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KR920001014A - Nonwoven web with improved barrier properties - Google Patents

Nonwoven web with improved barrier properties
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Publication number
KR920001014A
KR920001014AKR1019910009952AKR910009952AKR920001014AKR 920001014 AKR920001014 AKR 920001014AKR 1019910009952 AKR1019910009952 AKR 1019910009952AKR 910009952 AKR910009952 AKR 910009952AKR 920001014 AKR920001014 AKR 920001014A
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South Korea
Prior art keywords
web
nonwoven web
microns
polymer
pore size
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KR1019910009952A
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KR0158457B1 (en
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크레이머 티먼스 테리
미칼로비치 코빌리브커 피터
운 린-순
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존 웨인 돈하우어
킴벌리-클라크 코포레이션
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Application filed by 존 웨인 돈하우어, 킴벌리-클라크 코포레이션filedCritical존 웨인 돈하우어
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Abstract

Translated fromKorean

내용 없음No content

Description

Translated fromKorean
배리어(barrier)특성이 개선된 부직 웹(web)Nonwoven web with improved barrier properties

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 본 발명의 용융 취입 배리어층을 포함하는 부직포 라미네이트 제조에 사용되는 형성기의 개략도,1 is a schematic diagram of a former for use in the manufacture of a nonwoven laminate comprising a melt blown barrier layer of the present invention,

제2도는 본 발명에 의해 제조된 내부 용융 취입 배리어층을 포함하는 층 배열을 나타내는 본 발명의 부직포 라미네이트의 단면도,2 is a cross-sectional view of a nonwoven laminate of the present invention showing a layer arrangement comprising an internal melt blown barrier layer prepared by the present invention,

제3도는 본 발명에 의해 제조된 용융 취입 웹(시료1), 배리어층으로서 용융 취입 웹을 혼입한 SMS직물 라미네이트(시트2), 통상의 용융 취입 웹(시료3), 및 통상의 SMS직물 라미네이트(시료4)에 대한 공극크기 분포를 나타내는 그래프.3 is a melt blown web (sample 1) prepared according to the present invention, an SMS fabric laminate (sheet 2) incorporating the melt blown web as a barrier layer, a conventional melt blown web (sample 3), and a conventional SMS fabric laminate. Graph showing pore size distribution for (Sample 4).

Claims (19)

