KR970010708B1 - Process for preparing polyester fiber - Google Patents

Process for preparing polyester fiber Download PDF

Info

Publication number
KR970010708B1
KR970010708B1 KR1019930020853A KR930020853A KR970010708B1 KR 970010708 B1 KR970010708 B1 KR 970010708B1 KR 1019930020853 A KR1019930020853 A KR 1019930020853A KR 930020853 A KR930020853 A KR 930020853A KR 970010708 B1 KR970010708 B1 KR 970010708B1
Authority
KR
South Korea
Prior art keywords
weight
polyester fiber
compound
polyethylene terephthalate
integer
Prior art date
Application number
KR1019930020853A
Other languages
Korean (ko)
Other versions
KR950011666A (en
Inventor
한석호
김문찬
Original Assignee
동양폴리에스터 주식회사
배 도
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 동양폴리에스터 주식회사, 배 도 filed Critical 동양폴리에스터 주식회사
Priority to KR1019930020853A priority Critical patent/KR970010708B1/en
Publication of KR950011666A publication Critical patent/KR950011666A/en
Application granted granted Critical
Publication of KR970010708B1 publication Critical patent/KR970010708B1/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
    • D01F1/09Addition of substances to the spinning solution or to the melt for making electroconductive or anti-static 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
    • D01F6/78Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products
    • D01F6/84Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolycondensation products from copolyesters
    • 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
    • D02G3/02Yarns or threads characterised by the material or by the materials from which they are made
    • 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
    • D02G3/44Yarns or threads characterised by the purpose for which they are designed
    • D02G3/441Yarns or threads with antistatic, conductive or radiation-shielding properties
    • 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
    • D10B2331/04Fibres made from polymers obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds, e.g. polycondensation products polyesters, e.g. polyethylene terephthalate [PET]
    • 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
    • D10B2401/16Physical properties antistatic; conductive

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)
  • Polyesters Or Polycarbonates (AREA)

Abstract

Keeping polymer vessel which has polyethylene terephthalate oligomer l0[kg , at 260 degree C, a slurry is made with a terephthalic acid and an ethyleneglycol and SiO2 of which particle size is 0.05 micrometer, among the metal which has high electric property, SiO2 of which particle size is 0.02 micrometer, a calcium phosphate anhydride is fed in the slurry for 6 hours and an oligomer 20[kg is produced. To produced oligomer, an antimony trioxide, C12H250(C2H40)40H and C12H25SO3Na are thrown in and reacted at 280 degree C and then a polyester fiber is produced.

Description

폴리에스터 섬유의 제조방법Method for producing polyester fiber

본 발명은 일반 폴리에스터 섬유의 장점을 그대로 유지하면서 종래의 폴리에스터 섬유의 단점인 정전기 발생을 억제하여 제전성능을 부여하며 또한 흡수성을 부여하는 제전사의 개량된 제조방법에 관한 것이다.The present invention relates to an improved manufacturing method of an antistatic agent that imparts antistatic performance and provides absorbency while suppressing generation of static electricity, which is a disadvantage of conventional polyester fibers, while maintaining the advantages of general polyester fibers.

