KR20220040841A - Method Of Manufactoring Eco-Friendly High-Density Wiper For Semiconductor Clean Room - Google Patents
Method Of Manufactoring Eco-Friendly High-Density Wiper For Semiconductor Clean Room Download PDFInfo
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- 238000000034 method Methods 0.000 title claims abstract description 29
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04B—KNITTING
- D04B1/00—Weft knitting processes for the production of fabrics or articles not dependent on the use of particular machines; Fabrics or articles defined by such processes
- D04B1/22—Weft knitting processes for the production of fabrics or articles not dependent on the use of particular machines; Fabrics or articles defined by such processes specially adapted for knitting goods of particular configuration
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- A—HUMAN NECESSITIES
- A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
- A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
- A47L13/00—Implements for cleaning floors, carpets, furniture, walls, or wall coverings
- A47L13/10—Scrubbing; Scouring; Cleaning; Polishing
- A47L13/16—Cloths; Pads; Sponges
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B1/00—Cleaning by methods involving the use of tools
- B08B1/10—Cleaning by methods involving the use of tools characterised by the type of cleaning tool
- B08B1/14—Wipes; Absorbent members, e.g. swabs or sponges
- B08B1/143—Wipes
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- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02J—FINISHING OR DRESSING OF FILAMENTS, YARNS, THREADS, CORDS, ROPES OR THE LIKE
- D02J13/00—Heating or cooling the yarn, thread, cord, rope, or the like, not specific to any one of the processes provided for in this subclass
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04B—KNITTING
- D04B1/00—Weft knitting processes for the production of fabrics or articles not dependent on the use of particular machines; Fabrics or articles defined by such processes
- D04B1/14—Other fabrics or articles characterised primarily by the use of particular thread materials
- D04B1/16—Other fabrics or articles characterised primarily by the use of particular thread materials synthetic threads
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- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B3/00—Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating
- D06B3/04—Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of yarns, threads or filaments
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- D06C—FINISHING, DRESSING, TENTERING OR STRETCHING TEXTILE FABRICS
- D06C7/00—Heating or cooling textile fabrics
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/67—Apparatus specially adapted for handling semiconductor or electric solid state devices during manufacture or treatment thereof; Apparatus specially adapted for handling wafers during manufacture or treatment of semiconductor or electric solid state devices or components ; Apparatus not specifically provided for elsewhere
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Abstract
Description
본 발명은 반도체 제조라인에서 사용되는 극세사 와이퍼 제품의 고수축 공정시 사용되는 벤질알코올 유화액을 사용하지 않고 고수축공정을 함으로써 비휘발성 잔류물질(NVR)로 인한 반도체 제조 시의 문제 및 환경적 문제를 해결할 수 있는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법에 관한 것이다. The present invention solves problems and environmental problems in semiconductor manufacturing due to non-volatile residue (NVR) by performing a high shrinkage process without using benzyl alcohol emulsion used in the high shrinkage process of microfiber wiper products used in semiconductor manufacturing lines. It relates to a method of manufacturing an eco-friendly high-density wiper for a semiconductor manufacturing clean room that can be solved.
한국은 글로벌 메모리반도체 시장 1·2위 기업을 보유하고 있으며, 두 기업의 시장점유율 합계는 2018년 기준 D램 73%, 낸드플래시 46%로 세계시장에서 두각을 나타내고 있다.Korea has the first and second largest companies in the global memory semiconductor market, and the combined market share of the two companies is 73% for DRAM and 46% for NAND flash as of 2018.
이러한 반도체 제조공정의 미세화가 가속화될수록 미량의 불순물로도 불량발생 가능성이 커지므로 세정의 중요성이 커지는 추세이다. 세정은 반도체 메인 공정 중 약 15%를 차지하며 제품성능과 신뢰성, 수율과 직결되는 매우 중요한 공정으로서 회로 선폭이 미세화 시에는 라인이 좁고 깊어지게 되어 불순물을 제거하기가 더욱 어려워져 세정의 중요성이 점차 커지고 있다.As the miniaturization of the semiconductor manufacturing process is accelerated, the possibility of defects occurring even with a small amount of impurities increases, so the importance of cleaning is increasing. Cleaning accounts for about 15% of the main semiconductor process and is a very important process that is directly related to product performance, reliability, and yield. is growing
극세사 와이퍼 제품은 이러한 반도체 제조공정에서 발생한 다양한 잔류물과 이물질 등 오염원으로부터 세정하는데 사용되는 소재로서 반도체 품질에 직접적으로 영향을 끼치는 핵심제품이다.Microfiber wiper products are a core product that directly affects semiconductor quality as a material used to clean from contaminants such as various residues and foreign substances generated in the semiconductor manufacturing process.
