의 기계적인 물성저하를 방지하기 위해서는 선형디아민으로서는 에틸렌디아민과 1,2-프로필렌디아민을 적당량 혼합하여 사용하는 것이 가장 좋고 환형디아민으로서는 메타자이렌디아민과 1,4-사이클로헥산디아민을 혼합하여 사용하는 것이 가장 좋다.In order to maintain the reaction speed moderately, maintain the viscosity stability of the polymer and prevent mechanical degradation of the spun elastic yarn, it is best to use an appropriate amount of ethylenediamine and 1,2-propylenediamine as the linear diamine, and meta amine as the cyclic diamine. It is best to use a mixture of xylenediamine and 1,4-cyclohexanediamine.

에틸렌디아민과 1,2-프로필렌디아민의 사용몰비는 1 : 10∼10 : 1의 범위가 적당하며, 사용몰비가 1 : 10미만일 경우에는 반응성이 불량하고, 10 : 1을 초과하는 경우에는 쇄성장이 불충분하여 적절한 물성을 가질 수 있는 분자량을 얻을 수 없다The molar ratio of ethylenediamine and 1,2-propylenediamine is in the range of 1: 10 to 10: 1, and the reactivity is poor when the molar ratio is less than 1: 10, and when it exceeds 10: 1, chain growth Insufficient molecular weight that can have adequate physical properties

또한, 메탈자이렌디아민과 1,4-사이클로헥산디아민의 사용몰비는 1 : 10∼10 : 1의 범위가 적당하고, 사용 몰비가 1 : 10미만일 경우에는 반응성이 빨라서 부반응물이 생성되기 쉽고, 10 : 1을 초과하는 경우에는 반응성이 낮아서 물성이 우수한 폴리머를 얻을 수 없다.In addition, when the use molar ratio of the metal xylene diamine and 1,4-cyclohexanediamine is in the range of 1:10 to 10: 1, and the use molar ratio is less than 1:10, the reactivity is fast and the side reactions are easily formed. When it exceeds 10: 1, it is low in reactivity and a polymer having excellent physical properties cannot be obtained.

쇄성장된 예비중합물의 말단을 봉쇄시키는 쇄정지제인 모느아민계 화합물로서는 모노에탄올아민, 디에탄올아민, 프로필아민, 이소프로필아민, 디이프로필아민, 2-에틸헥실아민, 디(2-에틸헥실) 아민, 부닐아민등의 화합물이 있는데, 이소프로필아민이 쇄정지 효과가 우수하고, 중합물의 분자량을 적정하게 유지시키며 2차적인 무반응을 억제하여 중합물의 안정성을 부여한다. 모노아민계 화합물 사용량은 쇄성장제인 디아민 화합물 사용몰의 1∼30몰%가 적당하며, 1몰% 미만에시는 쇄정지 효과가 불량하여 중합물 점도의 경시변화가 심하여 점도가 계속 상승함으로시 방사가 큰판하고, 30몰%를 초과하는 경우에는 중합물의 쇄성장을 방해하여 적정분자량의 중합물을 얻을 수가 없어시 방사에 적당한 점도를 얻을 수가 없을 뿐만아니라 중합물의 물리적인 물성인 강도, 신도, 탄성회복율이 불량하다.Examples of all-amine compounds, which are chain stoppers for blocking the ends of the chain-grown prepolymer, are monoethanolamine, diethanolamine, propylamine, isopropylamine, dipropylpropyl, 2-ethylhexylamine, di (2-ethylhexyl) There are compounds such as amine and bunylamine, and isopropylamine has an excellent chain stop effect, maintains the molecular weight of the polymer moderately and suppresses the secondary non-reaction to impart stability of the polymer. The amount of monoamine-based compound used is 1 to 30 mol% of the mole used as a chain growth agent, and when it is less than 1 mol%, the chain stopping effect is poor. In the case of larger than 30 mol%, the chain growth of the polymer may be impeded to prevent the proper molecular weight of the polymer from being obtained. Therefore, it is not possible to obtain a viscosity suitable for spinning, and the strength, elongation and elastic recovery rate of the physical properties of the polymer. This is bad.

