KR101138291B1 - Method for manufacturing Lyocell based carbon fiber and Lyocell based carbon fabric - Google Patents
Method for manufacturing Lyocell based carbon fiber and Lyocell based carbon fabric Download PDFInfo
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- D01F9/00—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments
- D01F9/08—Artificial filaments or the like of other substances; Manufacture thereof; Apparatus specially adapted for the manufacture of carbon filaments of inorganic material
- D01F9/12—Carbon filaments; Apparatus specially adapted for the manufacture thereof
- D01F9/14—Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments
- D01F9/16—Carbon filaments; Apparatus specially adapted for the manufacture thereof by decomposition of organic filaments from products of vegetable origin or derivatives thereof, e.g. from cellulose acetate
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- D01D10/00—Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
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- D01D10/00—Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
- D01D10/06—Washing or drying
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- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/07—Addition of substances to the spinning solution or to the melt for making fire- or flame-proof filaments
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- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/02—Yarns or threads characterised by the material or by the materials from which they are made
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- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
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- D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
- D06M11/77—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with silicon or compounds thereof
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- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
- D06M15/19—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
- D06M15/37—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D06M15/643—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds containing silicon in the main chain
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Abstract
본 발명은 라이오셀계 탄소섬유 및 탄소직물의 제조방법에 관한 것으로서, 좀더 상세하게는 라이오셀 섬유 또는 라이오셀 직물을 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 전처리 공정, 안정화 공정, 탄화 공정 및 흑연화 공정을 거쳐서 이루어지는 탄소섬유 및 탄소직물의 제조방법에 관한 것이다.The present invention relates to a method for producing lyocell-based carbon fibers and carbon fabrics, and more particularly, pretreatment process, stabilization process, carbonization process and graphite immersed lyocell fiber or lyocell fabric in a silicone-based polymer solution and flame retardant salt solution It relates to a method for producing carbon fibers and carbon fabrics made through a oxidization process.
Description
본 발명은 라이오셀계 탄소섬유 및 탄소직물의 제조방법에 관한 것으로서, 좀더 상세하게는 라이오셀 섬유 또는 라이오셀 직물을 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 전처리 공정, 안정화 공정, 탄화 공정 및 흑연화 공정을 거쳐서 이루어지는 탄소섬유 및 탄소직물의 제조방법에 관한 것이다.The present invention relates to a method for producing lyocell-based carbon fibers and carbon fabrics, and more particularly, pretreatment process, stabilization process, carbonization process and graphite immersed lyocell fiber or lyocell fabric in a silicone-based polymer solution and flame retardant salt solution It relates to a method for producing carbon fibers and carbon fabrics made through a oxidization process.
일반적으로, 탄소섬유는 전구체(precursor)의 종류에 따라 레이온(rayon)계, 폴리아크릴로니트릴(polyacrylonitrile, PAN)계, 그리고 피치(pitch)계 탄소섬유로 분류된다. In general, carbon fibers are classified into rayon-based, polyacrylonitrile (PAN) -based, and pitch-based carbon fibers according to the kind of precursor.
지금까지 레이온계 탄소섬유는 고순도 비스코스 레이온 섬유로 제조되었는데, 제조공정에서 공해물질, 즉 용제로서 이황화탄소(CS2)를 사용하여 정부의 규제를 받을 뿐만 아니라, PAN계 탄소섬유나 피치계 탄소섬유에 비하여 경제성이 없어 시장규모도 점차 줄어들고 있는 추세이다. Until now, rayon-based carbon fibers have been made of high-purity viscose rayon fibers, which are not only regulated by the government using pollutants, that is, carbon disulfide (CS 2 ) as a solvent, but also PAN-based and pitch-based carbon fibers. Compared with the economy, the market size is gradually decreasing.
