KR100510766B1 - Island-in-the-sea microfiber - Google Patents
Island-in-the-sea microfiber Download PDFInfo
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- KR100510766B1 KR100510766B1 KR1019980010636A KR19980010636A KR100510766B1 KR 100510766 B1 KR100510766 B1 KR 100510766B1 KR 1019980010636 A KR1019980010636 A KR 1019980010636A KR 19980010636 A KR19980010636 A KR 19980010636A KR 100510766 B1 KR100510766 B1 KR 100510766B1
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- Prior art keywords
- sea
- component
- island
- microfiber
- elution
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- 229920001410 Microfiber Polymers 0.000 title claims abstract description 36
- 239000003658 microfiber Substances 0.000 title claims abstract description 36
- -1 polytrimethylene terephthalate Polymers 0.000 claims abstract description 36
- 238000004043 dyeing Methods 0.000 claims abstract description 24
- 229920002215 polytrimethylene terephthalate Polymers 0.000 claims abstract description 24
- 229920000728 polyester Polymers 0.000 claims abstract description 20
- 238000010828 elution Methods 0.000 claims abstract description 14
- 239000003513 alkali Substances 0.000 claims abstract description 13
- 239000000986 disperse dye Substances 0.000 claims abstract description 6
- 229920001577 copolymer Polymers 0.000 claims abstract 2
- 229920001634 Copolyester Polymers 0.000 claims description 8
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 8
- 239000005020 polyethylene terephthalate Substances 0.000 claims description 8
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 6
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 claims description 4
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 3
- 238000006068 polycondensation reaction Methods 0.000 claims 1
- 239000002649 leather substitute Substances 0.000 abstract description 9
- 230000014759 maintenance of location Effects 0.000 abstract description 6
- 230000000704 physical effect Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000000605 extraction Methods 0.000 abstract description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 15
- 239000000975 dye Substances 0.000 description 8
- 238000009987 spinning Methods 0.000 description 8
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- 239000004952 Polyamide Substances 0.000 description 6
- 238000004090 dissolution Methods 0.000 description 6
- 229920002647 polyamide Polymers 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 229920002635 polyurethane Polymers 0.000 description 5
- 239000004814 polyurethane Substances 0.000 description 5
- 238000011084 recovery Methods 0.000 description 5
- 235000011121 sodium hydroxide Nutrition 0.000 description 5
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 239000004745 nonwoven fabric Substances 0.000 description 4
- 229920001707 polybutylene terephthalate Polymers 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 230000009477 glass transition Effects 0.000 description 2
- 210000004209 hair Anatomy 0.000 description 2
- 238000010030 laminating Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- DNIAPMSPPWPWGF-VKHMYHEASA-N (+)-propylene glycol Chemical compound C[C@H](O)CO DNIAPMSPPWPWGF-VKHMYHEASA-N 0.000 description 1
- YPFDHNVEDLHUCE-UHFFFAOYSA-N 1,3-propanediol Substances OCCCO YPFDHNVEDLHUCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 238000010009 beating Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920000166 polytrimethylene carbonate Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/28—Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
- D01D5/30—Conjugate filaments; Spinnerette packs therefor
- D01D5/34—Core-skin structure; Spinnerette packs therefor
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
- D01F8/14—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
- Chemical Or Physical Treatment Of Fibers (AREA)
- Multicomponent Fibers (AREA)
Abstract
본 발명은 100℃ 이하에서 분산염료 염색이 가능하고, 해성분 용출후의 강도등 물성이 우수한 해도형 극세사에 관한 것이다.The present invention relates to a island-in-the-sea microfiber yarn capable of dyeing disperse dyes at 100 ° C. or lower and excellent in physical properties such as strength after sea component elution.
본 발명의 해도형 극세사는 알칼리 이용해성(易溶解性)이 우수한 공중합 폴리에스테르인 용출성분(해성분) 10∼60중량%와 폴리트리메틸렌 테레프탈레이트인 비용출성분(도성분) 90∼40중량%로 구성되며, 용출성분(해성분) 용출후 해도형 극세사의 강도 유지율이 80% 이상이다.The island-in-the-sea type microfiber of the present invention is 10 to 60% by weight of an elution component (sea component), which is a copolymer polyester having excellent alkali solubility, and 90 to 40% by weight of a non-extraction component, which is polytrimethylene terephthalate. It is composed of%, the elution component (sea component) The strength retention rate of the island-in-the-sea microfiber after elution is 80% or more.