중합물의 고형분을 조절하므로시 방사성을 좋게 하기 위한 용제로서는 디메틸아세트아미드, 디메틸포름아미드, 헥사메틸포스포로아미드, 디메틸니트로소아민, 디메틸프로피온아미드, 메톡시디메틸아세트아미드, N-메틸피로리딘, 디메틸설폭시드, 테트라메틸렌설폰등의 화합물이 있는데, 디메틸아세트아미드 또는 디메틸포름아미드가 중합물과의 상용성, 방사성, 용제회수성면에서 유리하다. 용제의 사용량은 중합물의 고형분이 15∼45%되게 조정하여 사용하는 것이 좋으며, 15% 미만이거나 45%를 초과할 경우에는 방사성에 악영향을 미친다.Solvents for improving radioactivity by controlling the solid content of the polymer include dimethylacetamide, dimethylformamide, hexamethylphosphoramide, dimethylnitrosoamine, dimethylpropionamide, methoxydimethylacetamide, N-methylpyrrolidine, dimethyl There are compounds such as sulfoxide, tetramethylene sulfone and the like, and dimethylacetamide or dimethylformamide is advantageous in terms of compatibility with the polymer, radioactivity and solvent recovery. The amount of the solvent to be used is preferably adjusted to 15 to 45% of the solid content of the polymer, if less than 15% or more than 45% adversely affects the radioactivity.

본 발명에서는 내열성향상을 위해 하기 일반식(I)로 표현되는 아민결합을 가진 인화합물을 사용한다.In the present invention, a phosphorus compound having an amine bond represented by the following general formula (I) is used for improving heat resistance.

(식중, R1, R2, R3, R4는 수소원자 또는 탄소수가 1∼10인 알킬기 또는 아릴기이며, R5는 탄소수 1∼10의 알킬렌기 또는 벤젠링이다.)(Wherein R 1 , R 2 , R 3 and R 4 are hydrogen atoms or alkyl groups or aryl groups having 1 to 10 carbon atoms, and R 5 is an alkylene group or benzene ring having 1 to 10 carbon atoms.)

아민결합을 가진 화합물로서는 포스포릴디메틸에탄올아민, 2- 디메틸아미노페놀디 페닐포스페이트, 2-디에틸아미노에탄올디메틸포스페이트, 2-에틸프로필아미노페놀디하이드로겐포스페이토, 2-디부틸아미노페놀디하이드로겐포스페이트가 사용가능 하다.Examples of the compound having an amine bond include phosphoryldimethylethanolamine, 2-dimethylaminophenoldiphenylphosphate, 2-diethylaminoethanoldimethylphosphate, 2-ethylpropylaminophenoldihydrogenphosphate, and 2-dibutylaminophenoldi. Hydrogenphosphate can be used.

아민결합을 가진 인화합물의 사용량은 최종 폴리머의 고형분에 대하여 0.01∼1.0중량%, 바람직스럽기는 0.05∼0.5중량%가 좋으며, 0.01중량% 미만이면 내열성의 개선을 보장할 수 없고, 10중량%를 초과하면 과량의 안정제 첨가로 인하여 방사시 폴리머 물성의 악화를 초래할 수 있다.The amount of the phosphorus compound having an amine bond is preferably 0.01 to 1.0% by weight, preferably 0.05 to 0.5% by weight, based on the solid content of the final polymer, and when it is less than 0.01% by weight, the improvement of heat resistance cannot be guaranteed and exceeds 10% by weight. Lower surface additives may cause deterioration of polymer properties during spinning due to the addition of excess stabilizer.

상술한 방법으로 제조한 폴리우레탄 중합체는 기계적인 물성과 산화방지성은 우수하나 내염소성이 불량하여 수영복으로 착용시 수영장의 염소에 의해 손상을 받아서 섬유의 강도와 탄성회복율이 저하되고, 변색현상이 발생된다. 따라서, 본 발명에서는 내염소성 향상제로서 하기식 (II)로 표현되는 디에스테르 금속염화합물을 첨가하였다.Polyurethane polymer prepared by the above-mentioned method is excellent in mechanical properties and anti-oxidation, but poor in chlorine resistance, and is damaged by chlorine in swimming pool when worn as a bathing suit, which lowers the strength and elastic recovery rate of fibers and causes discoloration. do. Therefore, in this invention, the diester metal salt compound represented by following formula (II) was added as a chlorine resistance improving agent.