라이오셀 섬유는 1978년 Akzo-Nobel사가 환경 공해 및 인체에 유해한 성분이 없는 새로운 공정을 개발하여 제조된 것으로서, 셀룰로오스가 주성분인 천연펄프와 펄프를 용해시키는 용제인 N-메틸몰포린-N-옥사이드(N-methylmorpholine-N-oxide:NMMO)를 주원료로 하여 제조된 건습식 방사섬유이다. 라이오셀 섬유의 원료는 목재펄프에서 추출된 셀룰로오스로서, 100% 생분해성 고분자이며, 재생이 가능하므로 환경 친화적인 특징을 가지고 있다. 또한 기존의 레이온 섬유가 지니고 있는 큰 문제점인 공해물질을 배출하지 않는 새로운 공법이 적용된다. The lyocell fiber was manufactured in 1978 by Akzo-Nobel, a company that developed a new process that is free from environmental pollution and harmful substances to humans. (N-methylmorpholine-N-oxide: NMMO) It is a wet and dry spinning fiber manufactured with the main raw material. The raw material of lyocell fiber is cellulose extracted from wood pulp, which is 100% biodegradable polymer and has environmentally friendly characteristics because it is recyclable. In addition, a new method is applied which does not emit pollutants, which is a big problem of existing rayon fibers.
라이오셀 섬유 역시 셀룰로오스계 섬유이며, 화학적 성질은 서로 비슷하지만, 기계적 특성 및 물리적 성질은 우수하며, 결정화도나 결정 배향도 등 미세구조 특성은 매우 다르다. 이러한 장점을 가지고 있음에도 불구하고, 1990년 초가 되어서야 방적사 형태로 생산되었으며, 2000년 초에 필라멘트(filament)사로 소규모로 상업화되었다. 2007년에 국내 (주)효성 및 (주)코오롱에서 라이오셀 필라멘트사를 대량 생산할 수 있는 체계를 갖추고 있다.The lyocell fiber is also a cellulose fiber, and the chemical properties are similar to each other, but the mechanical and physical properties are excellent, and the microstructural properties such as crystallinity and crystal orientation are very different. Despite these advantages, it was not produced in the form of spun yarn until early 1990, and commercialized on a small scale as a filament company in early 2000. In 2007, Hyosung Co., Ltd. and Kolon Co., Ltd. have a system for mass production of lyocell filament yarn.
일반적으로 탄소섬유의 제조를 위해서는 세개의 공정 단계 즉, 안정화 공정(stabilization), 탄화 공정(carbonization) 그리고 흑연화 공정(graphitization)을 거치게 된다. 상기 공정들은 섬유 상태 또는 직물 상태에서 수행되는데, 탄소섬유의 사용 목적에 따라서 최종 탄화 온도나 흑연화 온도를 결정하게 된다. 탄화 온도 및 흑연화 온도는 탄소섬유의 열전도도, 절연성 또는 탄성률에 큰 영향을 미친다.In general, the production of carbon fiber is subjected to three process steps, stabilization (carbonization) and graphitization (graphitization). The processes are carried out in a fibrous or woven fabric, which determines the final carbonization temperature or the graphitization temperature depending on the intended use of the carbon fiber. The carbonization temperature and the graphitization temperature have a great influence on the thermal conductivity, insulation, or modulus of elasticity of the carbon fiber.
또한, 안정화 공정 및 탄화 공정 중에 적용되는 열처리 온도, 승온속도, 승온단계, 섬유표면의 화학처리 및 분위기가스 등의 여러 가지 공정인자에 따라 탄소 섬유의 내부 구조와 물성은 크게 달라질 수 있다. 안정화 공정은 PAN계 또는 피치계 등 모든 탄소섬유에 대하여 공통적으로 행하는 열처리 단계로서, 특히 레이온계 탄소섬유에서는 가장 중요한 핵심 공정이다. 일반적으로 안정화 공정 중에서 심각한 화학적, 물리적 변화가 급격하게 발생하는데, 이후 탄화 공정에 필요한 높은 열처리온도를 견딜 수 있는 안정된 화학구조를 부여하는데 그 목적이 있다. 이러한 안정화 공정의 효과를 더욱 높이기 위하여 화학적 전처리공정이 필수적이며, 탄소섬유 제조에 있어서 전처리 공정과 관련된 기술의 개발이 요구되고 있다.In addition, the internal structure and physical properties of the carbon fiber may vary greatly depending on various process factors such as the heat treatment temperature, the temperature increase rate, the temperature increase step, the chemical treatment of the fiber surface, and the atmosphere gas applied during the stabilization process and the carbonization process. The stabilization process is a heat treatment step that is commonly performed on all carbon fibers such as PAN system or pitch system, and is the most important core process in rayon carbon fiber. In general, serious chemical and physical changes occur rapidly during the stabilization process, and its purpose is to provide a stable chemical structure capable of withstanding the high heat treatment temperature required for the carbonization process. In order to further enhance the effect of the stabilization process, a chemical pretreatment process is essential, and development of a technology related to the pretreatment process is required in carbon fiber production.