폴리에스터 섬유는 내열성, 내약품성, 강신도, 결정성, 굴곡강도 등의 물성이 우수하여 의류용으로 크게 각광을 받고 있지만 저온이며 저습도인 지역이나, 겨울철에는 안감이나, 란제리, 화운데이션, 기타 무진복이나 운동복 등 특수 기능복으로 사용하기에는 마찰에 의한 정전기의 발생으로 먼지들이 흡착, 오염이 쉽게 되고 또한 땀이나 습기를 흡수하는 성질이 약해 착용자에게 쇼크나 불쾌감을 주게 되는 문제점이 있다. 이러한 정전기적인 장애와 흡수성이 미약한 문제를 해결하기 위하여 많은 방법들이 제안되었다. 폴리옥시알킬렌글리콜에 메타크릴레이트나 비스페놀을 사용하고 플라즈마 방법으로 후가공 처리하여 대전방지 기능을 부여하는 방법이 있으나, 이 방법은 세탁후 제전성이 급격히 떨어지는 단점이 있었다. 이러한 내세탁성 문제를 해결하고 영구적인 제전성을 부여하기 위하여 일본 공개특허 공보 소화 52-47071호 및 동 52-47072호에서 소개된 폴리알킬렌글리콜과 알킬술폰산나트륨을 사용하여 폴리머를 개질하는 방법이 최근 많이 사용되고 있다. 알킬술폰산나트륨은 폴리머에 이온성지를 도입시켜 전하의 이동을 활발하게 하고 또한 폴리알킬렌글리콜의 공중합물과의 상승작용으로 우수한 제전성능을 발현시킬 수 있는 장점을 가지고 있다. 또한 SiO2를 사용하여 감량공정을 거쳐 다조홈을 생성하여 흡습성과 제전성능의 증가를 가져올 수 있다. 그러나, SiO2의 분산이 불량하면 폴리머 내부에서의 분산성이 나쁘고 방사시 팩압을 증가시키는 요인이 된다. 또한 방사노즐 내부에 나트륨금속염과 SiO2가 잔존하는 경우가 생겨 방사불량이 생기고 팩교환 주기가 짧아져 방사작업성이 떨어지고 폴리머내부에서의 분산성이 나빠, 염색불량의 원인이 되기도 한다.Polyester fiber is attracting much attention for clothing because it has excellent properties such as heat resistance, chemical resistance, elongation, crystallinity, and flexural strength, but in low temperature and low humidity areas, it is lining, lingerie, foundation, and other dust-free clothing in winter. In order to use it as a special functional clothing such as sportswear or the like, dust is easily adsorbed and contaminated by the generation of static electricity due to friction, and there is a problem in that shock or discomfort is given to the wearer due to the weak property of absorbing sweat or moisture. Many methods have been proposed to solve this problem of electrostatic failure and weak absorption. There is a method of imparting antistatic function by post-processing by using methacrylate or bisphenol in polyoxyalkylene glycol and plasma method, this method has a disadvantage in that the antistatic property is sharply reduced after washing. In order to solve this problem of washing resistance and to impart permanent antistatic properties, a method of modifying a polymer using polyalkylene glycol and sodium alkyl sulfonate introduced in Japanese Patent Laid-Open Nos. 52-47071 and 52-47072 is disclosed. This has been used a lot lately. Sodium alkyl sulfonate has an advantage of expressing excellent antistatic performance by introducing ionic paper into the polymer to promote charge transfer and synergy with the copolymer of polyalkylene glycol. In addition, SiO 2 may be used to create a multi-column groove through a weight loss process to increase hygroscopicity and antistatic performance. However, poor dispersion of SiO 2 results in poor dispersibility inside the polymer and increases pack pressure during spinning. In addition, sodium metal salt and SiO 2 remain inside the spinning nozzle, resulting in poor spinning and short cycle of pack replacement, resulting in poor spinning workability and poor dispersibility in the polymer, which can lead to poor dyeing.

한편 흡습성을 부여하기 위해 섬유 표면의 그르프트화와 친수성 성질에 의한 표면처리 및 표면의 비누화 처리 등이 있으나 내세탁성이 불량하여 영구적으로 흡습성을 발현하지 못하는 단점이 있다. 본 발명은 이러한 문제점을 해결코자 하는 것으로 유전율이 높은 금속미립자를 첨가하여 보다 제전성능을 높임을 특징으로 한다.On the other hand, in order to impart hygroscopicity, there are surface treatment and surface saponification treatment due to grafting and hydrophilic properties of the fiber surface, but there is a disadvantage in that it does not express hygroscopicity permanently due to poor washing resistance. The present invention is to solve this problem is characterized in that to increase the antistatic performance by adding a metal particle with a high dielectric constant.