본 발명의 해도형 극세사는 인공피혁 등의 제조에 유용하다.The island-in-the-sea microfiber of the present invention is useful for the manufacture of artificial leather and the like.
Description
본 발명은 인공피혁용 원사로 사용되는 해도형 극세사에 관한 것이다.The present invention relates to an island-in-the-sea microfiber yarn used as an artificial leather yarn.
인공피혁, 와이핑 원단 및 기능성 소재로 널리 사용되는 해도형 극세사는 용제 용해성이 다른 2종 이상의 폴리머를 복합방사한 후 적어도 1성분을 용제로서 용해하여 얻을 수 있다. 지금까지는 용출성분(해성분) 즉, 용제에 의해 용해되는 폴리머로는 공중합 폴리에스테르, 폴리스티렌 또는 폴리에틸렌 등이 주로 사용되고 있다. 그러나 그중에서도 알칼리 용해성이 우수한 공중합 폴리에스테르가 용출성분(해성분)으로 가장 적합하다. 그 이유로는 폴리스티렌 또는 폴리에틸렌은 유기 용제에 의해서만 용해가 가능하므로 용제 가격상승 및 작업시 위험성 등의 단점이 있기 때문이다. 공중합 폴리에스테르는 테레프탈산과 에틸렌 글리콜을 주성분으로 하고, 여기에 이소프탈산, 5-소디움 술포이소프탈산 및 / 또는 폴리에틸렌글리콜 3∼20 몰%가 공중합된 것으로서 일반 폴리에스테르에 비해 알칼리 용해성이 약 5배 이상 향상되는 것으로 알려져 있다.The island-in-the-sea type microfiber widely used as an artificial leather, a wiping fabric, and a functional material may be obtained by dissolving at least one component as a solvent after complex spinning two or more kinds of polymers having different solvent solubility. Until now, co-polyester, polystyrene, polyethylene, etc. are mainly used as an eluting component (sea component), ie, the polymer melt | dissolved by a solvent. Among them, however, copolyesters having excellent alkali solubility are most suitable as elution components (sea components). The reason is that the polystyrene or polyethylene can be dissolved only by the organic solvent, so there are disadvantages such as the increase in the solvent price and the risk in operation. Copolyester is composed mainly of terephthalic acid and ethylene glycol, and isophthalic acid, 5-sodium sulfoisophthalic acid, and / or 3 to 20 mol% of polyethylene glycol is copolymerized, and alkali solubility is about 5 times higher than that of general polyester. It is known that the above improvement.
한편 지금까지 용제에 용해되지 않는 비용출성분(도성분)은 폴리아미드, 개질 폴리아미드, 폴리에스테르 또는 개질 폴리에스테르 등이 사용되고 있다.On the other hand, polyamide, modified polyamide, polyester, modified polyester, etc. are used as a non-extractable component (doe component) which is not melt | dissolved in a solvent until now.
용출성분(해성분)이 상기 공중합 폴리에스테르이고, 비용출성분(도성분)이 폴리에스테르 또는 개질 폴리에스테르로 구성된 종래의 해도형 극세사는 다음과 같은 문제가 있다.Conventional islands-in-the-sea microfine yarns in which the elution component (sea component) is the co-polyester and the non-extraction component (conductive component) are composed of polyester or modified polyester have the following problems.
첫째, 비용출성분(도성분)인 폴리에스테르 또는 개질 폴리에스테르가 용출성분(해성분) 용출시 알칼리에 취하되어 물성이 저하되고, First, polyester or modified polyester, which is a non-eject component (isolated component), is dissolved in an alkali when eluting the eluted component (sea component), thereby deteriorating physical properties,
둘째, 비용출성분(도성분)인 폴리에스테르의 염색특성상 고온염색이 필요하여 염색이 복잡함과 동시에 고온염색으로 인공피혁의 입모가 손상되고Second, high temperature dyeing is required for the dyeing characteristics of polyester, which is a non-exhaust ingredient (composition), which makes the dyeing complex and damages the artificial leather's hair by high temperature dyeing.
