KR900005002B1 - Manufacturing process of nonwoven fabric felt - Google Patents

Manufacturing process of nonwoven fabric felt Download PDF

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Publication number
KR900005002B1
KR900005002B1 KR1019870013576A KR870013576A KR900005002B1 KR 900005002 B1 KR900005002 B1 KR 900005002B1 KR 1019870013576 A KR1019870013576 A KR 1019870013576A KR 870013576 A KR870013576 A KR 870013576A KR 900005002 B1 KR900005002 B1 KR 900005002B1
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South Korea
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felt
component
web
fiber
density
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KR1019870013576A
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Korean (ko)
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KR890008379A (en
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정수송
김우종
박세웅
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주식회사 코오롱
이강철
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    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/005Synthetic yarns or filaments
    • D04H3/009Condensation or reaction polymers
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/10Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between yarns or filaments made mechanically

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nonwoven Fabrics (AREA)

Abstract

A process for mfg. a long staple nonwoven fabric felt comprises spinning two component conjugated yarn having a reciprocal parallel sections, passing the yarn through the enclosed tube of 1.5-4.5 bar of gas stream to form a long staple web, needlepunching the web to be 0.23-0.32 g/cm3, and slack-heating it in the hot bath. The conjugated yarn comprises a high shrinkable copolymeric polyester resin contg. 85-95 mol.% of polyethyleneterephthalate and a polyamide resin. The felt has a good tensile and exfoliation strength, and is used in the mfr. of artificial leathers.

Description

장섬유 부직포 펠트(FELT)의 제조방법Manufacturing method of long fiber nonwoven felt (FELT)

제1도는 본 발명에 사용되는 장치의 예시도.1 is an illustration of an apparatus used in the present invention.

제2도의 (a)는 분할·수축처리전의 장섬유 부직포 웹의 부분확대도.Fig. 2 (a) is a partially enlarged view of the long fiber nonwoven web before division and shrinkage treatment.

(b)는 분할·수축처리전의 장섬유 부직포 웹의 단사확대 단면도.(b) is a single yarn enlarged cross-sectional view of a long fiber nonwoven web before division and shrinkage treatment.

제3도의 (a)는 분할·수축처리후의 장섬유 부직포 펠트의 부분확대도.(A) of FIG. 3 is a partial enlarged view of the long fiber nonwoven felt after division and shrinkage treatment.

(b)는 분할·수축처리후의 극세화된 장섬유의 단사확대 단면도.(b) is a single enlarged cross-sectional view of the ultrafine long fibers after split and shrink treatment.

* 도면의 주요부분에 대한 부호의 설명* Explanation of symbols for main parts of the drawings

1,1' : 각성분 폴리머의 용융장치 2 : 스핀블록(Spin Block)1,1 ': Melting device of each component polymer 2: Spin Block

3 : 밀폐형 관 3' : 공기류유입구3: sealed tube 3 ': air flow inlet

4 : 장섬유 웹(Web) 5 : 콘베어네트4: Long Fiber Web 5: Conveyor Net

6 : 니들펀칭끼 7 : 이완열처리욕조6: needle punching 7: relaxation heat treatment bath

8 : 권취기 9 : 개섬장치8: Winding machine 9: Opening device

본 발명은 복합방사 기술과 부직포 제조기술을 이용하여 제반 물리적성질이 우수한 인공피혁, 특히 스웨드조 인공피혁 제조용 장섬유 부직포 펠트의 제조방법에 관한 것으로서, 특히 극세사로 되고 고밀도화된 장섬유 부직포 펠트의 제조방법에 관한 것이다. 종래부터 인공피혁, 특히 스웨드조 인공피혁을 제조함에 있어서 직물·편물·부직포등을 이용하는 방법이 다수 제안되어 왔다.The present invention relates to a method for producing a long-fiber nonwoven felt for manufacturing artificial leather, especially suede artificial leather, having excellent physical properties by using a composite spinning technique and a nonwoven fabric manufacturing technique. It is about a method. Background Art Conventionally, a number of methods using woven fabrics, knitted fabrics, nonwoven fabrics, etc. have been proposed in the manufacture of artificial leather, in particular, suede artificial leather.