이성분 폴리머의 복합방사로 제조된 극세사는 복합과정 후 표면적이 비약적으로 상승하여 제거가 어려운 미세 굴곡부위에서도 뛰어난 오염제거 메커니즘을 가지고 있는데, 특히 고청정 환경이 요구되는 반도체 제조공정에서의 사용을 위해 벤질알코올 유화액을 사용한 고수축가공 공정 및 이를 사용한 고성능 와이퍼 소재가 개발되어 사용되고 있다.Microfibers manufactured by composite spinning of two-component polymers have an excellent decontamination mechanism even in minute curved areas that are difficult to remove due to a dramatic increase in surface area after the compounding process. A high shrinkage processing process using an alcohol emulsion and a high-performance wiper material using the same have been developed and used.
일본 가네보가 1975년 복합분할사인 베리마X를 출시한 이후, KB세이렌은 클린룸용 제품인 SAVINA MX를 개발하여 상업화하기 시작하였으며, SAVINA MX는 섬도 100d/50f와 40d/25f의 복합분할사 환편물로 산업용 고청정 와이퍼를 제조하여 널리 사용되고 있다. KB세이렌에서 생산된 제품은 반도체/집적회로 제조나 카메라용 정밀부품 어셈블리 등의 공정에서 최고의 고기능 와이퍼로 사용되고 있다.After Kanebo of Japan launched Verima X, a multi-split yarn in 1975, KB Siren developed and commercialized SAVINA MX, a cleanroom product, and SAVINA MX is a circular knitted fabric with multi-split yarns with fineness of 100d/50f and 40d/25f. It is widely used by manufacturing industrial high-clean wipers. Products produced by KB Siren are used as the best high-performance wipers in processes such as semiconductor/integrated circuit manufacturing and camera precision parts assembly.
이러한 고성능 와이퍼 제품은 전처리 후 고농도의 NaOH 수용액에 침지/습열처리하여 감량분할한 후 batch식 혹은 연속식의 벤질알코올 유화액 처리를 통해 고수축하는 고수축 가공을 통해 제조되어 왔는데, 이러한 극세사 와이퍼는 일반 저가형 와이퍼 대비 우수한 와이핑성을 가지고 있으나, 전술한 바와 같이 벤질알코올을 사용한 고수축공정을 적용하고 있어 상대적으로 높은 NVR을 나타내어 제조공정 중 안전 상 취급에 특별한 주의가 필요하다. 특히, 이러한 고수축 고밀도 와이퍼는 일단 수축이 된 이후에는 매우 치밀한 조직을 가지게 되어 내부의 잔류물질을 배출하기 위해서는 매우 가혹한 조건의 수세를 반복적으로 시행하여야 하며, 이를 완전히 제거하기 어려워 일반 와이퍼에 비해 보다 많은 비휘발성 잔류물질(NVR, Non-Volatile Residue)이 검출되고 있는 실정이다.These high-performance wiper products have been manufactured through high-shrinkage processing, which is reduced by immersion/moist heat treatment in high-concentration NaOH aqueous solution after pretreatment, and high-shrinkage through batch or continuous benzyl alcohol emulsion treatment. It has superior wiping properties compared to low-cost wipers, but as described above, a high-shrinkage process using benzyl alcohol is applied, so it exhibits a relatively high NVR. In particular, this high-shrink high-density wiper has a very dense structure once it is shrunk, so it is necessary to repeatedly perform water washing under very harsh conditions to discharge the residual substances inside, and it is difficult to completely remove it Many non-volatile residues (NVR, Non-Volatile Residue) are being detected.