셋째, 폴리에스테르의 낮은 탄성회복율에 기인하여 반발특성이 저하되는 등의 문제가 있다.Third, due to the low elastic recovery rate of the polyester, there is a problem that the repulsion characteristics are lowered.
따라서 본 발명의 목적은 상기와 같은 종래의 문제점들을 해결할 수 있는 새로운 해도형 극세사를 제공하는 것이다.Accordingly, an object of the present invention is to provide a new island-in-the-sea microfiber that can solve the above problems.
본 발명은 용출성분(이하 "해성분〃이라고 한다.) 용출후의 해도형 극세사의 강도 유지율이 80% 이상이고, 탄성회복율 및 세팅성 등의 물성이 우수하고, 100℃ 이하에서 분산염료 염색이 가능하며, 염색견뢰도가 향상된 해도형 극세사를 제공하고자 한다.The present invention is an elution component (hereinafter referred to as "sea component))) The strength retention rate of the island-in-the-sea microfiber after elution is 80% or more, and excellent in physical properties such as elastic recovery rate and setting property, and disperse dye dyeing is possible at 100 ° C or less. In addition, it is intended to provide an island-in-the-sea microfiber yarn with improved color fastness.
본 발명은 인공피혁용 원사 등으로 사용되는 해도형 극세사에 관한 것이다.The present invention relates to an island-in-the-sea microfiber yarn used as an artificial leather yarn or the like.
더욱 구체적으로 본 발명은 알칼리 이용해성(易溶解性)이 우수한 공중합 폴리에스테르인 해성분 10∼60중량%와 폴리트리메틸렌 테레프탈레이트인 도성분 90∼40중량%로 구성되며, 해성분 용출후 해도형 극세사의 강도유지율이 80% 이상이고, 100℃ 이하에서 분산염료 염색이 가능한 것을 특징으로 하는 해도형 극세사에 관한 것이다.More specifically, the present invention comprises 10 to 60% by weight of sea component, which is a copolyester having excellent alkali solubility, and 90 to 40% by weight of island component, which is polytrimethylene terephthalate. It relates to an island-in-the-sea microfiber yarn, characterized in that the strength retention rate of the microfiber yarn is 80% or more, and disperse dye dyeing is possible at 100 ° C or lower.
본 발명은 종래 해도형 극세사의 문제점들을 해결하기 위해서 해도형 극세사를 복합방사할 때 도성분으로 폴리에틸렌 테레프탈레이트(PET)와 폴리부틸렌 테레프탈레이트(PBT) 중간의 탄소수를 갖고 폴리아미드와 유사한 탄성회복율을 가지면서 내알칼리성이 뛰어나고 저온염색성 및 염색견뢰도가 우수한 폴리트리메틸렌 테레프탈레이트를 사용함을 특징으로 한다.In order to solve the problems of conventional islands-in-the-sea microfibers, the present invention has an elastic recovery rate similar to that of polyamide, having a carbon number between polyethylene terephthalate (PET) and polybutylene terephthalate (PBT) While having excellent alkali resistance and excellent low-temperature dyeing and dyeing fastness is characterized by using a polytrimethylene terephthalate.
이하 본 발명을 상세하게 설명하기로 한다.Hereinafter, the present invention will be described in detail.
본 발명의 해도형 극세사는 해성분인 알칼리 이용해성 공중합 폴리에스테르와 도성분인 폴리트리메틸렌 테레프탈레이트를 통상의 해도형 복합섬유용 구금장치로 복합방사한 후 연신하여 제조된다. 복합방사시 해성분은 10∼60중량%까지, 도성분은 90∼40중량%까지 사용가능하나, 해성분을 20∼50중량%, 도성분을 80∼50중량% 사용하는 것이 더욱 바람직하다.The island-in-the-sea-type microfiber of the present invention is prepared by complex spinning of an alkali-soluble co-polyester as a sea component and a polytrimethylene terephthalate as a island component by a conventional spinning device for island-in-the-sea composite fiber. The sea component can be used up to 10 to 60% by weight and the island component can be up to 90 to 40% by weight, but it is more preferable to use 20 to 50% by weight of the sea component and 80 to 50% by weight of the sea component.