직물·편물을 이용하는 방법은 제직·제편 방법으로 형성시킨 섬유구조물에 직접 기모하거나 또는 입모구조물에 폴리우레탄등의 고분자 탄성체를 처리한 다음 버핑(Buffing)하는 방법이며, 부직포를 이용하는 방법으로는 일반 단섬유를 3차원화 시킨 섬유질 재료에 탄성 고분자물질 또는 이를 주체로 하는 고분자물질의 용액 또는 에멀젼에 함침 또는 도포함으로써 목적물을 얻는 방법이 있고 2종 또는 2종이상의 용해성이 다른 고분자 물질로 구성된 단섬유를 이용 니들펀칭에 의해 3차원화 시킨 섬유질재료를 최소한 1종의 고분자물질 가용성 용제에서 그 섬유질 재료를 처리 부분적으로 용해시킴으로써 목적물을 얻는 방법등이 이용되고 있다. 그러나 이러한 방법들은 각각 장단점이 있다.The method of using woven fabrics or knitted fabrics is a method of directly raising the fiber structure formed by the weaving and knitting process or buffing after processing a polymer elastic body such as polyurethane to the napped structure. There is a method of obtaining a target object by impregnating or applying an elastic polymer material or a solution or emulsion of a polymer material mainly composed of the fibrous material in which the fiber is three-dimensional, and a single fiber composed of two or more kinds of different solubility polymer materials The method of obtaining the target object by dissolving the fibrous material three-dimensionalized by utilization needle punching at least 1 type of polymeric material soluble solvent, and partially dissolving it is used. However, each of these methods has advantages and disadvantages.

예를 들면 직물, 편물 또는 일반 단섬유를 이용한 방법은 유연한 풍합을 갖는 제품을 얻을 수 있는 반면 극세화 된 섬유질 재료를 얻기가 곤란하여 스웨드조 인공피혁 제조시 기모, 버핑후의 외관이 극히 조악하고 제반 기능성 및 물성이 낮아 고품질의 제품을 얻기가 실제적으로 곤란하며 2종 또는 그 이상의 용해성이 다른 고분자 물질로 구성된 단섬유를 이용할 경우에는 유연한 풍합을 얻기위해서는 고밀도의 섬유질재료의 사용에 곤란한 문제가 따르며 또한 극세섬유를 제조하기 위한 제조장치의 복잡성 및 3차원화 시킨 섬유질 재료중에서 최소 한가지 성분을 고분자물질 가용성 용제에서 용해제거해야 하므로 제조원가가 상승되는 문제점이 있었으며, 또 고밀도의 섬유질 재료를 얻기위해 섬유질 재료에 가해지는 총바늘 밀도가 높아 니들의 패턴에 의해 니들트랙(Needle track)이 발생하여 외관을 해치게 되며, 이를 제거하기 위해 기모가공, 버핑가공등을 수회 반복하게 됨으로써 기능성 및 물성을 저하시켰던 문제점이 있었다.For example, the method using woven fabrics, knitted fabrics or ordinary short fibers can provide products with a flexible blend, but it is difficult to obtain finely fibrous materials, and the appearance after raising and buffing in suede artificial leather is extremely poor. Due to its low functionality and physical properties, it is practically difficult to obtain high quality products. When using short fibers composed of two or more different solubility polymer materials, it is difficult to use high density fibrous materials to obtain flexible mixing. There is a problem in that the manufacturing cost is increased because at least one component of the manufacturing apparatus for manufacturing the ultrafine fibers and the three-dimensionalized fibrous material must be dissolved in the soluble solvent of the high molecular material, and the manufacturing cost is increased. The needle pattern is high due to the high total needle density applied. By being spoiled, and the appearance and the needle track (Needle track) occurs, the repeated several times brushed processing, such as buffing processing to remove them there is a problem that had reduced functionality and the physical property.

본 발명은 상술한 바와 같은 종래기술의 문제점을 해결한 것으로서 이하 상세히 설명하면 다음과 같다.The present invention solves the problems of the prior art as described above will be described in detail below.