(식중 R1: 에틸 또는 페닐기, R2: 탄소수 1∼10의 알킬기, 아릴기 또는 알킬아릴기, M1, M2: Na, Ca, Al, Zn, Ba, Pb 중에서 동일 또는 다른 금속이온)(Wherein R 1 : ethyl or phenyl group, R 2 : alkyl group having 1 to 10 carbon atoms, aryl group or alkylaryl group, M 1 , M 2 : same or different metal ion among Na, Ca, Al, Zn, Ba, Pb)

염소에 의한 손상을 방지하는 화합물로서는 금속계의 화합물을 사용하며, 이러한 화합물로서는 아연 스데아레이트, 아연라우레이트, 아연리시노레이트, 아연옥도에이트, 아연벤조에이트 등 지방족금속염이나산화아연, 산화알미늄, 산화질코늄, 산화마그네슘, 산화제2주석, 산화세리움등 금속산화물이나 안하이드라이드계 화합물을 알콜과 반응시켜서 디에스테르 화합물을 생성시킨 후, 말단의 수소를 금속으로 치환한 금속염계 화합물이 사용되며, 안하이드라이드계 화합물의 예로는 벤조익안하이드라이드, 아세틱벤조익안하이드라이드, 아세틱안하이드라이드, 프탈릭안하이드라이드, 석시닉안하이드라이드, 말레익안하이드라이드, 아세틱프타노익안하이드라이드 화합물등이 있는데 탄성중합체의 고유한 물성을 저해하지 않으면서도 염소에 대한 견뢰도를185 향상시키는데 가장 효과적인 화합물은 안하이드라이드계 화합물로부터 제조된 디에스테르 화합물의 말단수소를 금속으로 치환한 금속염계 화합물이 가장 효과적이다.Metal-based compounds are used as compounds to prevent damage by chlorine, and as such compounds, aliphatic metal salts such as zinc deslate, zinc laurate, zinc licinolate, zinc oxate and zinc benzoate, zinc oxide, aluminum oxide, Metal oxide compounds such as nitrous oxide, magnesium oxide, ditin tin oxide, cerium oxide, and anhydride compounds are reacted with alcohols to form diester compounds, and then metal salt compounds are used in which the terminal hydrogen is replaced with a metal. Examples of the anhydride-based compound are benzoic anhydride, acetic benzoic anhydride, acetic anhydride, phthalic anhydride, succinic anhydride, maleic anhydride, aceticptanoic anhydride compound And chlorine without compromising the inherent properties of the elastomer. The most effective compound for improving the fastness 185 is the most effective metal salt compound of the terminal hydrogen of the diester compound prepared from the anhydride compound substituted with a metal.

이러한, 금속염계 화합물의 적정사용량은 중합물 고형분에 대하며 0.01∼3중량%가 적당하며, 0.01중량%미만에시는 내염소성 효과가 불충분하며, 3중량%를 초과하는 경우에는 내염소성 상승효파가 미미하고 탄성중합체와 고유한 물성을 저해하고 방사성에도 악영향을 미친다.The proper amount of the metal salt-based compound is 0.01 to 3% by weight based on the solid content of the polymer, and at less than 0.01% by weight, the chlorine resistance effect is insufficient, and when it exceeds 3% by weight, the chlorine resistance synergistic effect is insignificant. It inhibits the elastomer and its inherent physical properties and adversely affects radioactivity.

상기의 방법으로 제조한 중합체 용액을 통상의 건식방사법을 이용하여 70데이너의 폴리우레탄 탄성사를 제조후 각종 물성을 측정하였다. 실시예에 기재된 인장강도, 신도 및 탄성회복율은 KSK 0219에 준하여 측정하였고, 내열성은 탄성사를 130℃의 열풍건조기에서 60분간 처리후 강도유지율 및 색상변화(Gray scale : ISO international standard)로 평가하였으며, 내염소성은 유효염소농도가 200P.P.M이고, pH가 7인 용액을 제조후 용액의 온도를 25℃로 유지시키고 이 용액내에 탄성사를 일정시간 처리후 인장강도 및 신도변화를 평가하였다.Various physical properties of the polymer solution prepared by the above method were prepared by using a conventional dry spinning method to prepare a polyurethane elastic yarn of 70 days. Tensile strength, elongation and elastic recovery rate described in the Examples were measured according to KSK 0219, and heat resistance was evaluated by strength retention rate and color change (Gray scale: ISO international standard) after 60 minutes treatment of the elastic yarn in a hot air dryer at 130 ° C. Chlorine resistance was 200 P.PM effective chlorine concentration, pH 7 was prepared after the solution temperature was maintained at 25 ℃ and the elastic yarn in the solution after a certain time to evaluate the tensile strength and elongation change.