본 발명의 목적은 라이오셀 섬유 또는 라이오셀 직물을 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 전처리 공정을 안정화 공정 전에 수행하므로써 안정화 공정의 효과를 더욱 높일 수 있는 라이오셀계 탄소섬유 및 탄소직물의 제조방법을 제공하는 것이다.An object of the present invention is to prepare a lyocell-based carbon fiber and carbon fabric that can further enhance the effect of the stabilization process by performing a pretreatment process to immerse the lyocell fiber or lyocell fabric in the silicone-based polymer solution and flame retardant salt solution before the stabilization process To provide a way.
본 발명의 라이오셀계 탄소섬유 및 탄소직물의 제조방법은 라이오셀 섬유 또는 라이오셀 직물을 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 전처리 공정, 안정화 공정, 탄화 공정 및 흑연화 공정을 거쳐 이루어지는 것을 특징으로 한다.The method for producing a lyocell-based carbon fiber and carbon fabric of the present invention is characterized in that the lyocell fiber or lyocell fabric is subjected to a pretreatment step, a stabilization step, a carbonization step and a graphitization step of immersing the lyocell fiber or the lyocell fabric in an aqueous solution of a flame retardant salt. It is done.
본 발명에 있어서 전처리 공정은 라이오셀 섬유 또는 라이오셀 직물을 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 것으로서, 상기 실리콘계 고분자의 예로서는 폴리실록산(Polysiloxane:PS), 폴리디메틸실록산(Polydimethylsiloxane:PDMS), 실온 경화형 실리콘(Room temperature vulcanizing silicone:RTV), 폴리메틸페닐실록산(Polymethyl phenyl siloxane:PMPS), 폴리실라잔(Polysilazane) 등을 들 수 있고, 상기 난연성 염의 예로서는 인산 (phosphoric acid:H3PO4), 인산나트륨(sodium phosphate:Na3PO4), 염화암모늄(ammonium chloride:NH4Cl) 등을 들 수 있다.In the present invention, the pretreatment step is to immerse the lyocell fiber or lyocell fabric in a silicone-based polymer solution and a flame retardant salt solution, examples of the silicone-based polymer is polysiloxane (PS), polydimethylsiloxane (PDMS), room temperature Room temperature vulcanizing silicone (RTV), polymethyl phenyl siloxane (PMPS), polysilazane (Polysilazane) and the like. Examples of the flame retardant salts include phosphoric acid (phosphoric acid: H 3 PO 4 ), phosphoric acid Sodium (phosphate: Na 3 PO 4 ), ammonium chloride (ammonium chloride: NH 4 Cl) and the like.
상기 실리콘계 고분자 용액에 있어서, 용매로는 극성 용매가 사용되는데, 상기 극성 용매의 예로는 아세톤(Acetone), 퍼클로로에틸렌(Perchloroethylene), 테트라히드로푸란(Tetrahydrofurane:THF), 메틸에테르케톤(Methyletherketone:MEK), 에틸알코올(Ethylalcohol), 메틸알코올(Methylalcohol) 등을 들 수 있다.In the silicone polymer solution, a polar solvent is used. Examples of the polar solvent include acetone, perchloroethylene, tetrahydrofurane (THF), and methyl ether ketone (MEK). ), Ethyl alcohol (Ethylalcohol), methyl alcohol (Methylalcohol) and the like.
본 발명의 전처리 공정에서 사용되는 실리콘계 고분자 용액 중의 실리콘계 고분자의 농도 범위는 1~15중량%인 것이 바람직한데, 상기 실리콘계 고분자의 농도가 1중량% 미만인 경우에는 농도가 너무 낮아 안정화 효과가 나타나지 않아서 바람직하지 않고, 15중량%를 초과하는 경우에는 불균일성뿐만 아니라 취성이 커져서 바람직하지 않다. 또한 난연성 염 수용액 중의 난연성 염의 농도 범위는 3~20중량%인 것이 바람직한데, 상기 난연성 염의 농도가 3중량% 미만인 경우에는 농도가 낮아 난연효과가 나타나지 않아서 바람직하지 않고, 20중량%를 초과하는 경우에는 과포화 상태가 나타나게 되어 바람직하지 않다.The concentration range of the silicon-based polymer in the silicon-based polymer solution used in the pretreatment process of the present invention is preferably 1 to 15% by weight, but when the concentration of the silicon-based polymer is less than 1% by weight, the concentration is too low, so the stabilizing effect is not preferable. In addition, when it exceeds 15 weight%, not only unevenness but also brittleness becomes large, and it is unpreferable. In addition, the concentration range of the flame retardant salt in the flame retardant salt aqueous solution is preferably 3 to 20% by weight, but when the concentration of the flame retardant salt is less than 3% by weight, the concentration is low, which is not preferable because the flame retardant effect does not appear, and when it exceeds 20% by weight It is not desirable to have a supersaturated state.