완전 비상용성이면서 상호 접합력이 없는 2종의 섬유형성성 열가소성 합성수지를 이용하되 그 구성성분의 85몰 퍼센트 이상 95몰 퍼센트 이하가 폴리에틸렌 테레프탈레이트인 고수축성 공중합 폴리에스테르 열가소성 합성수지로된 제1성분과 폴리아마이드계 열가소성 합성수지로 된 제2성분을 이용하여 교호병렬형의 단면을 갖는 2성분 복합사를 제조하되, 구금장치(2)를 통과한 2성분 복합사를 공기류의 압력이 1.5바아(BAR)-4.5바아(BAR)인 밀폐형 관(3)을 통과시킨 다음 개섬장치(9)로 장섬유 웹(WEB)(4)을 형성시키고 계속해서 펠트의 밀도가 0.23g/㎤-0.32g/㎤가 되도록 니들펀칭기(6)에서 니들펀칭한 후 이완열처리욕조(7)의 열탕속에서 펠트를 분할, 수축처리함으로써 처리후의 장섬유 단사 데니어가 0.01데니어 내지 0.1데니어로 극세섬유화 되고 펠트의 면적 수축율이 30-50퍼센트가 되는 장섬유 극세부직포 고밀도 펠트의 제조방법이다.A first component and a polycondensation copolymer made of a highly shrinkable co-polyester thermoplastic synthetic resin using two types of fiber-forming thermoplastic resins which are completely incompatible and non-bonding, and wherein 85 to 95 mol percent of the components are polyethylene terephthalate. A bicomponent composite yarn having an alternating parallel type cross section is manufactured using a second component made of an amide thermoplastic synthetic resin, and the bicomponent composite yarn having passed through the detention apparatus 2 has an air pressure of 1.5 bar (BAR). After passing through a closed tube (3) of -4.5 bar (BAR) and forming a long fiber web (WEB) (4) with the carding machine (9), the density of the felt was 0.23 g / cm 3-0.32 g / cm 3 After needle punching in the needle punching machine 6, the felt is divided and shrunk in the boiling water of the relaxation heat treatment bath 7 so that the long-fiber single yarn denier after treatment is ultrafine fibers of 0.01 denier to 0.1 denier and the number of felt areas It is a manufacturing method of long fiber ultrafine nonwoven high density felt with shrinkage of 30-50%.

제1도중 1,1'는 2성분폴리머의 용융장치, 3'는 공기류 유입구, 5는 콘베어네트, 8은 펠트권취기이다.In FIG. 1, 1, 1 'is a melting apparatus of a two-component polymer, 3' is an air inlet, 5 is a conveyor net, and 8 is a felt winding machine.

본 발명에 사용되는 2종의 섬유형성성 열가소성 수지는 완전 비상용성이면서 상호접합력이 없는 합성수지를 이용해야 하며 그중 한성분은 고수축성을 가진 성분이어야 함을 필수조건으로 한다.The two fiber-forming thermoplastic resins used in the present invention must use synthetic resins that are completely incompatible and have no mutual bonding force, and one of them must be a component having high shrinkability.

만일 상용성과 접합력이 있는 열가소성 합성수지를 사용할 경우에는 제조공정상 복합방사와 니들펀칭 공정상에는 문제점이 없으나 분할처리공정 중에서 섬유의 극세화를 이루기가 어려워 본 발명의 목적을 달성하기 곤란하다.If a thermoplastic synthetic resin having compatibility and bonding strength is used, there is no problem in the composite spinning and needle punching processes in the manufacturing process, but it is difficult to achieve the miniaturization of the fibers in the splitting process, and thus it is difficult to achieve the object of the present invention.

또한 사용성분 폴리머의 한 성분이 고수축성이 아닐 경우에는 분할 수축처리 공정중 섬유의 극세화는 얻을 수 있으나 수축 후의 펠터의 밀도가 낮아 본 발명의 소기의 목적인 고밀도펠트를 얻을 수 없게 된다.In addition, when one component of the used component polymer is not highly shrinkable, fine fibers can be obtained during the split shrinkage process, but the density of the felt after shrinkage is low so that the high density felt, which is the intended purpose of the present invention, cannot be obtained.