Translated fromKorean
중합체의 분자량 분포가 2.2 내지 3.5Mw/Mn이고, 용융 유속이 230℃에서 800gms/10min를 초과하는 개질된 중합체의 반응기 과립으로부터 형성된 미세 섬유의 부직 웹.A nonwoven web of fine fibers formed from reactor granules of modified polymer having a molecular weight distribution of 2.2 to 3.5 Mw / Mn and a melt flow rate of greater than 800 gms / 10 min at 230 ° C.제1항에 있어서, 중합체 배출량이 3PIH를 초과할때 웹이 형성됨을 특징으로 하는 부직 웹.The nonwoven web of claim 1 wherein the web is formed when the polymer emissions exceed 3PIH.제1항에 있어서, 웹의 평균 섬유 크기가 1 내지 3미크론이고 공극 크기가 주로 7내지 12미크론 범위내에서 분포되고 공극 크기 분포의 피크가 10미크론 미만임을 특징으로 하는 부직 웹.The nonwoven web of claim 1 wherein the web has an average fiber size of 1 to 3 microns, a pore size is distributed primarily in the range of 7 to 12 microns and a peak of the pore size distribution is less than 10 microns.중합체의 분자량 분포가 2.8 내지 3.5Mw/Mn이고, 용융 유속이 230℃에서 3000gms/10min를 초과하는 개질된 중합체의 반응기 과립으로부터 형성된 부직 웹.A nonwoven web formed from reactor granules of modified polymer having a molecular weight distribution of 2.8 to 3.5 Mw / Mn and a melt flow rate of greater than 3000 gms / 10 min at 230 ° C.제4항에 있어서, 개질된 중합체가 웹을 형성하기 전에 500ppm이하의 과산화물을 반응기 과립에 첨가함으로써 생성되는 것을 특징으로 하는 부직 웹.The nonwoven web of claim 4 wherein the modified polymer is produced by adding up to 500 ppm of peroxide to the reactor granules before forming the web.제4항 또는 제5항에 있어서, 중합체 배출량이 3PIH를 초과할때 웹이 형성됨을 특징으로 하는 부직 웹.6. The nonwoven web of claim 4 or 5 wherein the web is formed when the polymer emissions exceed 3PIH.제4항 또는 제5항에 있어서, 웹의 평균 섬유 크기가 1 내지 3미크론이고 공극 크기가 주로 7내지 12미크론범위에서 분포되고 공극 크기분포의 피크가 10미크론 미만임을 특징으로 하는 부직 웹.6. The nonwoven web of claim 4 or 5, wherein the web has an average fiber size of 1 to 3 microns, a pore size mainly in the range of 7 to 12 microns, and a peak of the pore size distribution is less than 10 microns.중합체의 분자량 분포가 2.2 내지 2.8Mw/Mn이고, 용융 유속이 230℃에서 800gms/10min를 초과하는 개질된 중합체의 반응기 과립으로부터 형성된 부직 웹.A nonwoven web formed from reactor granules of modified polymer having a molecular weight distribution of 2.2 to 2.8 Mw / Mn and a melt flow rate of greater than 800 gms / 10 min at 230 ° C.제8항에 있어서, 개질된 중합체가 웹을 형성하기 전에 500 내지 3000ppm의 과산화물을 반응기 과립에 첨가함으로써 생성되는 것을 특징으로 하는 부직 웹.9. The nonwoven web of claim 8 wherein the modified polymer is produced by adding 500 to 3000 ppm peroxide to the reactor granules before forming the web.제8항 또는 제9항에 있어서, 이 3PIH를 초과할때 웹이 중합체 배출량 형성됨을 특징으로 하는 부직 웹.10. The nonwoven web of claim 8 or 9, wherein the web forms a polymer emissions when above 3PIH.제8항 또는 제9항에 있어서, 웹의 평균 섬유 크기가 1 내지 3미크론이고 공극 크기가 주로 7내지 12미크론범위에서 분포되고 공극 크기분포의 피크가 10미크론 미만임을 특징으로 하는 부직 웹.10. The nonwoven web of claim 8 or 9, wherein the web has an average fiber size of 1 to 3 microns, a pore size mainly in the range of 7 to 12 microns, and a peak of the pore size distribution is less than 10 microns.중합체의 분자량 분포가 2.2 내지 3.5Mw/Mn이고, 용융 유속이 230℃에서 800gms/10min를 초과하는 개질된 중합체의 반응기 과립으로부터 용융 취입하는 단계로 이루어지는 , 미세 섬유와 작은 공극 크기 분포를 갖는 부직 웹의 형성방법.Nonwoven web with fine fibers and small pore size distribution, consisting of melt blowing from reactor granules of modified polymer having a molecular weight distribution of 2.2 to 3.5 Mw / Mn and a melt flow rate of greater than 800 gms / 10 min at 230 ° C. Method of formation.제12항에 있어서, 중합체의 배출량이 3PIH를 초과함을 특징으로 방법.The method of claim 12, wherein the polymer has an emission greater than 3PIH.중합체의 분자량 분포가 2.8 내지 3.5Mw/Mn이고, 용융 유속이 230℃에서 3000gms/10min를 초과하는 개질된 중합체의 반응기 과립을 용융 취입하는 단계로 이루어지는 , 미세 섬유와 작은 공극 크기 분포를 갖는 부직 웹의 형성방법.Nonwoven web with fine fibers and small pore size distribution, consisting of melt blowing a reactor granule of modified polymer having a molecular weight distribution of 2.8 to 3.5 Mw / Mn and a melt flow rate of greater than 3000 gms / 10 min at 230 ° C. Method of formation.제14항에 있어서, 개질된 중합체가 웹을 형성하기 전에 500ppm이하의 과산화물을 반응기 과립에 첨가함으로써 생성되는 것을 특징으로 하는 방법.15. The process of claim 14, wherein the modified polymer is produced by adding up to 500 ppm of peroxide to the reactor granules before forming the web.제14항 또는 제15항에 있어서, 중합체의 배출량이 3PIH를 초과함을 특징으로 하는 방법.16. The method of claim 14 or 15, wherein the polymer has an emission greater than 3PIH.중합체의 분자량 분포가 2.8 내지 2.8Mw/Mn이고, 용융 유속이 230℃에서 800gms/10min를 초과하는 개질된 중합체의 반응기 과립을 용융 취입하는 단계로 이루어지는 , 미세 섬유와 작은 공극 크기 분포를 갖는 부직 웹의 형성방법..Nonwoven web with fine fibers and small pore size distribution, consisting of melt blowing the reactor granules of the modified polymer having a molecular weight distribution of 2.8 to 2.8 Mw / Mn and a melt flow rate of greater than 800 gms / 10 min at 230 ° C. Formation method of ..제17항에 있어서, 개질된 중합체가 웹을 형성하기 전에 500 내지 3000ppm의 과산화물을 첨가함으로써 생성되는 것을 특징으로 하는 방법.18. The method of claim 17, wherein the modified polymer is produced by adding 500-3000 ppm peroxide before forming the web.제17항 또는 제18항에 있어서, 중합체의 배출량이 3PIH를 초과함을 특징으로 하는 방법.19. The method of claim 17 or 18, wherein the amount of polymer released is greater than 3PIH.※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019910009952A1990-06-181991-06-17Non-woven web and method of forming the sameExpired - Fee RelatedKR0158457B1 (en)

Applications Claiming Priority (2)

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US540,0701975-01-10
US54007090A1990-06-181990-06-18

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KR920001014Atrue KR920001014A (en)1992-01-29
KR0158457B1 KR0158457B1 (en)1998-12-01

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EP (1)EP0462574B2 (en)
JP (1)JP2849591B2 (en)
KR (1)KR0158457B1 (en)
AU (1)AU636487B2 (en)
DE (1)DE69109543T3 (en)
ES (1)ES2071865T3 (en)

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JP2849591B2 (en)1999-01-20
EP0462574B2 (en)2001-12-19
EP0462574A1 (en)1991-12-27
AU7704391A (en)1991-12-19
DE69109543T3 (en)2002-08-08
KR0158457B1 (en)1998-12-01
DE69109543T2 (en)1995-09-21
ES2071865T3 (en)1995-07-01
AU636487B2 (en)1993-04-29
EP0462574B1 (en)1995-05-10
JPH07119014A (en)1995-05-09
DE69109543D1 (en)1995-06-14

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