즉 본 발명은 폴리에틸렌 테레프탈레이트(PET)를 기재로 하여 폴리에스터 섬유를 제조함에 있어서, 폴리옥시알킬렌글리콜화합물, 비반응성 폴리알킬술폰산금속염, 콜로이드상의 SiO2, 포스페이트계 분산제 및 유전율이 높은 하기 식(1)의 금속미립자를 첨가 공중합시켜 수득한 폴리에스터로 제조한 제전성 및 흡습성이 우수한 폴리에스터 섬유의 제조방법에 관한 것이다.That is, the present invention, in the production of polyester fibers based on polyethylene terephthalate (PET), polyoxyalkylene glycol compound, non-reactive polyalkylsulfonic acid metal salt, colloidal SiO 2 , phosphate-based dispersant and high dielectric constant The manufacturing method of the polyester fiber excellent in the antistatic property and hygroscopicity produced from the polyester obtained by addition-copolymerization of the metal fine particle of (1).

MexOy…………………………………………………………………………… (1)MexOy… … … … … … … … … … … … … … … … … … … … … … … … … … … … … (One)

(여기에서 Me는 3주기 또는 4주기 전이금속원소 또는 In, Sn, Sb, Ge, Al, Ga으로부터 선택되는 화합물이고, x, y는 0 내지 5의 정수이다.)(Where Me is a 3- or 4-cycle transition metal element or a compound selected from In, Sn, Sb, Ge, Al, Ga, and x and y are integers from 0 to 5.)

본 발명에서 사용되는 유전율이 높은 상기 식(Ⅰ)의 금속미립자는 입자 크기가 0.001㎛∼1㎛로 입자의 크기가 커지면 방사시 팩압이 증가되며 방사불량의 원인이 된다. 첨가량은 PET대비 0.01∼10중량%가 바람직한바 이보다 적은 량일 경우 제전효과가 크지 못하며, 이 이상 첨가하게 되면 방사불량을 초래하며 사물성이 저하된다.The metal fine particles of the formula (I) having a high dielectric constant used in the present invention have a particle size of 0.001 µm to 1 µm, which increases the pack pressure during spinning and causes radiation failure. If the amount is less than 0.01 to 10% by weight compared to the preferred amount less than the antistatic effect is not great, if added more than this will result in poor radiation and lower the objectivity.

한편 본 발명에서 규소화합물과 금속미립자의 분산을 용이하게 하기 위하여 사용하는 분산제는 하기 식(2)와 같다.On the other hand, the dispersant used to facilitate the dispersion of the silicon compound and metal fine particles in the present invention is as shown in the following formula (2).

MHn2(PO4) n3………………………………………………………………………(2)MHn 2 (PO 4 ) n 3 . … … … … … … … … … … … … … … … … … … … … … … … … … … (2)

(여기에서 M은 K, Na, Ca, Al, NH4으로 구성되는 군으로부터 선택되는 화합물이고 ; n2는 0∼4의 정수이며, n3는 1∼2의 정수이다.)(Here, M is a compound selected from the group consisting of K, Na, Ca, Al, NH 4; n 2 is an integer of 0 to 4, n 3 is an integer of 1 to 2.)

본 발명에서 분산제로 사용하는 상기 일반식(2)의 화합물은 NaH2PO4, Na2HPO4, Na3PO4, KH2PO4, K2HPO4, K3PO4, CaH4(PO4)2, CaHPO4, NH4H2PO4, (NH4)2HPO4등을 예시할 수 있다.The compound of formula (2) used as a dispersant in the present invention is NaH 2 PO 4 , Na 2 HPO 4 , Na 3 PO 4 , KH 2 PO 4 , K 2 HPO 4 , K 3 PO 4 , CaH 4 (PO 4 ) 2 , CaHPO 4 , NH 4 H 2 PO 4 , (NH 4 ) 2 HPO 4 and the like can be exemplified.

이때 사용함량은 다음에 기술될 SiO2의 0.05∼5중량%가 바람직하다. 0.05중량% 이하일 경우에는 분산제의 효과가 크게 감소하여 금속 및 규소 미립자가 균일하게 분산되지 못하고 큰 응집입자의 형성이 증가하게 된다. 또한 5중량% 이상일 경우에는 방사후 사물성이 저하되는 문제가 발생한다.At this time, the use content is preferably 0.05 to 5% by weight of SiO 2 to be described later. If less than 0.05% by weight, the effect of the dispersant is greatly reduced, the metal and silicon fine particles are not uniformly dispersed, the formation of large aggregated particles is increased. In addition, when 5% by weight or more, the problem of deterioration of the object after spinning occurs.