따라서 본 발명에서는 2종의 섬유형성성 열가소성 합성수지의 제1성분을 그 구성성분의 85몰 퍼센트 이상 95몰 퍼센트 이하가 폴리에틸렌 테레프탈레이트로 구성된 고수축성 공중함 폴리에스테르 열가소성 합성수지로 된것을 이용하였으며 가장 좋은 범위는 87몰 퍼센트 이상 95몰 퍼센트 이하이다.Therefore, in the present invention, the first component of the two fiber-forming thermoplastic synthetic resins is made of a high shrinkage hollow core polyester thermoplastic synthetic resin composed of polyethylene terephthalate with 85 mol percent to 95 mol percent of the components. The range is 87 mole percent or more and 95 mole percent or less.

또한 교호병렬형의 단면을 형성하는 전기 2성분 복합사의 성분비는 제1성분 : 제2성분의 비율이 80 : 20-60 : 40정도의 범위가 바람직하나 장섬유 웹형성시 양호한 조업성, 웹의 균제도 및 분할 수축처리후의 펠트의 극세화, 고밀도화등을 고려할 때 70 : 30의 성분비가 가장 바람직하다.In addition, the component ratio of the electric two-component composite yarn forming an alternating parallel type cross section is preferably in the range of 80: 20-60: 40 for the ratio of the first component to the second component. The component ratio of 70:30 is the most preferable in consideration of the fineness and the high density of the felt after the uniformity and the split shrinkage treatment.

본 발명에 있어서 2성분 복합사는 제1도의 콘베어 네트(5)상에 웹을 형성시 공기류의 압력이 1.5바아-4.5바아인 밀폐형 관을 통과시킴을 필요로 한다.In the present invention, the two-component composite yarn needs to pass through a hermetic tube having a pressure of 1.5 bar-4.5 bar when forming a web on the conveyor net 5 of FIG.

만일 공기류의 압력이 1.5바아 이하일 경우는 본 발명자들이 실험한 결과 밀폐형 관을 통과한 멀티필라멘트군이 개섬장치에 의해 개섬될 때 개섬불량의 원인이 되며 또한 4.5바아 이상일 경우에는 사절의 유발을 빈번하게 일으켜 조업성을 저하시키는 주 원인이 된다. 양호한 개섬성과 조업성의 측면을 고려할 때 가장 적합한 공기류의 압력은 1.7바아-4.3바아의 범위이다.If the air flow pressure is 1.5 bar or less, the inventors have tested the multifilament group that passed through the sealed tube when the carding machine is opened. It is the main cause of deterioration of operability. In view of good openness and operability, the most suitable air pressure is in the range of 1.7 bar to 4.3 bar.

또한 본 발명에 있어서 형성된 전기 장섬유 웹은 니들펀칭 후의 펠트의 밀도가 0.23g/㎤-0.32g/㎤가 되도록 니들펀칭 조건을 설정함을 필요로 한다. 일반적으로 고밀도 펠트라함은 수축후의 펠트의 밀도가 0.35g/㎤이상이 됨을 일컫는다.In addition, the electric long-fiber web formed in the present invention requires setting needle punching conditions so that the density of the felt after needle punching is 0.23 g / cm 3 -0.32 g / cm 3. In general, high density felt refers to the density of the felt after shrinkage is 0.35 g / cm 3 or more.

만일 니들펀칭후의 펠트의 밀도가 0.23g/㎤ 이하가 되도록 니들펀칭 조건을 설정하면 섬유간의 3차원 교락의 치밀도가 부족하여 열수축처리후의 펠티밀도가 고밀도화 될 수 없을 뿐아니라 스웨드조 인공피혁 제조시 기모버핑후의 제품의 품위가 떨어지게 된다.If the needle punching condition is set so that the density of felt after needle punching is 0.23g / cm3 or less, the density of three-dimensional entanglement between fibers is insufficient, so that the felt density after heat shrinkage treatment cannot be made high and suede artificial leather is manufactured. The quality of the product after raising the buff will be reduced.