상기 NVR은 와이퍼 제조공정 중 사용된 화학물질이 완전히 제거되지 않아 와이핑 시 반도체를 도리어 오염시킬 수 있기 때문에 핵심적인 성능으로 인식되고 있다. 이러한 벤질알코올은 주로 방부제로 사용되는데 알러지를 유발하고 내장기관 독성(불임유발 우려) 위험성이 있는 것으로 알려진 유해물질로 취급에 특별한 주의가 필요하다. 또한 세계적으로 환경규제가 갈수록 강화되어가고 있으며, 친환경 공정이 강조되어 가고 있어 친환경적인 제조 공정의 적용이 절실히 요구되고 있는 실정이다. The NVR is recognized as a core performance because the chemicals used during the wiper manufacturing process are not completely removed and can contaminate the semiconductor during wiping. Benzyl alcohol is mainly used as a preservative, but special attention is required in handling as it is a toxic substance known to cause allergies and have a risk of internal organ toxicity (infertility risk). In addition, environmental regulations around the world are getting stronger and eco-friendly processes are being emphasized, so the application of eco-friendly manufacturing processes is urgently required.
따라서 본 발명에서는 파티클이 극도로 적은 청정 환경인 반도체 제조공정에 적용 가능한 고밀도 와이퍼를 제조함에 있어 비휘발성 잔류물질(NVR)의 발생을 최소화하고 유해한 공정을 사용하지 않는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법을 제공하는 것을 기술적과제로 한다.Therefore, in the present invention, in manufacturing a high-density wiper applicable to a semiconductor manufacturing process, which is a clean environment with extremely few particles, the generation of non-volatile residues (NVR) is minimized and an eco-friendly high-density wiper for a semiconductor manufacturing clean room that does not use a harmful process It is a technical task to provide a manufacturing method.
그러므로 본 발명에 의하면, 폴리아미드부분과 폴리에스테르부분으로 이루어진 NP분할복합사의 DTY가공사를 양면환편기에 공급하여 편직한 후, 80~90℃에서 정련하고, 100~130℃, 알칼리용액하에서 감량분할 및 고수축가공을 한 후, 180~195℃, 30~40m/min으로 열고정하는 것을 특징으로 하는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법이 제공된다.Therefore, according to the present invention, the DTY processing yarn of the NP split composite yarn consisting of a polyamide part and a polyester part is supplied to a double-sided circular knitting machine and knitted, and then refined at 80 to 90 ° C. There is provided a method of manufacturing an eco-friendly high-density wiper for a semiconductor manufacturing clean room, characterized in that heat setting is performed at 180 to 195° C. and 30 to 40 m/min after high shrinkage processing.
이하 본 발명을 보다 상세히 설명하기로 한다. Hereinafter, the present invention will be described in more detail.
본 발명은 반도체 제조라인에서 사용되는 극세사 와이퍼 제품의 고수축 공정시 사용되는 벤질알코올 유화액을 사용하지 않고 고수축공정을 함으로써 비휘발성 잔류물질(NVR)로 인한 반도체 제조 시의 문제 및 환경적 문제를 해결할 수 있는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법에 관한 것이다. The present invention solves problems and environmental problems in semiconductor manufacturing due to non-volatile residue (NVR) by performing a high shrinkage process without using benzyl alcohol emulsion used in the high shrinkage process of microfiber wiper products used in semiconductor manufacturing lines. It relates to a method of manufacturing an eco-friendly high-density wiper for a semiconductor manufacturing clean room that can be solved.
본 발명의 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법은 크게 원사의 DTY가공, 편직, 정련, 감량분할·고수축가공의 순으로 이루어진다. The manufacturing method of the eco-friendly high-density wiper for a semiconductor manufacturing clean room of the present invention is largely composed of yarn DTY processing, knitting, refining, weight reduction division and high shrinkage processing in the order.
본 발명에서 사용되는 원사는 폴리아미드부분과 폴리에스테르부분으로 이루어진 NP분할복합사로서 상기 폴리에스테르부분이 중량비 80:20~90:10인 TPA와 IPA(Isophthalic acid)가 EG(Ethylene Glycol)와 반응되어 이루어진 고수축 폴리에스테르인 NP분할복합사를 사용한다.The yarn used in the present invention is an NP split composite yarn composed of a polyamide part and a polyester part. TPA and IPA (Isophthalic acid) in which the polyester part has a weight ratio of 80:20 to 90:10 are reacted with EG (Ethylene Glycol) NP split composite yarn, which is a high-shrink polyester, is used.