또한, 상기 침지처리는 상온(약 25℃)~80℃의 온도에서 실리콘계 고분자 용액과 난연성 염 수용액에 각각 1시간 이내의 시간 동안, 바람직하게는 10분~1시간의 시간 동안 순차적으로 침지처리하므로써 수행되는 것이 바람직한데, 상기 온도가 상온 미만인 경우에는 안정화 효과가 낮아 바람직하지 않고, 80℃를 초과하는 경우에는 섬유의 유연성이 떨어져서 바람직하지 않으며, 1시간을 초과하는 경우에는 셀룰로오스가 용액에서 팽윤되거나 강도가 떨어질 가능성이 있어서 바람직하지 않다. 상기 침지처리시에 실리콘계 고분자 용액과 난연성 염 수용액에 침지처리하는 순서에는 특별히 제한이 없으나, 실리콘계 고분자 용액에 먼저 침지시킨 후 난 연성 염 수용액에 침지시키는 것이 바람직하다.In addition, the immersion treatment is performed by sequentially immersing the silicon-based polymer solution and the flame-retardant salt aqueous solution for 1 hour, preferably 10 minutes to 1 hour at a temperature of room temperature (about 25 ℃) ~ 80 ℃ If the temperature is less than room temperature, it is preferable that the stabilizing effect is not preferable, and if it exceeds 80 ° C, the flexibility of the fiber is not preferable, and if it exceeds 1 hour, the cellulose swells in solution or It is not preferable because the strength may drop. There is no particular restriction on the order of the immersion treatment in the silicone-based polymer solution and the flame-retardant salt aqueous solution during the immersion treatment, it is preferable to be immersed in the silicone-based polymer solution first, and then immersed in the flame-retardant salt aqueous solution.
본 발명에 있어서 안정화 공정은 2단계로 수행되며, 1단계는 100~250℃의 온도범위에서 10~30시간 동안, 2단계는 300~500℃의 온도범위에서 10~100시간 동안 열처리하므로써 수행되는 것이 바람직하다. 안정화 공정에 있어서 1단계가 100℃ 미만의 온도에서 열처리되는 경우에는 건조가 되지 않기 때문에 바람직하지 않고, 250℃를 초과하는 온도에서 열처리되는 경우에는 섬유의 열분해가 일어날 우려가 있어서 바람직하지 않으며, 10시간 미만의 시간 동안 열처리되는 경우에는 섬유가 유연성을 잃을 수 있기 때문에 바람직하지 않고, 30시간을 초과하는 시간 동안 열처리되는 경우에는 안전화 효율이 떨어져서 바람직하지 않다. 또한, 안정화 공정에 있어서 2단계가 300℃ 미만의 온도에서 열처리되는 경우에는 안정화 효과가 두드러지지 않아서 바람직하지 않고, 500℃를 초과하는 온도에서 열처리되는 경우에는 안정화 효과보다는 탄화효과가 두드러져서 바람직하지 않으며, 10시간 미만의 시간 동안 열처리되는 경우에는 섬유가 유연성을 잃을 수 있기 때문에 바람직하지 않고, 100시간을 초과하는 시간 동안 열처리되는 경우에는 안정화 효과 및 효율이 떨어져서 바람직하지 않다.In the present invention, the stabilization process is carried out in two steps, the first step is carried out by heat treatment for 10 to 30 hours in the temperature range of 100 ~ 250 ℃, the second step is 10 to 100 hours in the temperature range of 300 ~ 500 ℃ It is preferable. In the stabilization process, if the first step is heat-treated at a temperature below 100 ° C., it is not preferable because it is not dried, and if heat-treated at a temperature above 250 ° C., thermal decomposition of the fiber may occur, which is not preferable. The heat treatment for less than the time is not preferable because the fiber may lose flexibility, and if the heat treatment for more than 30 hours, the safety efficiency is inferior. In addition, in the stabilization process, the second step is not preferable because the stabilization effect is not noticeable when the heat treatment at a temperature below 300 ℃, the carbonization effect is more preferable than the stabilization effect when heat treatment at a temperature above 500 ℃. In addition, when the heat treatment for less than 10 hours is not preferable because the fiber may lose flexibility, the heat treatment for more than 100 hours is not preferable because the stabilization effect and efficiency is inferior.