또한 니들펀칭후의 펠트의 밀도가 0.32g/㎤ 이상이 되도록 니들펀칭 조건을 설정한 경우에는 니들펀칭시 장섬유와 니들사이의 마찰이 심하여 장섬유의 파사를 일으키게 되어 펠팅효과를 떨어뜨릴 뿐만아니라 바늘에 심한 손상을 주게 된다.In addition, when needle punching conditions are set so that the density of felt after needle punching is 0.32g / cm3 or more, the friction between the long fibers and the needles during needle punching is severe, which causes the long fibers to be broken and not only reduce the felting effect. Severe damage to the product.

양호한 3차원 교락의 치밀도와 장섬유의 파사를 일으키지 않는 니들펀칭의 조건은 니들펀칭후의 펠트의 밀도를 0.27g/㎤-0.30g/㎤의 범위가 되도록 니들펀칭 조건을 설정하는 것이 바람직하다.The condition of needle punching that does not cause good three-dimensional entanglement density and long fiber breakage is preferably set to needle punching conditions such that the density of felt after needle punching is in the range of 0.27 g / cm 3 -0.3 g / cm 3.

본 발명의 장섬유 부직포 제조에 효과를 더 해줄 수 있는 니들의 타입으로는 컨벤션 타입(Convention Type)보다는 다이프레스드 타입(Die Pressed)이 보다 유리하며 니들의 규격으로는 3b/3E보다는 2b/2E또는 1b/1E가 훨씬 적합하다.(b : barb, E : Edge) 본 발명에 있어서 상술한 방법으로 제조된 3차원 교락장섬유 부직포 펠트는 열탕속에서 처리함으로써 장섬유 단사 데니어가 0.01데니어 내지 0.1데니어로 극세섬유화되고 펠트의 면적수축율이 30-50퍼센트로 고밀도화 되는데 이는 교호병렬형의 단면을 구성하는 각 성분 폴리머의 상호작용에 의한 것으로 제1성분은 85몰 퍼센트 이상 95몰 퍼센트 이하가 폴리에틸렌테레프탈레이트인 고수축성 공중합 폴리에스테르 열가소성 합성수지이고, 제2성분은 폴리아마이드계 열가소성 합성수지로 구성되었기 때문에 두 성분 폴리머간의 고유의 수축률차가 크게 다르고 또한 제사공정 중에서 구금을 통과한 전기 2성분 복합사는 공기류의 압력에 의해 완전 연신은 되었지만 통상의 필라멘트 연신공정에서와 같은 열에 의한 열고정을 실시하지 않았기 때문에 공기류에 의한 연신시 받은 내부수축 응력은 그대로 보지하게 된다.As the type of needle that can further effect the long fiber nonwoven fabric of the present invention, a die pressed type is more advantageous than a convention type, and the size of the needle is 2 b rather than 3 b / 3 E. / 2 E or 1 b / 1 E is much more suitable (b: barb, E: Edge) The three-dimensional entangled long-fiber nonwoven felt produced by the method described above in the present invention is a long-fiber single yarn denier by treating in hot water Is 0.01 denier to 0.1 denier and the density of felt is increased to 30-50 percent, which is due to the interaction of each component polymer constituting the alternating parallel type cross section. Highly shrinkable co-polyester thermoplastic synthetic resins with percent or less of polyethylene terephthalate, and the second component is composed of polyamide-based thermoplastic synthetic resins. The inherent shrinkage difference between the polymers is significantly different, and the electric two-component composite yarns passed through the detention during the weaving process are completely stretched by the pressure of the air stream, but they are not heat-set by heat as in the normal filament stretching process. The internal shrinkage stress received during the stretching is retained as it is.

따라서 장섬유 웹을 형성한 후 니들펀칭 공정까지는 제2a도와 같은 3차원 교락을 유지한 상태에서는 제2b도의 한 단면에와 같이 동일단면내에 2성분의 폴리머가 동시에 존재를 하게되나, 이를 열탕속에서 분할, 수축처리하면 제3b도와 같이 각성분의 수축률차에 의해 자연분할되어 극세섬유화 되고 동시에 고밀도화 되는 장섬유 극세부직포 고밀도 펠트를 얻을 수 있다.Therefore, after the long fiber web is formed, the needle punching process maintains three-dimensional entanglement as shown in FIG. By dividing and shrinking, as shown in FIG. 3B, a long fiber ultrafine nonwoven fabric high density felt is spun naturally by the shrinkage difference of each component, which is microfiber and at the same time high density.