본 발명에서의 폴리옥시알킬렌글리콜 화합물은 수평균 분자량이 2,000 이상이고 30,000 이하인 하기 식(3)의 화합물로서 PET대비 0.01∼3.5중량%를 축중합시키기에 넣어 폴리에스터주쇄의 말단에 공중합시킴이 바람직하고, 투입량이 0.01중량% 이하일 경우 제전성 및 흡습성이 극히 떨어지고 3.5중량% 이상일 경우에는 사의 기본물성이 저하된다.The polyoxyalkylene glycol compound in the present invention is a compound of formula (3) having a number average molecular weight of 2,000 or more and 30,000 or less and copolymerized at the end of the polyester backbone by condensation polymerization of 0.01 to 3.5% by weight relative to PET. Preferably, when the amount is 0.01% by weight or less, the antistatic properties and hygroscopicity is extremely inferior, and when 3.5% by weight or more, the basic physical properties of the yarn is lowered.

R1O(R2O) n1H …………………………………………………………………………(3)R 1 O (R 2 O) n 1 H... … … … … … … … … … … … … … … … … … … … … … … … … … … … (3)

(여기에서 R1은 C1∼C13인 알킬기 또는 H이고, R2는 C2∼C13인 알킬렌기이며, n1은 20∼150의 정수이다.)(Herein, R 1 is C 1 -C 13 alkyl group or H, R 2 is C 2 -C 13 alkylene group, n 1 is an integer of 20 to 150.)

축중합시의 반응온도는 초기 260℃에서 1시간 30분에 걸쳐 조절하고 올리고머 반응종료시까지 이 온도를 유지한다. 한편 본 발명에서의 폴리알킬술폰산금속염은 식(4)의 비반응성 폴리알킬술폰산금속염을 사용하며, 그 사용량은 PET대비 0.01∼2중량%가 바람직하다.The reaction temperature at the time of the condensation polymerization is controlled at an initial stage of 260 ° C. over 1 hour and 30 minutes and maintained at the end of the oligomer reaction. On the other hand, the polyalkylsulfonic acid metal salt of the present invention uses a non-reactive polyalkylsulfonic acid metal salt of formula (4), the amount of which is preferably 0.01 to 2% by weight relative to PET.

R3SO3Me ………………………………………………………………………………(4)R 3 SO 3 Me... … … … … … … … … … … … … … … … … … … … … … … … … … … … … … (4)

(여기에서 R3은 C3∼C25인 알킬기 또는 C7∼C30인 아릴기이고, Me는 Li, K, Na이다.)(Wherein R 3 is a C 3 ~C 25 alkyl group or a C 7 ~C 30 aryl group, Me is Li, K, Na.)

이때, 폴리알킬술폰산금속염의 함량이 2중량%보다 많으면 디에틸렌글리콜(DEG)의 함량이 많아져서 동일 용융점도에서 중합물을 배출할 경우 고유점도가 높아져 사물성에서 신도가 너무 낮아지는 단점이 발생하고 0.01중량%보다 적은 경우에는 점도가 낮아져서 곤란하다. 따라서 바람직한 첨가량은 PET대비 0.01∼2중량%이다.At this time, when the content of the polyalkyl sulfonate metal salt is more than 2% by weight, the content of diethylene glycol (DEG) increases, so that when the polymer is discharged at the same melt viscosity, the intrinsic viscosity becomes high, and the elongation is too low in the object. When less than 0.01 weight%, a viscosity becomes difficult and it is difficult. Therefore, the preferred amount is 0.01 to 2% by weight compared to PET.

또한 일반적으로 알려진 바와 같이 축중합시 촉매로서 Sb2O3를 200∼400ppm 첨가하고 아래와 같은 인화합물을 10∼200ppm 첨가한후 2시간 동안 반응을 시킴으로써 열안정성을 높일수 있다.In addition, as is generally known, thermal stability can be enhanced by adding 200-400 ppm of Sb 2 O 3 as a catalyst during condensation polymerization, adding 10-200 ppm of the following phosphorus compounds, and reacting for 2 hours.