또한 도성분은 해도형 극세사를 구성하는 각 필라멘트의 단면에 적어도 10개 이상 각각 분리되어 배열되고 섬유축 길이방향에 연속하여 있으며, 해성분 용출후의 도성분 한 개의 섬도는 0.01∼0.25 데니어인 것이 바람직하다.In addition, the island component is arranged separately in the cross section of each filament constituting the island-in-the-sea fine microfiber, and is continuous in the longitudinal direction of the fiber axis, the fineness of one island component after sea component elution is preferably 0.01 to 0.25 denier Do.
본 발명의 해도형 극세사는 스테이플 섬유 및 필라멘트 섬유를 모두 포함한다.The island-in-the-sea microfiber of the present invention includes both staple fibers and filament fibers.
본 발명에서 도성분으로 사용되는 폴리트리메틸렌 테레프탈레이트는 테레프탈산 또는 디메틸테레프탈레이트와 1,3-프로판디올을 축중합하여 제조되며 식(Ⅰ)와 같은 구조식을 갖는다.Polytrimethylene terephthalate to be used as a component in the present invention is prepared by condensation polymerization of terephthalic acid or dimethyl terephthalate and 1,3-propanediol and has a structural formula (I).
폴리트리메틸렌 테레프탈레이트는 중합방법 및 화학적 구조가 폴리에틸렌 테레프탈레이트와 매우 유사하지만 열적, 기계적 특성에 있어서는 많은 차이가 있다.Polytrimethylene terephthalate has a very similar polymerization method and chemical structure to polyethylene terephthalate, but there are many differences in thermal and mechanical properties.
폴리트리메틸렌 테레프탈레이트는 폴리에틸렌 테레프탈레이트나 폴리부틸렌 테레프탈레이트에 비해 특히 신축성, 촉감, 내알칼리성 및 염색성 등이 우수하다.Polytrimethylene terephthalate is superior in polyethylene terephthalate and polybutylene terephthalate in particular in elasticity, touch, alkali resistance and dyeing property.
폴리트리메틸렌 테레프탈레이트는 초기 모듈러스가 나일론 수준으로 비교적 낮아 소프트한 촉감을 나타낸다. 그 결과 폴리에틸렌 테레프탈레이트와 같이 촉감을 개선하기 위한 알칼리 감량 가공이 필요없게 된다.Polytrimethylene terephthalate exhibits a soft hand with a relatively low initial modulus to nylon levels. As a result, there is no need for alkali weight loss processing to improve the feel, such as polyethylene terephthalate.
또한 폴리트리메틸렌 테레프탈레이트는 신축성 및 내알칼리성이 매우 우수하며, 100℃ 이하에서 분산염료 염색이 가능하며, 염색 견뢰도도 매우 우수하다.In addition, polytrimethylene terephthalate has excellent elasticity and alkali resistance, it is possible to dye disperse dyes at less than 100 ℃, dyeing fastness is also very good.
폴리트리메틸렌 테레프탈레이트는 유리전이 온도가 45℃∼65℃로 폴리아미드와 유사하고, 용융점은 228℃이다.Polytrimethylene terephthalate has a glass transition temperature of 45 ° C. to 65 ° C., similar to polyamide, and a melting point of 228 ° C.
결정화 온도는 65℃ 수준이고 결정화 속도는 빠르다. 또한 300℃ 이상의 고온에서는 열분해된다.The crystallization temperature is at 65 ° C. and the crystallization rate is fast. Moreover, it decomposes thermally at high temperature 300 degreeC or more.
이와 같은 열적 특성으로 인해 폴리트리메틸렌 테레프탈레이트는 일반 방사 및 연신기대에서 무리없이 방사, 연신할 수 있다. 연신 온도는 60℃∼160℃, 연신배율은 2.5∼3.5 정도가 무난하다.Due to these thermal properties, polytrimethylene terephthalate can be easily spun and stretched in the normal spinning and stretching zone. The stretching temperature is 60 ° C to 160 ° C and the stretching magnification is about 2.5 to 3.5.