본 발명의 방법에 의해 제조된 장섬유 극세부직포 고밀도 펠트는 펠트제조시 단섬유를 이용하여 제조한 펠트의 경우보다 중량 및 두께 조절이 용이하며 또한 제조설비가 훨씬 간단하여 제조원가의 질감에 큰 효과를 얻을 수 있다.The long-fiber ultrafine nonwoven high density felt produced by the method of the present invention is easier to control the weight and thickness than the felt produced using short fibers in the manufacture of felt, and the manufacturing equipment is much simpler, which has a great effect on the texture of manufacturing cost. You can get it.

즉 단섬유를 이용하여 펠트를 제조할 경우에는 방사, 연신, 크림핑, 커팅공정등의 단섬유 제조공정과 오프닝(Opening), 카딩(Carding), 니들펀칭(Needle-Punching)등의 펠트제조 공정등의 복잡한 공정을 거치는 반면 본 발명에 의한 방법은 방사공정후에 장섬유 웹을 형성시킨 후 직접 니들펀칭에 의한 펠트의 제조가 가능하므로 제조공정을 크게 단축시킬 수 있다.In other words, when the felt is manufactured using short fibers, a short fiber manufacturing process such as spinning, stretching, crimping and cutting processes, and a felt manufacturing process such as opening, carding, and needle punching are required. On the other hand, the method according to the present invention can form the long fiber web after the spinning process, and then directly manufacture the felt by needle punching, thereby greatly shortening the manufacturing process.

또한 장섬유극세사를 이용한 고밀도 펠트이므로 단섬유 또는 단섬유극세사를 이용하여 제조한 펠트에 비해 인장강력(Cross Direction, Machine Direction 포함)이 우수하고 균일할 뿐아니라 박리강력등 제반 물리적, 기계적 성질이 우수하여 이를 이용하여 기모, 버핑등의 공정을 거쳐 스웨드조 인공피혁등을 제조했을 때 외관이 우수하며 기능성, 실용성등이 양호한 고품위의 제품을 얻을 수 있다.In addition, since it is a high-density felt using long fiber microfiber, tensile strength (including cross direction and machine direction) is better and uniform than felt manufactured using short fiber or short fiber microfiber, and it has excellent physical and mechanical properties such as peel strength. By using this, suede artificial leather is manufactured by raising, buffing, etc., high-quality products with excellent appearance and excellent functionality and practicality can be obtained.