(여기에서 R46는 H 또는 알킬기이다.)(Wherein R 4 to 6 are H or an alkyl group)

본 발명에서 사용되는 규소미립자(SiO2)의 첨가량은 PET대비 0.1∼10중량%로 하는 것이 적당하다. 0.1중량% 이하인 경우 표면 요철갯수가 적어 염색시 심색효과와 흡습성이 저하되며 10% 이상 첨가시 사물성이 현저히 저하되는 문제가 있다.The amount of silicon fine particles (SiO 2 ) used in the present invention is suitably 0.1 to 10% by weight compared to PET. When less than 0.1% by weight, the number of surface irregularities is small, there is a problem that the deep color effect and hygroscopicity when dyeing, and when added more than 10%, the objectivity is significantly reduced.

본 발명에서 슬러리 제조방법으로는 에틸렌글리콜(EG)에 30중량%로 분산시킨 SiO2도우프(dope)액에 일반식(2)의 분산제를 투입하고 여기에 EG/TPA 몰비가 1.1이 되도록 적정량의 에틸렌글리콜(EG)을 첨가한 후 교반시켜 균일하게 분산된 규소미립자에틸렌글리콜액을 만들고 약 10시간 방치한 후 테레프탈산(TPA)을 EG/TPA 몰비가 1.1이 되게 넣어 슬러리를 제조한다.In the present invention, in the slurry production method, a dispersant of the general formula (2) is added to a SiO 2 dope liquid dispersed in ethylene glycol (EG) at 30% by weight, and the EG / TPA molar ratio is adjusted to 1.1. After the addition of ethylene glycol (EG) and stirred to make a uniformly dispersed silicon fine ethylene glycol liquid and left for about 10 hours, terephthalic acid (TPA) to the EG / TPA molar ratio of 1.1 to prepare a slurry.

본 발명의 중합공정은 알킬술폰산금속염과 폴리옥시알킬렌글리콜을 축중합 초기에 투입하여 약 1시간에 걸쳐 0.5torr까지 진공을 걸어주며 그후 280℃에서 2시간동안 0.5torr 이하에서 중합시켜 폴리에스터중합폴리머를 만든다. 본 발명에 따라 수득하는 폴리에스터 제전사는 폴리에스터 섬유 고유의 물성을 저해하지 않으면서도 제전성능이 우수하고 흡습성이 뛰어나며 심색성, 광택 촉감이 우수한 의류용 및 기능복에 널리 사용이 가능하다.In the polymerization process of the present invention, the alkyl sulfonate metal salt and polyoxyalkylene glycol are introduced at the initial stage of the condensation polymerization, and vacuum is applied to 0.5 torr over about 1 hour, and then polymerized at 0.5 tor or less for 2 hours at 280 ° C. to polymerize the polyester. Make a polymer. The polyester antistatic yarn obtained according to the present invention can be widely used in clothing and functional clothes having excellent antistatic performance, excellent hygroscopicity, deep colorability and gloss feel without sacrificing the inherent properties of polyester fibers.

이하에 실시예를 들어 설명한다.An example is given and described below.

(측정방법)(How to measure)

(1) 수분율(moisture regain) : 용출처리한 시료를 110℃에서 60분간 건조해서 무게(W1)를 측정하고 상온(25℃, 60%RH)에서 12시간 방치한 시료 무게(W2)를 측정하여(1) Moisture regain: Measure the weight (W1) by drying the eluted sample at 110 ° C for 60 minutes, and measure the weight of the sample (W2) left at room temperature (25 ° C, 60% RH) for 12 hours.

로 계산Calculate

(2) 비저항 : 항온항습실에서 일본 TOA사의 전기저항측정기를 사용하여 측정한다.(2) Resistivity: Measured by using an electric resistance measuring instrument of TOA of Japan in a constant temperature and humidity room.

(3) 마찰대전압, 반감기 : 가네보식 마찰대전압 측정기를 사용하여 측정한다.(3) Friction band voltage, half-life: Measured using a Kanebo friction belt voltage meter.

※ 비저항, 마찰대전압, 반감기는 온도 20±2℃, 습도 40±2RH%에서 측정하였다.※ Specific resistance, friction band voltage and half-life were measured at 20 ± 2 ℃ and 40 ± 2RH% humidity.