한편 폴리트리메틸렌 테레프탈레이트의 기계적 물성으로는 복굴절율이 0.073이고, 밀도가 1.33g/㎠이고, 공정수분율이 0.15이고, 강도 및 신도는 폴리아미드와 유사하다. 본 발명의 해도형 극세사는 상기 폴리트리메틸렌 테레프탈레이트를 도성분으로 사용하기 때문에 종래 폴리에스테르 또는 개질 폴리에스테르를 도성분으로 사용한 해도형 극세사의 여러 문제점들을 해결할 수 있다.On the other hand, the mechanical properties of polytrimethylene terephthalate are birefringence of 0.073, density of 1.33 g / cm 2, process water content of 0.15, and strength and elongation are similar to those of polyamide. Since the island-in-the-sea microfiber of the present invention uses the polytrimethylene terephthalate as the island component, various problems of the island-in-the-sea microfiber yarn using the conventional polyester or modified polyester as the island component can be solved.
구체적으로 도성분이 폴리에스테르 또는 개질 폴리에스테르인 종래 해도형 극세사의 경우 해성분 용출시 도성분이 알칼리에 취화되어 물성이 저하되므로, 제품 물성을 중요시하는 가구용 등의 인공피혁 제조시 강도 보강을 위해 인공피혁 이면에 직물을 라미네이팅하거나 코팅작업을 해야하므로 제조공정이 복잡해지고 제조원가가 상승하게 된다. 그러나 본 발명은 폴리트리메틸렌 테레프탈레이트의 내알칼리성이 일반 폴리에스테르에 비해 3배 정도 강하므로 이와 같은 단점을 보완할 수 있다. 그 결과 해성분 용출 후의 해도형 극세사의 강도유지율은 80% 이상이다. 해도형 극세사의 강도유지율은 다음과 같이 구한다. Specifically, in the case of conventional island-in-the-sea type microfibers in which the island component is a polyester or a modified polyester, since the island component is embrittled in alkali when the sea component is eluted, the physical properties thereof are deteriorated. Laminating or coating the fabric on the back side requires complicated manufacturing processes and increases manufacturing costs. However, since the alkali resistance of the polytrimethylene terephthalate is about three times stronger than that of general polyester, the present invention can compensate for this disadvantage. As a result, the strength retention rate of the island-in-the-sea microfiber after elution of the sea component is 80% or more. The strength maintenance rate of island-in-the-sea microfiber is calculated as follows.
해도형 극세사의 강도유지율 (%) = t 100 Strength retention rate of islands-in-the-sea microfiber (%) = t 100
여기서 A는 95℃의 가성소오다 수용액 (3% 농도)에서 5분간 처리한 해도형 극세사의 강도이고, B는 상기 가성소오다 수용액에서 처리하기전 해도형 극세사의 강도이다. Where A is the strength of the island-in-the-sea microfiber yarn treated for 5 minutes in an aqueous solution of caustic sodium hydroxide (3% concentration) at 95 ° C., and B is the strength of the island-in-the-sea microfiber yarn before treatment in the aqueous solution of caustic soda.
또한 상기 종래 해도형 극세사의 경우 도성분의 평균섬도가 0.05 데니어 수준의 극세사이고, 폴리에스테르의 염색성이 나쁘기 때문에 선명한 농색을 발현하는 것과 염색견뢰도를 적정 수준으로 유지하는 것이 매우 곤란하다. 따라서 염색성을 향상시키기 위해 염색시 강제 비팅 및 고온 염색조건을 적용하기 때문에 인공피혁 표면의 입모가 손상되기 쉬우며, 폴리우레탄의 취화가 발생할 수 있어 폴리우레탄의 선정에 제약이 많은 실정이다. 그러나 본 발명은 도성분인 폴리트리메틸렌 테레프탈레이트가 100℃ 이하에서 뛰어난 염색성을 갖고 있고 염색견뢰도도 우수한 장점이 있다.In the case of the conventional islands-in-the-sea microfiber, the average fineness of the island component is a microfiber of the level of 0.05 denier, and since the dyeability of the polyester is poor, it is very difficult to express vivid dark colors and maintain the dyeing fastness at an appropriate level. Therefore, forced beating and high-temperature dyeing conditions are applied during dyeing to improve dyeability, and thus, the surface of artificial leather is easily damaged, and embrittlement of polyurethane may occur, and thus there are many limitations in the selection of polyurethane. However, the present invention has an excellent dyeability of polytrimethylene terephthalate as an island component at 100 ° C. or less, and also has excellent dyeing fastness.