[실시예]EXAMPLE

극한점도가 0.65(25℃의 OCP 용매로 측정)이고 그 구성성분의 90몰 퍼센트가 폴리에틸렌테레프탈레이트로 구성된 고수축성 공중합 폴리에스테르 열가소성 합성수지를 제1성분으로 하고, 상대점도가 2.50(25℃의 H2SO4용매로)인 폴리아마이드계 열가소성 합성수지를 제2성분으로 하여 290℃에서 방사하여 제2a도와 같은 교호병렬형의 단면을 형성시킨 후(이때 제1성분과 제2성분의 성분비는 7 : 3으로 하였다) 공기류의 압력이 2.5바아인 밀폐형 관을 통과시켜 장섬유단사데니어가 1데니어가 되도록 장섬유 옵을 형성한 후 2barb/2Edge 규격의 다이프레스 타입(Singer사 제품) 니들을 사용하여 니들펀칭후의 중량이 800g/㎡, 후도 2.9mm, 밀도가 0.27g/㎤ 되도록 니들펀칭 하였다. 이를 계속해서 100℃의 열탕속에서 분할 수축처리하여 면적수축률이 40%이고, 분할 후 장섬유단사데니어가 0.03데니어-0.09데니어 펠트의 밀도가 0.39g/㎤인 장섬유극세부직포 고밀도 펠트를 제조하였다. 이와 같이 제조한 고밀도펠트를 30퍼센트 폴리우레탄의 DMF용액에 함침한 후 응고 건조시키고 기모, 버핑하여 스웨드조 인공피혁을 제조한 후 천연스웨드와의 품질을 비교한 결과는 표 1과 같다.The ultimate viscosity is 0.65 (measured by OCP solvent at 25 ° C.) and 90 mole percent of its constituents are composed of polyethylene terephthalate, a highly shrinkable copolyester thermoplastic synthetic resin as a first component, and a relative viscosity of 2.50 (H at 25 ° C.). 2 SO 4 solvent) and a polyamide-based thermoplastic synthetic resin as a second component was spun at 290 ℃ to form an alternating parallel cross-section as shown in Fig. 2a (the ratio of the components of the first component and the second component is 7: 3) The long-fiber Op is formed so that the long-fiber single yarn denier becomes 1 denier by passing through a sealed tube with an air flow pressure of 2.5 bar, and then using a 2 barb / 2 edge standard die press needle (manufactured by Singer). Needle punching was carried out such that the weight after needle punching was 800 g / m 2, the thickness was also 2.9 mm, and the density was 0.27 g / cm 3. Subsequently, the shrinkage treatment was performed in a hot water bath at 100 ° C. to prepare a long fiber ultra-fine nonwoven high density felt having an area shrinkage of 40% and a long fiber single yarn denier of 0.03 denier-0.09 denier felt having a density of 0.39 g / cm 3. . The high-density felt prepared in this way was impregnated with DMF solution of 30% polyurethane, coagulated, dried, brushed, and buffed to manufacture suede artificial leather, and the results of comparing with the quality of natural suede are shown in Table 1.

[표 1]TABLE 1

Figure kpo00001
Figure kpo00001

Claims (1)

완전비상용성이고 상호간에 접합력이 없는 2종의 섬유형성성 열가소성수지를 사용하되, 제1성분은 그 구성성분의 85몰% 이상 95몰% 이하가 폴리에틸렌테레프탈레이트인 고수축성 공중합 폴리에스테르 수지이고, 제2성분은 폴리아마이드계 수지인 것을 사용하여 교호병렬형 단면을 가지는 2성분 복합사를 방사한 다음, 이것을 공기류의 압력이 1.5-4.5바아(BAR)인 밀폐형 관을 통과시켜서 장섬유 웹(WEB)을 형성시키고, 이어서 상기웹을 밀도가 0.23g/㎤-0.32g/㎤이 되도록 니들펀칭한 다음, 이안상태로 열탕에 통과시켜주는 장섬유 부직포 펠트의 제조방법.Two types of fiber-forming thermoplastic resins, which are completely incompatible with each other and have no bonding strength, are used. The first component is a highly shrinkable co-polyester resin in which at least 85 mol% and at most 95 mol% of the components are polyethylene terephthalate. The second component is a polyamide-based resin and spun a bicomponent composite yarn having an alternating parallel cross section, and then passes through a closed tube having an air pressure of 1.5-4.5 bar (BAR) to form a long fiber web ( WEB), and then the web is needle punched to a density of 0.23 g / cm 3-0.32 g / cm 3, and then passed through the hot water in a binocular state for producing a long fiber nonwoven felt.
KR1019870013576A 1987-11-30 1987-11-30 Manufacturing process of nonwoven fabric felt KR900005002B1 (en)

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EP1028186A4 (en) * 1997-10-31 2003-01-29 Teijin Ltd Nonwoven fabric, and sheetlike materials and synthetic leathers made by using the same

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KR100403766B1 (en) * 2001-12-26 2003-10-30 주식회사 효성 Method for Producing Nonwaven Fabric Using Highly-Contractive Composite Monofilament
KR100447500B1 (en) * 2002-05-16 2004-09-08 주식회사 코오롱 A side by side type conjugate fiber with excellent crimping property
KR100476461B1 (en) * 2002-08-26 2005-03-17 김학용 A process of preparing for non-woven fabric composed nano fiber

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1028186A4 (en) * 1997-10-31 2003-01-29 Teijin Ltd Nonwoven fabric, and sheetlike materials and synthetic leathers made by using the same
US6566287B1 (en) 1997-10-31 2003-05-20 Teijin Limited Non-woven fabric, and sheet and artificial leather produced from the same

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