(실시예 1)(Example 1)

폴리에틸렌테레프탈레이트 올리고머(PET) 10kg이 함유된 중합조를 260℃로 유지하면서 테레프탈산 8645g과 에틸렌글리콜 3875g과 미립자 크기가 0.05μm의 SiO2400g 및 유전율이 높은 금속미립자(1) 중 입자크기가 0.02㎛의 SnO2200g을 앞에서 기술한 방법에 따라 슬러리를 준비하되 분산제는 (2)화합물 중의 1종인 칼슘포스페이트 안하이드라이드[CaH(PO4)] 6g을 잘 혼합된 슬러리에 6시간에 걸쳐서 투입하여 20kg의 올리고머를 제조한 후 다른 중합조로 10kg을 옮긴다. 이 올리고머에 삼산화안티몬 4g과 식(3)의 화합물 C12H25O(C2H4O)40H 100g과 식(4)의 화합물 C12H25SO3Na 50g을 투입한 후, 280℃에서 반응시켜 본 발명의 폴리에스터를 제조하였다. 얻어진 중합체를 통상의 방법으로 건조한 후, 중공율 20%로 방사하여 얻어진 미연신사를 80℃로 유지된 가열로울러 및 120℃로 유지된 열판에 의해 1070m/min의 연신속도로 연신하여 75d/36f의 연신사를 제조하였다.While maintaining a polymerization tank containing 10 kg of polyethylene terephthalate oligomer (PET) at 260 ° C., 8645 g of terephthalic acid, 3875 g of ethylene glycol, 400 g of SiO 2 having a particle size of 0.05 μm, and a high dielectric constant metal fine particle (1) had a particle size of 0.02 μm. Prepare 200g of SnO 2 according to the method described above, but dispersing agent was added 20g of 6g of calcium phosphate anhydride [CaH (PO 4 )], one of the compounds (2), over 6 hours After preparing the oligomer of 10kg was transferred to another polymerization tank. The compounds of antimony trioxide 4g and formula (3) in the oligomer C 12 H 25 O (C 2 H 4 O) was charged into the compound C 12 H 25 SO 3 Na 50g of 40 H 100g and expression (4), 280 ℃ Reaction was carried out to prepare the polyester of the present invention. After drying the obtained polymer in a conventional manner, the unstretched yarn obtained by spinning at a hollow rate of 20% was stretched at a drawing speed of 1070 m / min by a heating roller maintained at 80 ° C. and a hot plate maintained at 120 ° C. to obtain 75 d / 36f. The drawn yarn was manufactured.

(실시예 2∼5, 비교예 1∼5)(Examples 2-5, Comparative Examples 1-5)

공중합성분의 조성은 표 1과 같으며, 실시예 2∼3과 비교예 1은 (1)화합물의 함량을 변화시킨 것이며, 실시예 4, 5, 6은 (1)화합물로써 각각 TiO2, MoO3, SnO2를 Sb2O3로 코팅한 화합물을 사용한 것이며, 비교예 2, 3은 (2)의 화합물 함량을 변화시킨 것이며, 비교예 4는 (1)화합물을 사용하지 않은 것이며, 비교예 5는 (1)과 (2)화합물을 사용하지 않은 것 이외에는 실시예 1과 동일한 방법으로 실시하였다.The composition of the copolymerization components is shown in Table 1, and Examples 2 to 3 and Comparative Example 1 were to change the content of the compound (1), and Examples 4, 5, and 6 were (1) compounds, respectively, TiO 2 and MoO. 3 , a compound coated with SnO 2 with Sb 2 O 3 was used, Comparative Examples 2 and 3 were to change the compound content of (2), Comparative Example 4 is not using the compound (1), Comparative Example 5 was carried out in the same manner as in Example 1 except that Compounds (1) and (2) were not used.

하기 표 1에서 알 수 있는 바와 같이 본 발명에 따른 실시예 1∼6이 비교예 1∼5에 비하여 흡습성, 제전성 및 사물성이 전반적으로 양호함을 알 수 있다.As can be seen in Table 1, Examples 1 to 6 according to the present invention can be seen that the overall hygroscopicity, antistatic properties and the objectability compared to Comparative Examples 1 to 5.