그리고 폴리트리메틸렌 테레프탈레이트는 유리전이 온도가 45∼65℃로서 폴리아미드와 유사하고, 폴리부틸렌 테레프탈레이트보다는 높은 특징으로 탄성회복율이 우수함과 동시에 세팅성도 양호하고, 반발 탄성이 우수하여 본 발명의 해도형 극세사는 다양한 용도의 인공피혁용 원사로 사용될 수 있다.In addition, polytrimethylene terephthalate has a glass transition temperature of 45-65 ° C., similar to polyamide, and is higher than polybutylene terephthalate, and has excellent elastic recovery rate, good setting property, and excellent resilience. The island-in-the-sea microfiber yarn can be used as an artificial leather yarn for various purposes.
실시예 및 비교실시예를 통해 본 발명을 더욱 구체적으로 살펴본다. 그러나 본 발명이 하기 실시예에만 한정되는 것은 아니다.The present invention will be described in more detail through Examples and Comparative Examples. However, the present invention is not limited only to the following examples.
실시예 1Example 1
메틸렌 클로라이드와 트리플로로아세틱 액시드가 50:50인 30℃ 용액에서 측정한 고유점도가 0.88인 폴리트리메틸렌 테레프탈레이트를 도성분으로 사용하여, 이를 온도가 260℃인 도성분 압출기에서 용융한다.Polytrimethylene terephthalate having an intrinsic viscosity of 0.88 measured in a 30 ° C. solution of 50:50 methylene chloride and trifluoroacetic acid is used as a island component and melted in a island-based extruder having a temperature of 260 ° C. .
한편 알칼리 이용해성 공중합 폴리에스테르를 해성분으로 사용하여, 이를 온도가 285℃인 해성분 압출기에서 용융한다.On the other hand, using an alkali-soluble copolyester as a sea component, it is melted in a sea component extruder having a temperature of 285 ℃.
각각 압출기에서 용융된 도성분(폴리트리메틸렌 테레프탈레이트)과 해성분(알칼리 이용해성 공중합 폴리에스테르)를 70:30의 중량비로 온도가 285℃이고 도성분의 개수가 36개인 해도형 복합섬유용 방사구금에 공급하여 복합방사한 다음 1,200m/분의 권취속도로 미연신사를 제조한다. 계속해서 미연신사를 3.6배의 연신배율로 연신한 후 51㎜의 스테이플을 제조한 다음 이들을 NaOH 3% 수용액에서 3, 5, 10, 20분간 처리하여 해성분을 용출한다. 해성분 용출 전,후의 스테이플 강도를 측정한 결과는 표 1과 같다.Spinning of the island component (polytrimethylene terephthalate) and the sea component (alkali-soluble copolyester) melted in an extruder, respectively, with a weight ratio of 70:30 at a temperature of 285 ° C. and 36 islands After supplying to the prison complex spinning, undrawn yarn is produced at a winding speed of 1,200m / min. Subsequently, after stretching the undrawn yarn at a draw ratio of 3.6 times, 51 mm staples are prepared, and these are treated in 3, 5, 10, and 20 minutes in an NaOH 3% aqueous solution to elute the sea component. Table 1 shows the results of measuring the staple strength before and after dissolution of the sea component.
실시예 2Example 2
메틸렌 클로라이드와 트리플로로아세틱 액시드가 50:50인 30℃ 용액에서 측정한 고유점도가 0.88인 폴리트리메틸렌 테레프탈레이트를 도성분으로 사용하여, 이를 온도가 260℃인 도성분 압출기에서 용융한다.Polytrimethylene terephthalate having an intrinsic viscosity of 0.88 measured in a 30 ° C. solution of 50:50 methylene chloride and trifluoroacetic acid is used as a island component and melted in a island-based extruder having a temperature of 260 ° C. .
한편 알칼리 이용해성 공중합 폴리에스테르를 해성분으로 사용하여, 이를 온도가 285℃인 해성분 압출기에서 용융한다.On the other hand, using an alkali-soluble copolyester as a sea component, it is melted in a sea component extruder having a temperature of 285 ℃.