일반 폴리에스테르는 TPA(Terephthalic acid)와 EG(Ethylene Glycol)의 축중합체이며, 주로 TPA는 결정영역, EG는 비결정영역 형성에 기여하는 것으로 알려지고 있다. 본 발명에서는 이러한 중합과정에서 TPA와 IPA(Isophthalic acid)를 중량비 80:20~90:10로 공급하여 EG와 반응시켜 공중합한 것으로서 TPA의 결정영역이 감소하여 열에 의한 수축률이 증가하게 되어 고수축 폴리에스테르가 된다. General polyester is a condensate of TPA (Terephthalic acid) and EG (Ethylene Glycol), and it is known that TPA mainly contributes to the formation of a crystalline region and EG contributes to the formation of an amorphous region. In the present invention, in the polymerization process, TPA and Isophthalic acid (IPA) are supplied in a weight ratio of 80:20 to 90:10 and reacted with EG to be copolymerized. becomes an ester.
이러한 고수축 폴리에스테르와 나일론수지를 통상의 방법으로 복합방사하여 NP분할복합사를 제조하게 되는데, 이러한 고수축 NP복합분할사는 수축가공을 통해 밀도가 매우 높아 형태안정성을 가지면서 분할사 비표면적의 증가로 와이핑성이 뛰어난 특징이 있다.NP split composite yarn is manufactured by composite spinning of such high shrinkage polyester and nylon resin in a conventional way. This high shrinkage NP composite split yarn has a very high density through shrinkage processing and thus has dimensional stability while reducing the specific surface area of the split yarn. It has excellent wiping properties due to the increase.
이렇게 제조된 고수축 NP복합분할사는 폴리에스테르부분의 비결정영역을 늘리고자 중합과정에서 IPA를 첨가하여 제조함으로써 향상된 열수축성을 통해 벤질알코올계 유화액을 사용하지 않고도 고수축이 가능한 장점이 있다.The high shrinkage NP composite split yarn prepared in this way has the advantage of being able to have high shrinkage without using benzyl alcohol emulsion through improved heat shrinkage by adding IPA in the polymerization process to increase the amorphous region of the polyester part.
본 발명에서는 상기 NP복합분할사를 그대로 사용하기보다는 NP복합분할사에 열을 가하면서 꼬았다가 풀어주어 필라멘트사에 벌키성을 부여함과 동시에 NP 계면에서의 초기 분할을 촉진시키기 위하여 DTY가공사를 만들어 제직 또는 편직에 사용하게 된다.In the present invention, rather than using the NP composite split yarn as it is, twist and untwist while applying heat to the NP composite split yarn to give bulkiness to the filament yarn and at the same time to promote the initial split at the NP interface. It is made and used for weaving or knitting.
이러한 DTY가공사는 상기 NP분할복합사를 제1피드롤러에 통과시키고 140~ 160℃의 제1차히터에서 열처리한 후, 디스크형가연장치로 가연비 1.3~1.4로 가연하면서 제2피드롤러를 통과시키면서 연신비 1.10~1.35로 연신한 후, 공기압력 13~16kgf/㎠로 교락한 후 사속 400~550m/min으로 권취하여 제조하게 된다.This DTY processing worker passes the NP split composite yarn through the first feed roller and heat-treats it in the first heater at 140 to 160 ° C. After stretching at a draw ratio of 1.10 to 1.35 while making it, it is entangled with an air pressure of 13 to 16 kgf/cm 2 and wound up at a yarn speed of 400 to 550 m/min.
제1히터온도가 140℃미만일 경우에는 가연사의 벌키성이 떨어지며, 160℃초과일 경우에는 미해연이 발생되거나 융착이 발생하는 문제점이 발생될 수 있다.When the temperature of the first heater is less than 140 ℃, the bulkiness of the false twisted yarn is deteriorated, and when it is more than 160 ℃, there may be problems in that untwisted or fusion occurs.