[표 1]TABLE 1

(1), (3), (4) 화합물은 폴리에틸렌테레프탈레이트(PET) 대비 중량%이고, (2)화합물은 SiO2400g대비 중량% 임Compounds (1), (3) and (4) are weight percent based on polyethylene terephthalate (PET), and (2) compounds are weight percent compared to 400 g of SiO 2.

Claims (5)

폴리에틸렌테레프탈레이트(PET)를 사용하여 폴리에스터 섬유를 제조함에 있어서, 공중합시 폴리옥시 알킬렌글리콜화합물, 비반응성 폴리알킬술폰산금속염, 유전율이 높은 하기 식(1)의 금속미립자, SiO2(PET대비 0.1∼10중량%) 및 분산제로써 포스페이트 화합물을 가하여 공중합시켜 수득한 폴리에스터를 사용하는 것을 특징으로 하는 폴리에스터 섬유의 제조방법.In preparing polyester fiber using polyethylene terephthalate (PET), polyoxyalkylene glycol compound, non-reactive polyalkyl sulfonate metal salt during copolymerization, metal fine particles of formula (1) having a high dielectric constant, SiO 2 (compared to PET) 0.1 to 10% by weight) and a polyester obtained by copolymerization by adding a phosphate compound as a dispersing agent is used. MexOy…………………………………………………………………………… (1)MexOy… … … … … … … … … … … … … … … … … … … … … … … … … … … … … (One) (여기에서 Me는 3주기 또는 4주기 전이금속원소 또는 In, Sn, Sb, Ge, Al, Ga중의 1종이고, x, y는 0∼5의 정수이다.)(Me here is a three- or four-cycle transition metal element or one of In, Sn, Sb, Ge, Al, Ga, x, y is an integer of 0-5.) 제1항에 있어서, 금속미립자는 입자크기가 0.001㎛∼1㎛이고, 폴리에틸렌테레프탈레이트의 0.01∼10중량% 투입됨을 특징으로 하는 폴리에스터 섬유의 제조방법.The method for producing a polyester fiber according to claim 1, wherein the metal fine particles have a particle size of 0.001 µm to 1 µm and 0.01 to 10% by weight of polyethylene terephthalate. 제1항에 있어서, 포스페이트 화합물은 하기 식(2)를 만족하는 적어도 1종이고 SiO2대비 0.05∼5중량% 첨가함을 특징으로 하는 폴리에스터 섬유의 제조방법.The method of claim 1, wherein the phosphate compound is at least one member and method of producing a polyester fiber which is characterized by adding 0.05 to 5%, based on the weight of SiO 2 that satisfies the following formula (2). MHn2(PO4) n3………………………………………………………………………(2)MHn 2 (PO 4 ) n 3 . … … … … … … … … … … … … … … … … … … … … … … … … … … (2) (여기에서 M은 K, Na, Ca, Al, NH4중의 1종, n2는 0∼4의 정수, n3는 1∼2의 정수이다.)(Wherein M is one species of K, Na, Ca, Al, NH4, n 2 is an integer of 0 to 4, n 3 is an integer of 1-2.) 제1항에 있어서, 폴리옥시알킬렌글리콜 화합물은 수평균분자량이 2,000 이상이고 30,000 이하인 하기식(3)의 화합물이고, 폴리에틸렌테레프탈레이트 대비 0.01∼3.5중량%를 축중합 시기에 넣어 폴리에스터 주쇄의 말단에 공중합시키는 것을 특징으로 하는 폴리에스터 섬유의 제조방법.The polyoxyalkylene glycol compound according to claim 1, wherein the polyoxyalkylene glycol compound is a compound of formula (3) having a number average molecular weight of 2,000 or more and 30,000 or less, wherein 0.01 to 3.5% by weight of polyethylene terephthalate is added to A method for producing a polyester fiber, characterized in that copolymerized at the end. R1O(R2O) n1H …………………………………………………………………………(3)R 1 O (R 2 O) n 1 H... … … … … … … … … … … … … … … … … … … … … … … … … … … … (3) (여기에서 R1은 C1∼C13인 알킬기 또는 H, R2는 C2∼C13인 알킬렌기, n1은 20∼150의 정수이다.)(Wherein R 1 is C 1 ~C 13 alkyl group or H, R 2 is C 2 ~C 13 alkyl group, n 1 is an integer of 20-150.) 제1항에 있어서, 비반응성 폴리알킬술폰산금속염은 하기 식(4)의 화합물이며 첨가량이 폴리에틸렌테레프탈레이트 대비 0.01∼2중량%임을 특징으로 하는 폴리에스터 섬유의 제조방법.The method of producing a polyester fiber according to claim 1, wherein the non-reactive polyalkylsulfonic acid metal salt is a compound represented by the following formula (4), and the amount added is 0.01 to 2% by weight relative to polyethylene terephthalate. R3SO3Me ………………………………………………………………………………(4)R 3 SO 3 Me... … … … … … … … … … … … … … … … … … … … … … … … … … … … … … (4) (여기에서 R3은 C3∼C25인 알킬기 또는 C7∼C30인 아릴기, Me는 K, Li, Na중의 1종이다.)(Herein, R 3 is C 3 -C 25 alkyl group or C 7 -C 30 aryl group, Me is one of K, Li and Na.)
KR1019930020853A 1993-10-08 1993-10-08 Process for preparing polyester fiber KR970010708B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019930020853A KR970010708B1 (en) 1993-10-08 1993-10-08 Process for preparing polyester fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019930020853A KR970010708B1 (en) 1993-10-08 1993-10-08 Process for preparing polyester fiber