본 발명에 있어서 탄화 공정은 900~1700℃의 온도범위에서 10~30시간 동안 열처리하므로써 수행되는 것이 바람직하다. 탄화 공정의 온도가 900℃ 미만인 경우에는 탄화율이 80% 이하로 너무 낮아서 바람직하지 않고, 1700℃를 초과하는 경우에는 탄화보다는 흑연화 효과가 두드러지고, 강도가 떨어져서 바람직하지 않으며, 탄화 공정이 10시간 미만 동안 열처리되는 경우에는 충분한 탄화공정이 이루어지지 않아서 바람직하지 않고, 30시간을 초과하는 동안 열처리되는 경우에는 탄화수율이 떨어져서 바람직하지 않다.In the present invention, the carbonization process is preferably performed by heat treatment for 10 to 30 hours in the temperature range of 900 ~ 1700 ℃. If the temperature of the carbonization process is less than 900 ° C, the carbonization rate is too low, which is too low at 80% or less.If the temperature of the carbonization process is higher than 1700 ° C, the graphitization effect is more pronounced than carbonization, and the strength is not preferable. If the heat treatment for less than the time is not preferable because the sufficient carbonization process is not made, and if the heat treatment for more than 30 hours, the carbonization yield is not preferable.
본 발명에 있어서 열전도도, 절연성 또는 내열특성 등을 제어할 수 있는 흑연화 공정은 2000~2800℃의 흑연화 온도까지 승온시켰다가 2000~2800℃의 온도에서 체류시간을 10시간 이하 즉, 0~10시간으로 하여 수행되는 것이 바람직한데, 상기 온도가 2000℃ 미만인 경우에는 흑연화도가 떨어져서 바람직하지 않고, 2800℃를 초과하는 경우에는 경제성 대비 흑연화 효과가 떨어져서 바람직하지 않다. 2000~2800℃에서의 체류시간이 0시간이라 함은 상기 흑연화 온도까지 승온시켰다가 바로 냉각시키는 것을 의미하며, 체류시간이 10시간이라 함은 상기 흑연화 온도에서 10시간 동안 유지시켰다가 냉각시키는 것을 의미한다. 상기 흑연화 온도에서의 체류시간이 10시간을 초과하는 경우에는 최종 탄화수율이 떨어져서 바람직하지 않다.In the present invention, the graphitization process that can control the thermal conductivity, insulation, or heat resistance characteristics is raised to a graphitization temperature of 2000 ~ 2800 ℃, the residence time at a temperature of 2000 ~ 2800 ℃ 10 hours or less, that is, 0 ~ It is preferably carried out for 10 hours, the graphitization degree is not preferable when the temperature is less than 2000 ℃, it is not preferable because the graphitization effect compared to economical efficiency is lower than 2800 ℃. The retention time at 2000 ~ 2800 ° C. is 0 hours means that the graphitization temperature is raised and cooled immediately. The retention time is 10 hours. The retention time is maintained at the graphitization temperature for 10 hours and then cooled. Means that. If the residence time at the graphitization temperature exceeds 10 hours, the final carbonization yield is not preferable, which is undesirable.