상기 가연을 행한 후 제2피드롤러를 통과시키는데, 제1피드롤러와 제2피드롤러의 속도차를 이용하여 필라멘트를 연신하게 된다. 이때 연신비는 1.10~1.35배인 것이 바람직한데, 연신비가 1.10배보다 적으면 미해연이 발생되어 가연사의 균제도가 떨어지며, 1.35배 초과일 경우에는 사절이 발생하거나 편직준비 및 편직단계에서의 작업성 저하 등의 문제점을 야기시킨다. After performing the false twist, it passes through the second feed roller, and the filament is drawn by using the speed difference between the first feed roller and the second feed roller. At this time, it is preferable that the draw ratio is 1.10 to 1.35 times. If the draw ratio is less than 1.10 times, untwisted occurs and the uniformity of the false twisted yarn is lowered. cause the problems of
상기 연신후 인터레이스노즐에서 교락하고 사속 400~550m/min으로 권취롤러로 권취하여 DTY가공사를 완성하게 되는데, 상기 제2피드롤러를 통과한 필라멘트는 집속성 향상을 위하여 교락을 하게 되는데, 교락시 공기압력은 13~16kgf/㎠가 바람직한데, 압력이 16kgf/㎠초과일 경우, 편직 후에 원단 표면에 인터레이스 자국이 발생할 수 있으며, 13kgf/㎠미만일 경우 편직 시에 위단발생 및 편직불량의 문제점이 발생될 수 있다.After the stretching, it is entangled in the interlace nozzle and wound with a winding roller at a yarn speed of 400 to 550 m/min to complete the DTY processing. The pressure is preferably 13-16kgf/cm2. If the pressure exceeds 16kgf/cm2, interlacing marks may occur on the surface of the fabric after knitting. can
이렇게 준비한 NP분할복합사의 DTY가공사를 양면환편기에 공급하여 편직하게 된다.The DTY processing of the NP split composite yarn prepared in this way is supplied to a double-sided circular knitting machine and knitted.
상기 편직후 80~90℃에서 정련하고, 100~130℃, 알칼리용액하에서 감량분할 및 고수축가공을 한 후, 180~195℃, 30~40m/min으로 열고정하여 본 발명의 클린룸용 친환경 고밀도 와이퍼를 제조하게 된다.After knitting, refining at 80~90℃, reducing division and high shrinkage under 100~130℃, alkali solution, heat setting at 180~195℃, 30~40m/min, eco-friendly high-density wiper for clean room of the present invention will be manufactured
정련공정은 80~90℃에서 15~20분간 행하며, 감량분할 공정 및 고수축 공정은100~130℃, 알칼리(NaOH) 용액 하에서 행하게 된다. 열고정은 180~195℃, 30~40m/min으로 하여 열고정 체임버 내에서 50~60초간 체류하게 한다. The refining process is carried out at 80~90℃ for 15~20 minutes, and the reduction division process and the high shrinkage process are performed at 100~130℃, under an alkali (NaOH) solution. The heat setting is 180~195℃, 30~40m/min, and it is allowed to stay in the heat setting chamber for 50~60 seconds.
상기 분할 및 고수축가공시 분할도는 80~90%, 수축률은 20~30%인 것이 고밀도 와이퍼의 형태안정성과 와이핑성에 바람직하다.It is preferable that the degree of division is 80 to 90%, and the shrinkage is 20 to 30% during the division and high shrinkage processing, and the shape stability and wiping property of the high-density wiper are preferable.
기존의 NP분할사를 사용한 극세사 와이퍼의 고수축 가공은 합성섬유 고분자쇄의 구조적 변형을 위해 벤질알코올계 유화액을 사용하였는데, 상기 벤질알코올은 내장기관 독성을 가진 것으로 알려져 있어 취급 상 주의를 요하고 폐수처리가 까다로운 치명적인 단점을 가지고 있어서 환경 친화적인 공정으로의 전환이 절실히 요구되고 있다.The high shrinkage processing of the microfiber wiper using the existing NP split yarn used a benzyl alcohol-based emulsion for structural modification of the synthetic fiber polymer chain. It has a fatal disadvantage that it is difficult to treat, so conversion to an environmentally friendly process is urgently required.