각각 압출기에서 용융된 도성분(폴리트리메틸렌 테레프탈레이트)과 해성분(알칼리 이용해성 공중합 폴리에스테르)를 70:30의 중량비로 온도가 285℃이고 도성분의 개수가 36개인 해도형 복합섬유용 방사구금에 공급하여 복합방사한 다음 1,200m/분의 권취속도로 미연신사를 제조한다. 계속해서 미연신사를 3.6배의 연신배율로 연신한 후 51㎜의 스테이플을 제조한 다음 오프닝, 카딩하여 중량이 400g/㎡인 부직포를 제조한다.Spinning of the island component (polytrimethylene terephthalate) and the sea component (alkali-soluble copolyester) melted in an extruder, respectively, with a weight ratio of 70:30 at a temperature of 285 ° C. and 36 islands After supplying to the prison complex spinning, undrawn yarn is produced at a winding speed of 1,200m / min. Subsequently, the non-drawn yarn is drawn at a draw ratio of 3.6 times, and then a 51 mm staple is produced, and then opened and carded to produce a nonwoven fabric having a weight of 400 g / m 2.
상기 부직포에 폴리우레탄을 함침한 다음, NaOH 3% 수용액으로 부직포내 해성분을 용출한다. 계속해서 이들을 버핑한 다음 미케톤(MIKETONE) 레드 FB (스미토모사 제품) 염료를 8% owf 사용하여 염색한다. 이때 염색온도에 따른 염료 잔류양을 측정한 결과는 표 2와 같다.The nonwoven fabric is impregnated with polyurethane, and the sea component in the nonwoven fabric is eluted with an aqueous NaOH 3% solution. They are then buffed and then stained with 8% owf of the MIKETONE Red FB (Sumitomosa) dye. At this time, the result of measuring the dye residual amount according to the dyeing temperature is shown in Table 2.
비교실시예 1Comparative Example 1
오르토클로로페놀 25℃ 용액에서의 고유점도가 0.65인 일반 폴리에틸렌 테레프탈레이트를 도성분으로 사용한 것을 제외하고는 실시예 1과 동일한 공정 및 조건으로 스테이플을 제조하고, NaOH 3% 수용액에서 해성분을 용출한다. 해성분 용출 전,후의 스테이플 강도를 측정한 결과는 표 1과 같다.A staple was prepared in the same process and conditions as in Example 1 except that general polyethylene terephthalate having an intrinsic viscosity of 0.65 in a 25 ° C. solution of orthochlorophenol was used as a island component, and the sea component was eluted in an aqueous NaOH 3% solution. . Table 1 shows the results of measuring the staple strength before and after dissolution of the sea component.
비교실시예 2Comparative Example 2
오르토클로로페놀 25℃ 용액에서의 고유점도가 0.65인 일반 폴리에틸렌 테레프탈레이트를 도성분으로 사용한 것을 제외하고는 실시예 2와 동일한 공정 및 조건으로 부직포를 제조한 다음 폴리우레탄 함침, 해성분 용출, 버핑 및 염색한다.Non-woven fabrics were prepared in the same process and conditions as in Example 2, except that general polyethylene terephthalate having an intrinsic viscosity of 0.65 in a 25 ° C. solution of orthochlorophenol was used as a component, followed by polyurethane impregnation, dissolution of sea components, buffing and Dye
이때 염색온도에 따른 염료 잔류양을 측정한 결과는 표 2와 같다.At this time, the result of measuring the dye residual amount according to the dyeing temperature is shown in Table 2.
< 표 1 > 용출시간에 따른 용출 전,후의 스테이플 강도 측정 결과<Table 1> Staple strength measurement results before and after dissolution according to dissolution time
< 표 2 > 염색온도에 따른 염료 잔류량 측정 결과<Table 2> Result of Dye Residue Measurement by Dyeing Temperature
본 발명의 해도형 극세사는 도성분인 폴리트리메틸렌 테레프탈레이트의 내알칼리성이 우수하여 해성분 용출후 해도형 극세사의 강도유지율이 80% 이상이다. 따라서 본 발명의 해도형 극세사로 제품 물성을 중요시하는 가구용 인공피혁을 제조하는 경우, 종래 강도 등의 물성 보강을 위해 인공피혁 이면에 직물을 라미네이팅하거나 코팅하는 공정을 생략할 수 있어서 원가절감이 가능하다.The island-in-the-sea microfiber of the present invention is excellent in alkali resistance of polytrimethylene terephthalate as an island component, and the strength retention rate of the island-in-the-sea island microfiber after elution of sea component is 80% or more. Therefore, in the case of manufacturing artificial leather for furniture that emphasizes product properties with island-in-the-sea microfiber of the present invention, it is possible to omit the process of laminating or coating the fabric on the back side of artificial leather in order to reinforce physical properties such as conventional strength. .