한편, 중합물의 점도는 부룩필드(Brook Field제품) 모델번호 DV-III로 측정하였다.In addition, the viscosity of the polymer was measured by Brookfield (Brook Field) model number DV-III.

다음의 실시예 및 비교예는 본 발명을 좀더 구체적으로 설명하는 것이지만, 본 발명의 범주를 한정하는 것은 아니다.The following examples and comparative examples further illustrate the present invention, but do not limit the scope of the present invention.

(실시예 1)(Example 1)

분자량이 1980인 폴리테트라메틸렌에테르글리콜 0.92몰과 1,4-부탄디올을 0.08몰 혼합한 용액에 4,4' 디메틸디이소시아네이트 1.7몰을 첨가하여 질소가스 분위기하에서 75℃×60분간 중합하여 예비중합물을 제조하였다. 이 예비중합물을 디메틸아세트아미드에 용해시켜 용액의 온도를 5℃까지 냉각한 후 쇄성장제로서 선형디아민인 에틸렌 디아민과 1,2-프로필렌다이만 및 환형디아민 1,4-사이클로헥산디아민과 메타자이렌디아민을 전체 디아민몰을 기준으로 하여 7.0/1.5/1.2/0.3의 몰비율로 혼합한 후 디메틸아세트아미드에 20%의 농동로 용해시킨다. 이 용액내의 전체디아민의 몰수가 예비중합물의 말단 디이소시아네이트와 비교하여 0.95가 되도록 하며 중합액에 서서히 첨가한다. 제조된 중합물의 점도는 3,700포이즈 이었다. 이소프로필아민을 디메틸아세트아미드에 20%의 농도로 용해시킨 용액을 이소프로필아민의 몰수가 최초 예비중합물의 말단 이소시아네이트와 비교하여 0.05몰이 되도록 하여 쇄성장된 중합물에 서서히 첨가하여 점도가 3,000포이즈인 중합물을 얻었으며, 이 중합액에 아세틱안하이드라이드를 디메틸아세트아미드에 2% 농도로 용해시킨 용해액 250g을 첨가하여 중합물의 점도를 안정화시켰다.1.7 mol of 4,4 'dimethyl diisocyanate was added to a solution containing 0.92 mol of polytetramethylene ether glycol having a molecular weight of 1980 and 0.08 mol of 1,4-butanediol, and then polymerized in a nitrogen gas atmosphere at 75 캜 for 60 minutes to prepare a prepolymer. Prepared. The prepolymer was dissolved in dimethylacetamide, the solution was cooled to 5 ° C., and then linear diamine, ethylene diamine, 1,2-propylenediman, and cyclic diamine 1,4-cyclohexanediamine and metazyme as chain growth agents. Rendiamine is mixed at a molar ratio of 7.0 / 1.5 / 1.2 / 0.3 based on the total diamine moles and then dissolved in dimethylacetamide with a concentration of 20%. The number of moles of total diamine in this solution is 0.95 compared to the terminal diisocyanate of the prepolymer, and is slowly added to the polymerization solution. The viscosity of the prepared polymer was 3,700 poise. A solution obtained by dissolving isopropylamine in dimethylacetamide at a concentration of 20% was gradually added to a chain-grown polymer with a molar number of isopropylamine of 0.05 mole compared to the terminal isocyanate of the first prepolymer, resulting in a viscosity of 3,000 poises. To the polymer solution, 250 g of a solution in which acetic anhydride was dissolved in dimethylacetamide at a concentration of 2% was added to stabilize the viscosity of the polymer.