또한, 기존의 NP분할사를 사용한 극세사 와이퍼는 일반 저가형 와이퍼 대비 우수한 와이핑성을 가지고 있으나, 전술한 바와 같이 벤질알코올을 사용한 고수축공정을 적용하고 있어 상대적으로 높은 NVR을 나타낸다. 이러한 고수축 고밀도 와이퍼는 일단 수축이 된 이후에는 매우 치밀한 조직을 가지게 되어 내부의 잔류물질을 배출하기 위해서는 매우 가혹한 조건의 수세를 반복적으로 시행하여야 하며, 그럼에도 완벽한 제거는 어려운데 반하여, 본원발명에 의한 와이퍼는 폴리에스테르부분의 비결정영역을 늘리고자 중합과정에서 IPA를 첨가하여 제조함으로써 향상된 열수축성을 통해 벤질알코올계 유화액을 사용하지 않고도 고수축이 가능하여 화학약품을 거의 사용하지 않아 NVR이 크게 저감될 수 있으며, 수세공정을 단순화 할 수 있어 비용면에서도 매우 유리하다.In addition, the existing microfiber wipers using NP split yarns have superior wiping properties compared to general inexpensive wipers, but as described above, a high shrinkage process using benzyl alcohol is applied, thereby exhibiting a relatively high NVR. This high-shrink high-density wiper has a very dense structure once it is shrunk, so it is necessary to repeatedly perform water washing under very severe conditions in order to discharge the residual material inside. is manufactured by adding IPA in the polymerization process to increase the amorphous region of the polyester part, and through improved heat shrinkability, high shrinkage is possible without using benzyl alcohol emulsion. In addition, the washing process can be simplified, which is very advantageous in terms of cost.
그러므로 본 발명에 의하면 와이핑성능이 우수하면서도 기존의 감량분할, 고수축의 공정을 통합하고 고수축공정시 상기 벤질알코올계 유화액을 사용하지 않으므로 NVR이 저감되어 친환경적이며 에너지/용수는 약 50%, 제조원가는 약 25% 이상 절감이 가능한 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법을 제공할 수 있다. Therefore, according to the present invention, while wiping performance is excellent, the existing reduction division and high shrinkage processes are integrated, and the benzyl alcohol-based emulsion is not used during the high shrinkage process, so the NVR is reduced and eco-friendly, and energy/water is about 50%, It is possible to provide a manufacturing method of an eco-friendly high-density wiper for a semiconductor manufacturing clean room that can reduce manufacturing cost by about 25% or more.
도 1은 본 발명의 실시예 1에 의해 제조된 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 표면현미경사진이며,
도 2는 본 발명의 실시예 1에 의해 제조된 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 단면현미경사진이다.1 is a surface micrograph of an eco-friendly high-density wiper for a semiconductor manufacturing clean room manufactured according to Example 1 of the present invention;
2 is a cross-sectional micrograph of an eco-friendly high-density wiper for a semiconductor manufacturing clean room manufactured according to Example 1 of the present invention.
다음의 실시예에서는 본 발명의 반도체 제조 클린룸용 친환경 고밀도 와이퍼를 제조하는 비한정적인 예시를 하고 있다.In the following embodiment, a non-limiting example of manufacturing an eco-friendly high-density wiper for a semiconductor manufacturing clean room of the present invention is given.
[실시예 1][Example 1]
TPA와 IPA(Isophthalic acid)를 중량비 80:20로 하고 EG(Ethylene Glycol)와 반응되어 이루어진 고수축 폴리에스테르와 나일론을 복합방사하여 얻은 NP복합분할사(75D/48f, 7분할, PET:Nylon=70:30)를 하기 표 1의 조건에 의해 DTY가공한 후,양면환편기에 공급하여 Interlock 조직으로 편직하였다(32G).NP composite split yarn (75D/48f, 7-split, PET:Nylon= 70:30) was subjected to DTY processing according to the conditions in Table 1 below, and then supplied to a double-sided circular knitting machine and knitted with an interlock structure (32G).
정련은 90℃ x 15min, 감량분할/고수축(액류 Rapid)은 130℃ 20min간, NaOH 3.0%농도 하에서 행하여 분할도 80%, 수축률 20%가 되도록 실시하였다. 열고정 조건은 185℃ x 40m/min의 조건으로 행하였다.Refining was carried out at 90° C. x 15 min, and reduction division/high shrinkage (liquid flow rapid) was performed at 130° C. for 20 min at a concentration of 3.0% NaOH, so that the division degree was 80% and the shrinkage rate was 20%. The heat setting conditions were 185°C x 40 m/min.