또한 본 발명의 해도형 극세사중 도성분인 폴리트리메틸렌 테레프탈레이트가 뛰어난 염색성을 갖고 있어서 100℃ 이하에서 분산염료 염색이 가능하다.In addition, polytrimethylene terephthalate, an island component of the island-in-the-sea microfiber of the present invention has excellent dyeing property, and disperse dye dyeing is possible at 100 ° C or lower.
따라서 폴리우레탄의 선정 폭이 넓어질 수 있으며, 염색시 발생할 수 있는 표면 입모의 손상을 방지할 수 있어 자외선, 오존 등에 대한 염색견뢰도도 우수하다.Therefore, the range of selection of polyurethane can be widened, and it is possible to prevent damage to surface hairs that may occur during dyeing, and thus dyeing fastness against ultraviolet rays and ozone is also excellent.
한편 본 발명의 해도형 극세사는 탄성회복율 및 세팅성이 우수하여 다양한 용도에 유용하게 사용될 수 있다.Meanwhile, the island-in-the-sea type microfiber of the present invention has excellent elastic recovery rate and setting property, and thus may be usefully used in various applications.
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KR100546222B1 (en) * | 1998-09-15 | 2006-05-03 | 주식회사 새 한 | Manufacturing method of deep color polyester islands-in-the-sea microfiber |
KR100534519B1 (en) * | 1998-09-18 | 2006-03-14 | 주식회사 코오롱 | An island-in-the-sea microfiber excellent in crimping property and its manufacturing method. |
KR20010044149A (en) * | 2000-11-27 | 2001-06-05 | 구광시 | A sea-island typed composit fiber used in warp knitting, and a process of preparing for the same |
KR100426590B1 (en) * | 2001-11-02 | 2004-04-08 | 주식회사 코오롱 | A sea-island typed conjugate fiber with excellent elasticity recovery |
KR20050073909A (en) * | 2004-01-12 | 2005-07-18 | 주식회사 휴비스 | Ultra fine conjugate ptt fibers for artificial leather and manufacturing method thereof |
ATE478986T1 (en) * | 2004-03-30 | 2010-09-15 | Teijin Fibers Ltd | COMPOSITE FIBER AND FLAT COMPOSITE GOODS OF THE SEA ISLAND TYPE AND METHOD FOR THE PRODUCTION THEREOF |
KR100660934B1 (en) * | 2004-11-25 | 2006-12-26 | 주식회사 새 한 | Polylactic acid island-type microfiber and manufacturing method |
KR100783801B1 (en) * | 2007-02-05 | 2007-12-07 | 주식회사 새 한 | Alkali-soluble polymer extraction type polytrimethylene terephthalate yarn and polytrimethylene terephthalate yarn prepared therefrom |
KR100808567B1 (en) * | 2007-04-30 | 2008-02-29 | 성안합섬주식회사 | Volume yarn using a soluble polyester resin and a method for producing the fiber product |
KR102200706B1 (en) * | 2019-12-09 | 2021-01-11 | 주식회사 자인 | Sea-island type composite yarn using recycled PET and manufacturing method thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19980025671A (en) * | 1996-10-04 | 1998-07-15 | 이명환 | Manufacturing method of polyester islands-in-the-sea composite fiber |
-
1998
- 1998-03-27 KR KR1019980010636A patent/KR100510766B1/en not_active IP Right Cessation
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR19980025671A (en) * | 1996-10-04 | 1998-07-15 | 이명환 | Manufacturing method of polyester islands-in-the-sea composite fiber |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101372016B1 (en) | 2013-02-14 | 2014-03-14 | 성안합섬주식회사 | Island-in-sea type conjugated fiber for textile having excellent spinning properties and weavability and preparation method thereof |
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KR19990076028A (en) | 1999-10-15 |
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