Publications (2)

Publication Number Publication Date
KR950011666A KR950011666A (en) 1995-05-15
KR970010708B1 true KR970010708B1 (en) 1997-06-30

Family

ID=19365491

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019930020853A KR970010708B1 (en) 1993-10-08 1993-10-08 Process for preparing polyester fiber

Country Status (1)

Country Link
KR (1) KR970010708B1 (en)

Also Published As

Publication number Publication date
KR950011666A (en) 1995-05-15

Similar Documents

Publication Publication Date Title
US4158083A (en) Fibrous article sized with a branched water-dispersible polyester
US3557039A (en) Aqueous dispersion of block or graft polymer useful in surface modifying treatment of polyester shaped articles
US3652713A (en) Polyester composition having improved antistatic properties and process for the preparation thereof
US4215026A (en) Aqueous dispersion of a branched polyester
KR970010708B1 (en) Process for preparing polyester fiber
US2974066A (en) Anti-static compositions and synthetic filamentary textile materials treated therewith
KR950008906B1 (en) Method of manufacturing polyester fiber having high anti-static and hygroscopic property
US4336685A (en) Synthetic polymer films and fibers rendered permanently anti-static
KR970010712B1 (en) Process for preparing antistatic polyester fiber
US4470914A (en) Polyoxyalkylene lubricants of improved oxidative stability and lower viscosity
KR970010721B1 (en) Process for preparing antistatic electricity polyester fiber
KR970010706B1 (en) Method for manufacturing an anti-static electricity polyester fiber
KR0152280B1 (en) Process for preparing antistatic polyester fiber
KR970010722B1 (en) Process for preparing antistatic polyester fiber
JP3086507B2 (en) Thermoplastic synthetic resin molded product
CA1111187A (en) Self-extinguishing and thermostable copolyesters and process for making the same
KR970010707B1 (en) Process for preparing antistatic electricity polyester fiber
KR0164449B1 (en) Manufacturing method of polyester fiber with antistatic property
KR0125968B1 (en) Manufacturing method of modified polyester fiber
MY108689A (en) Curable composition
US3910867A (en) Shaped structures of acrylonitrile polymers with permanent antistatic properties
KR940007689B1 (en) Process for preparation of polyester fiber
KR100295014B1 (en) Manufacturing method of antistatic polyester fiber
CA1095071A (en) Thermostable flameproofing agent for copolyesters, process for making it, copolyester compositions prepared by using it, process for making said compositions and formed bodies made from said compositions
KR900004914B1 (en) Manufacturing process of polyester 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: 20120619

Year of fee payment: 16

EXPY Expiration of term