[비교예 1][Comparative Example 1]
일반 NP분할사를 양면환편기에 공급하여 Interlock 조직으로 편직하고(32G), 정련은 90℃ x 15min, 감량분할은 100℃, 30분간 NaOH 3.0%농도 하에서 행한 후, 고수축은 130℃ 20min간 벤질알코올 유화액을 사용하여 분할도 80%, 수축률 20%가 되도록 실시하였다. 열고정 조건은 185℃ x 40m/min의 조건으로 행하였다.General NP split yarn to double-sided circular knitting machine Supply and knit with an interlock structure (32G), scouring at 90℃ x 15min, reducing division at 100℃ for 30 minutes under NaOH 3.0% concentration, high shrinkage at 130℃ for 20min using benzyl alcohol emulsion, splitting degree 80 %, the shrinkage rate was 20%. Heat setting conditions were performed under the conditions of 185°C x 40 m/min.
제조된 실시예 1 및 비교예 1의 와이퍼의 물성분석결과는 다음 표 2와 같다.The results of physical property analysis of the wipers of Example 1 and Comparative Example 1 are shown in Table 2 below.
- 원단상태에서 분할된 원사의 개수를 측정
- 외부전문가 입회 시험하여 결과 확인microscopy
- Measure the number of divided yarns in the fabric state
- Test results in the presence of external experts
- 중금속은 산을 사용하여 물질을 저분자화하고 분광분석기를 사용하여 정량분석함.
-화합물은 추출기를 사용하여 추출 후 분광분석기를 사용하여 정량분석함.Quantitative analysis through GC, LC, ICP, etc.
- Heavy metals are reduced in molecular weight using acids and quantitatively analyzed using a spectrometer.
-The compound is extracted using an extractor and then quantitatively analyzed using a spectrometer.
용매 100㎖ 넣은 orbital shaker에 교반한 후
Reflux condensor가 장착된 250㎖ Round Flask에 교반액을 넣고 Hot plate를 사용하여 용매를 10㎖ 이하가 되도록 농축.
이 농축액을 무게가 측정된 Aluminium Dish에 넣고
200℃ Oven에 넣고 용매를 증발시킨 후 무게를 측정Precisely measure the weight of one wiper to 5 significant digits.
After stirring on an orbital shaker containing 100 ml of solvent
Put the stirring solution in a 250ml round flask equipped with a reflux condensor and use a hot plate to concentrate the solvent to 10ml or less.
This concentrate is placed in a weighed aluminum dish and
Put it in an oven at 200℃, evaporate the solvent, and then measure the weight.
시간absorption
hour
시편의 1cm 위에서 정중앙에 Auto dispensor를 이용하여 물 1ml를 가한 후 각인한 부분까지 물이 도달하는 시간을 측정Engraved using a rubber seal with a diameter of 6 cm in the center of the specimen.
Measure the time it takes for water to reach the engraved part after adding 1ml of water using an auto dispenser to the center of the specimen 1cm above it.
시편의 0.5cm 부위를 물에 담그고 1cm 통과하는 시점부터 4cm 통과하는 시점의 시간을 측정Cut the specimen to 2 cm in width and 5 cm in length, and mark the cut specimen with a line at 1 cm and 4 cm positions.
Immerse a 0.5 cm part of the specimen in water and measure the time from the time it passes 1 cm to the time it passes 4 cm.
D.I. Water가 담긴 수조에 와이퍼를 30초간 침지.
흡수가 완료된 와이퍼를 꺼내어 30초간 자연스럽게
물을 탈수한 후 탈수된 시험편의 중량을 소수점 2자리까지 측정Weigh the wipers
Immerse the wiper in a water bath containing DI Water for 30 seconds.
Take out the wiper that has been absorbed and take it out naturally for 30 seconds
After dehydrating the water, measure the weight of the dehydrated specimen to 2 decimal places.
이 액을 Liquid Particle Counter를 사용하여 ㎖당 Particle 수를 측정하여 기록.Put one wiper into a Sus Tray containing 100ml of DI Water and stir at 100rpm for 3 minutes using a Biaxial Shaker.
Measure and record the number of particles per ml using the Liquid Particle Counter of this solution.
(Fiber)Lint
(Fiber)
넣고 Orbital Shaker를 이용하여 100rpm 3분동안 교반.
Wiper를 핀셋으로 건져낸 후 교반된 D.I. Water를
여과지가 장착된 여과장치를 이용하여 여과.