중합완료후 포스포릴디메틸에탄올아민을 디메틸아세트아미드에 10%의 농도로 용해시킨 용해액을 포스포릴디메틸에탄올아민이 최종 폴리머 고형분의 0.2중량%가 되게 첨가함과 동시에 내염소성 향상제로시 아세틱안하이드라이드 화합물로부터 제조된 디에스테르 금속염 화합물의 말단수소를 아연으로 치환한 화합물을 디메딜아세트아미드에 2%의 농도로 용해시킨 용해액을 내염소성 향상제가 최종폴리머 고형분의 0.5중량%가 되도록 첨가하여 최종 중합물의 고형분을 32%로 조정하였으며, 이때의 점도는 3,300포이즈이다.After the completion of the polymerization, a solution of phosphoryldimethylethanolamine dissolved in dimethylacetamide at a concentration of 10% was added so that phosphoryldimethylethanolamine became 0.2% by weight of the final polymer solids, and at the same time, as a chlorine resistance enhancer. A solution obtained by dissolving a compound substituted with terminal hydrogen in zinc of a diester metal salt compound prepared from a lide compound at a concentration of 2% in dimedylacetamide was added so that the chlorine resistance enhancer was 0.5% by weight of the final polymer solids. Solid content of the polymer was adjusted to 32% with a viscosity of 3,300 poise.

이 중합물을 통상의 건식방사법으로 이용하여 방사후 70데니어의 폴리우레탄 탄성사를 제조하였으며, 물성을 평가한 결과는 표 1과 같다.This polymer was used in a conventional dry spinning method to prepare a polyurethane elastic yarn of 70 denier after spinning, the results of the evaluation of physical properties are shown in Table 1.

(비교실시예1)Comparative Example 1

포스포릴디메틸에탄올 아민화합물을 사용하지 않는 것 이외에는 실시예 1과 동일하게 중합했으며, 물성을 평가한 결과는 표 1과 같다.Polymerization was carried out in the same manner as in Example 1 except that no phosphoryldimethylethanol amine compound was used, and the results of the evaluation of the physical properties are shown in Table 1.

(비교실시예 2)Comparative Example 2

내염소성 향상제를 사용하지 않은 것 이외에는 실시예 1과 동일하게 중합했으며, 물성을 평가한 결과는 표 1과 같다.The polymerization was carried out in the same manner as in Example 1 except that the chlorine resistance enhancer was not used, and the results of evaluating the physical properties are shown in Table 1.

[표 1] 물성평가결과[Table 1] Property evaluation results

Claims (3)

수평균 분자량 1,000∼3,000의 고분자량 디올화합물 90∼95몰%와 수평균 분자량 50∼500의 저분자량 디올화합물 5∼10몰%로 구성되는 디올화합물 1몰과 디이소시아네이트 화합물 1.25∼2.5몰의 비율로 예비중합후 용제를 혼합하여 예비중합물의 용액을 제조하고 4종의 디아민 화합물을 일정비율로 혼합한 쇄성장제를 예비중합물의 0.60∼0.98몰% 사용하여 쇄성장시켜 방사에 유리한 점도를 만든 다음, 디아민화합물에 대하여 1∼30몰%의 모노아민화합물로 쇄정지시킨 후, 일반식 (I)로 표현되는 내열성 향상 첨가제와 일반식 (II)로 표현되는 내염소성 향상제인 디에스테로 금속염화합물을 첨가하여 중합물을 얻고 이를 방사함을 특징으로 하는 탄성섬유의 제조방법The ratio of 1 mol of a diol compound and 1.25 to 2.5 mol of a diisocyanate compound consisting of 90 to 95 mol% of a high molecular weight diol compound having a number average molecular weight of 1,000 to 3,000 and 5 to 10 mol% of a low molecular weight diol compound having a number average molecular weight of 50 to 500 After prepolymerization, solvents were mixed to prepare a solution of the prepolymer, and chain growth was performed using 0.60-0.98 mol% of a pre-polymerized chain growth agent mixed with four diamine compounds at a constant ratio to make a viscosity favorable for spinning. After the chain stops with 1 to 30 mol% of a monoamine compound with respect to the diamine compound, a heat resistance improving additive represented by the general formula (I) and a diester metal salt compound which is a chlorine resistance enhancer represented by the general formula (II) are added. Method for producing an elastic fiber, characterized in that to obtain a polymer by spinning (식중, R1, R2, R3, R4는 수소원자 또는 탄소수가 1∼10인 알킬기 또는 아릴기이며, R5는 탄소수 1∼10의 알킬렌기 또는 벤젠링이다.)(Wherein R 1 , R 2 , R 3 and R 4 are hydrogen atoms or alkyl groups or aryl groups having 1 to 10 carbon atoms, and R 5 is an alkylene group or benzene ring having 1 to 10 carbon atoms.) (식중 R1: 에틸 또는 페닐기, R2: 탄소수 1∼10의 알킬기, 아릴기 또는 알킬아릴기, M1, M2 : Na, Ca, Al, Zn, Ba, Pb 중에서 동일 또는 다른 금속이온)(Wherein R 1 : ethyl or phenyl group, R 2 : alkyl group having 1 to 10 carbon atoms, aryl group or alkylaryl group, M1, M2: same or different metal ion among Na, Ca, Al, Zn, Ba, Pb) 제 1 항에 있어서, 내열성 향상첨가제 사용량은 폴리머 고형분에 대하여 0.01∼1.0중량%임을 특징으로한 탄성섬유의 제조방법.The method for producing an elastic fiber according to claim 1, wherein the amount of the heat resistance improving additive is 0.01 to 1.0% by weight based on the polymer solids. 제 1 항에 있어서, 내염소성 향상제 사용량은 폴리머 고형분에 내하여 0.01∼3중량%임을 특징으로 하는 탄성섬유의 제조방법.The method of manufacturing an elastic fiber according to claim 1, wherein the amount of the chlorine resistance enhancer is 0.01 to 3% by weight, based on the polymer solid content.
KR1019940038735A 1994-12-29 1994-12-29 Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property KR970010727B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019940038735A KR970010727B1 (en) 1994-12-29 1994-12-29 Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019940038735A KR970010727B1 (en) 1994-12-29 1994-12-29 Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property