이하, 도면을 참고하여 본 발명을 상세하게 설명하면 다음과 같다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정의 일례를 도시한 순서도로서, 먼저 출발물질인 라이오셀 섬유를 직조하여 평직, 능직 또는 주자직 직물구조로 만드는 제직공정(1) 후, 제직된 직물을 아세톤과 같은 유기용제를 이용하여 세척하는 세척공정(2)을 거치면서 불순물을 제거하고, 섬유의 잔류응력을 완화시킨다. 그 후, 실리콘계 고분자와 난연성 염을 포함하는 화학적 전처리제를 순차적으로 통과시킨 후 건조시키는 전처리공정(3)을 거친 직물은, 열처리 단계인 안정화 공정(4), 탄화 공정(5) 및 흑연화 공정(6)을 거치면서 탄소직물로 전환된다. 그 후에 탄소직물에 남아있는 타르나 불순물들을 제거하는 세척공정(7)을 거쳐서 본 발명에 따른 라이오셀계 탄소직물을 제조한다.1 is a flow chart showing an example of a lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention, first weaving a lyocell fiber as a starting material to make a plain weave, twill or main weave fabric structure after the weaving process (1) To remove impurities and to reduce the residual stress of the fiber, the woven fabric is subjected to a washing process (2) for washing with an organic solvent such as acetone. Thereafter, the fabric which passed through the pretreatment step (3) of sequentially passing through a chemical pretreatment agent containing a silicone-based polymer and a flame retardant salt and then drying, is subjected to a stabilization step (4), a carbonization step (5), and a graphitization step, which are heat treatment steps. Converted to carbon fabric through (6). Thereafter, a lyocell-based carbon fabric according to the present invention is prepared through a washing process 7 for removing tar or impurities remaining on the carbon fabric.
도 2는 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정에 있어서의 안정화 공정 사이클의 일례를 나타낸 것으로서, 상기 안정화 공정은 2단계로 수행되며, 이 공정동안 주로 탈수소화 반응 및 고리화 반응 등이 일어나고, 약 60~70중량%의 무게 감량이 발생한다. 안정화 공정의 1단계에서 약 100~250℃까지 10~30℃/시간의 승온속도로 승온시키고, 2단계에서는 약 300~500℃까지 2~10℃/시간의 낮은 승온속도로 승온시켜 열처리를 수행하므로써 안정화 직물이 제조된다.Figure 2 shows an example of the stabilization process cycle in the lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention, the stabilization process is carried out in two steps, mainly during the dehydrogenation reaction and cyclization reaction, etc. This happens, and weight loss of about 60 to 70% by weight occurs. In the first step of the stabilization process, the temperature is raised to a temperature increase rate of 10 to 30 ° C./hour up to about 100 to 250 ° C., and in the second step, the temperature is raised to a low temperature rising rate of 2 to 10 ° C./hour up to about 300 to 500 ° C. Thereby stabilizing fabric is produced.
도 3은 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정에 있어서의 탄화 공정 사이클의 일례를 나타낸 것으로서, 상기 탄화 공정은 불활성 분위기에서, 약 900~1700℃까지 30~100℃/시간의 승온속도로 승온시키고, 10~30시간 동안 열처리하고 나서 자연냉각시킴으로써 수행된다.Figure 3 shows an example of a carbonization process cycle in the lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention, the carbonization process is heated to 30 ~ 100 ℃ / hour to about 900 ~ 1700 ℃ in an inert atmosphere It is carried out by heating up at a rate, heat treatment for 10-30 hours and then naturally cooling.
도 4는 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정에 있어서의 흑연화 공정 사이클의 일례를 나타낸 것으로서, 상기 흑연화 공정은 상기 탄화 공정에서 처리된 탄소섬유 또는 탄소직물을 통상의 열처리로에서 불활성 분위기에서, 약 1000~1500℃까지는 100~200℃/시간의 승온속도로 승온시키고, 그 후 2000~2800℃의 온도까지는 50~100℃/시간의 승온속도로 승온시킨 후, 2000~2800℃의 온도에서 체류시간을 0~10시간으로 하여 열처리하여 수행된다.Figure 4 shows an example of the graphitization process cycle in the lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention, the graphitization process is a conventional heat treatment of the carbon fiber or carbon fabric treated in the carbonization process In an inert atmosphere at about 1000-1500 ° C., and then at a temperature increase rate of 100-200 ° C./hour, and then to a temperature of 2000-2800 ° C., at a temperature increase rate of 50-100 ° C./hour, then 2000-2800. It is carried out by heat treatment with a residence time of 0 to 10 hours at a temperature of ℃.
본 발명에 따르면, 라이오셀 섬유 또는 라이오셀 직물을 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 전처리 공정을 안정화 공정 전에 수행하므 로써 안정화 공정의 효과를 더욱 높일 수 있다.According to the present invention, the effect of the stabilization process can be further enhanced by performing a pretreatment step of immersing the lyocell fiber or lyocell fabric in the silicone polymer solution and the flame retardant salt solution before the stabilization process.