여과된 여과지를 건조한 후 Microscope를 사용하여 100마이크로 이상의 Lint의 숫자를 기록.Put 1 wiper in the Sus Tray containing 100ml of DI Water.
and stirred for 3 minutes at 100rpm using an Orbital Shaker.
After removing the wiper with tweezers, use the stirred DI Water.
Filtration using a filter device equipped with filter paper.
After drying the filtered paper, record the number of lints over 100 micrometers using a microscope.
Claims (4)
상기 NP분할복합사의 폴리에스테르부분은 중량비 80:20~90:10인 TPA와 IPA(Isophthalic acid)가 EG(Ethylene Glycol)와 반응되어 이루어진 고수축 폴리에스테르인 것을 특징으로 하는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법.The method of claim 1,
The polyester part of the NP split composite yarn is a high-shrinkage polyester made by reacting TPA and IPA (Isophthalic acid) with a weight ratio of 80:20 to 90:10 with EG (Ethylene Glycol). A method of manufacturing a wiper.
상기 NP분할복합사의 DTY가공사는 NP분할복합사를 제1피드롤러에 통과시키고 140 ~ 160℃의 제1차히터에서 열처리한 후, 디스크형가연장치로 가연비 1.3~1.4로 가연하면서 제2피드롤러를 통과시키면서 연신비 1.10~1.35로 연신한 후, 공기압력 13~16kgf/㎠로 교락한 후 사속 400~550m/min으로 권취한 DTY가공사인 것을 특징으로 하는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법.The method of claim 1,
The DTY processing worker of the NP split composite yarn passes the NP split composite yarn through the first feed roller and heat-treats it in the first heater at 140 ~ 160 ° C. A method of manufacturing an eco-friendly high-density wiper for a semiconductor manufacturing clean room, characterized in that it is a DTY processing worker that is stretched at a draw ratio of 1.10 to 1.35 while passing through a roller, entangled at an air pressure of 13 to 16 kgf/cm2, and then wound at a yarn speed of 400 to 550 m/min. .
상기 알칼리용액 하에서 감량분할 및 고수축가공시 분할도는 80~90%, 수축률은 20~30%인 것을 특징으로 하는 반도체 제조 클린룸용 친환경 고밀도 와이퍼의 제조 방법.The method of claim 1,
The method of manufacturing an eco-friendly high-density wiper for a semiconductor manufacturing clean room, characterized in that the degree of division is 80 to 90% and the shrinkage is 20 to 30% during reduction division and high shrinkage processing under the alkali solution.
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Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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KR910007890A (en) * | 1989-10-24 | 1991-05-30 | 오일러, 라피체 | Method for preparing aminopyrimidine |
KR20030006773A (en) * | 2001-07-16 | 2003-01-23 | 주식회사 효성 | Process for preparing a high shrinkage polyester fiber |
KR100704382B1 (en) * | 2005-11-07 | 2007-04-06 | 주식회사 새 한 | Manufacturing method of knit-wiper for use of lcd or semiconductor plants and knit-wiper thereby |
KR20100032002A (en) | 2008-09-17 | 2010-03-25 | 주식회사 코오롱 | Method of manufacturing a woven wiping cloth |
KR20120045563A (en) * | 2010-10-29 | 2012-05-09 | (재)한국섬유소재연구소 | Low lint knitting using nylon/polyester partition yarn, process for manufacturing the same |
-
2020
- 2020-09-24 KR KR1020200124057A patent/KR102486315B1/en active IP Right Grant
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR910007890A (en) * | 1989-10-24 | 1991-05-30 | 오일러, 라피체 | Method for preparing aminopyrimidine |
KR20030006773A (en) * | 2001-07-16 | 2003-01-23 | 주식회사 효성 | Process for preparing a high shrinkage polyester fiber |
KR100704382B1 (en) * | 2005-11-07 | 2007-04-06 | 주식회사 새 한 | Manufacturing method of knit-wiper for use of lcd or semiconductor plants and knit-wiper thereby |
KR20100032002A (en) | 2008-09-17 | 2010-03-25 | 주식회사 코오롱 | Method of manufacturing a woven wiping cloth |
KR20120045563A (en) * | 2010-10-29 | 2012-05-09 | (재)한국섬유소재연구소 | Low lint knitting using nylon/polyester partition yarn, process for manufacturing the same |
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