Publications (2)

Publication Number Publication Date
KR960023324A KR960023324A (en) 1996-07-18
KR970010727B1 true KR970010727B1 (en) 1997-06-30

Family

ID=19404955

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019940038735A KR970010727B1 (en) 1994-12-29 1994-12-29 Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property

Country Status (1)

Country Link
KR (1) KR970010727B1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100487835B1 (en) * 1996-11-18 2005-08-31 바이엘 악티엔게젤샤프트 Chlorine Resistant Elastane Fiber

Also Published As

Publication number Publication date
KR960023324A (en) 1996-07-18

Similar Documents

Publication Publication Date Title
KR101130510B1 (en) Anti-chlorine Spandex Fiber and Preparation Method thereof
KR100437988B1 (en) High chlorine and heat resistant spandex fiber and manufacturing method thereof
JP4065233B2 (en) Spandex containing a mixture of phenolic compounds and inorganic additives
US4499221A (en) Polyurethane composition improved in dyeing property
KR970010727B1 (en) Method for the preparation of polyurethane filaments with heat resistant and anti-chlorine property
KR0131832B1 (en) Manufacturing method of polyurethan elastic fiber
KR950013484B1 (en) Method for the preparation of the elastic fiber having heat and chlorine resistane
JP4264912B2 (en) Polyurethane urea composition and polyurethane elastic fiber
EP0610378B1 (en) Stabilized polyurethaneurea solutions and spandex fibres therefrom
KR0139357B1 (en) Polyurethane Elastic Fiber Manufacturing Method
KR970007688B1 (en) Manufacturing method of chloride-proof elastic fiber with autioxidation property
KR970007685B1 (en) Manufacturing method of elastic fiber
KR0134656B1 (en) Method for manufacturing polyuretane elastomer with good viscosity stability
KR0131833B1 (en) Manufacturing method of ployurethane
JP2000169700A (en) Polyurethane composition and polyurethane elastic yarn
KR940011541B1 (en) Manufacturing process of polyurethane elastic fiber having an excellent dyeing property
JP4613802B2 (en) Polyurethane elastic fiber, method for producing the same, and use thereof
KR960011609B1 (en) Process for preparing elastic fiber with an excellent stability to ultraviolet and chlorine resistance
KR970010728B1 (en) Method for the preparation of viscosity -stable and high elastic recoverable polyurethane filaments
KR0150690B1 (en) Process for preparing polyurethane-elastic fiber having oxidation-resistance and heat-resistance
KR970010729B1 (en) Manufacturing process of polyurethane elastic fiber having excellent light and heat-resistant properties
KR0163493B1 (en) Method of manufacturing polyurethane elastic fiber
KR940011771B1 (en) Process for preparation of polymer used with textile
JPS59223751A (en) Polyurethane composition
KR940003861B1 (en) Forming method of elastic fiber

Legal Events

Date Code Title Description
A201 Request for examination
G160 Decision to publish patent application
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20050112

Year of fee payment: 9

LAPS Lapse due to unpaid annual fee