이하, 실시예를 통하여 본 발명을 더욱 상세히 설명하고자 한다. 단, 하기 실시예는 본 발명을 예시하는 것일 뿐, 본 발명의 내용이 하기 실시예에 의해 한정되는 것은 아니다. Hereinafter, the present invention will be described in more detail with reference to Examples. However, the following examples are illustrative of the present invention, and the contents of the present invention are not limited by the following examples.
[실시예][Example]
섬도 300tex 정도의 라이오셀 섬유를 라피어직기를 사용하여 능직 직물구조로 제직한 후, 순도 99.8%의 아세톤에 약 2시간 동안 침지시켜 세척하였다. 세척된 직물을 25℃에서 퍼클로로에틸렌에 용해된 실리콘계 고분자인 RTV 실리콘 5중량%의 용액에 약 30분 동안 침지한 후, 난연성 염인 염화암모늄 15중량%의 수용액에 약 30분 동안 침지하고, 이어서 80℃의 온도에서 건조시켰다. 상기 전처리된 직물은 열처리로에서, 30℃/시간의 승온속도로 200℃까지 온도를 올린 후, 2℃/시간의 낮은 승온속도로 300℃까지 온도를 올림으로써 안정화처리하였다. 그 후, 50℃/시간의 승온속도로 1700℃까지 온도를 올린 후, 10시간 동안 탄화처리를 하였으며, 그런 다음 100℃/시간의 승온속도로 2000℃까지 온도를 올리고 1시간 동안 유지하여 흑연화 처리를 수행하였다. 이에 의해서 얻어진 탄소직물 및 이 탄소직물로부터 뽑아낸 탄소섬유의 특성을 하기 표 1에 나타내었다.The lyocell fibers having a fineness of about 300 tex were woven into a twill weave structure using a rapier weaving machine, and then washed by dipping in acetone having a purity of 99.8% for about 2 hours. The washed fabric was immersed in a solution of 5% by weight of RTV silicone, a silicone-based polymer dissolved in perchloroethylene at 25 ° C. for about 30 minutes, and then immersed in an aqueous solution of 15% by weight of ammonium chloride, a flame retardant salt, for about 30 minutes. It dried at the temperature of 80 degreeC. The pretreated fabric was stabilized by raising the temperature to 200 ° C. at a temperature increase rate of 30 ° C./hour in a heat treatment furnace and then raising the temperature to 300 ° C. at a low temperature increase rate of 2 ° C./hour. Thereafter, the temperature was raised to 1700 ° C. at a temperature rising rate of 50 ° C./hour, followed by carbonization for 10 hours. Treatment was carried out. The properties of the carbon fabric thus obtained and the carbon fibers extracted from the carbon fabric are shown in Table 1 below.
[비교예][Comparative Example]
상기 실시예에 있어서 전처리 공정인 실리콘계 고분자 용액 및 난연성 염 수용액에 침지처리하는 과정을 생략한 것을 제외하고는, 실시예와 동일하게 처리하여 얻어진 탄소직물 및 이 탄소직물로부터 뽑아낸 탄소섬유의 특성을 하기 표 1에 나타내었다.Except for omitting the immersion treatment in the silicone-based polymer solution and flame retardant salt solution in the pretreatment step in the above embodiment, the characteristics of the carbon fabric obtained by the same process as the embodiment and the carbon fiber extracted from the carbon fabric It is shown in Table 1 below.
주) week)
안정화율(%) : 안정화 공정 후 탄소함량%Stabilization rate (%): Carbon content% after stabilization process
도 1은 본 발명에 의한 라이오셀계 탄소직물 제조공정의 일례를 도시한 순서도이고,1 is a flow chart showing an example of a lyocell-based carbon fabric manufacturing process according to the present invention,
도 2는 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정에 있어서의 안정화 공정 사이클의 일례를 나타내는 도면이고,2 is a view showing an example of the stabilization process cycle in the lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention,
도 3은 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정에 있어서의 탄화 공정 사이클의 일례를 나타내는 도면이고,3 is a view showing an example of a carbonization process cycle in the lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention,
도 4는 본 발명에 의한 라이오셀계 탄소섬유 및 탄소직물 제조공정에 있어서의 흑연화 공정 사이클의 일례를 나타내는 도면이고,4 is a view showing an example of the graphitization process cycle in the lyocell-based carbon fiber and carbon fabric manufacturing process according to the present invention,
도 5는 본 발명에 의해 제조된 라이오셀 탄소직물의 형상 사진이다.Figure 5 is a shape photograph of the lyocell carbon fabric produced by the present invention.
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