JPH01201582A - Surface-active polyester fibrous structure and production thereof - Google Patents
Surface-active polyester fibrous structure and production thereofInfo
- Publication number
- JPH01201582A JPH01201582A JP63022314A JP2231488A JPH01201582A JP H01201582 A JPH01201582 A JP H01201582A JP 63022314 A JP63022314 A JP 63022314A JP 2231488 A JP2231488 A JP 2231488A JP H01201582 A JPH01201582 A JP H01201582A
- Authority
- JP
- Japan
- Prior art keywords
- graft
- swelling agent
- treatment
- polyester
- monomer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229920000728 polyester Polymers 0.000 title claims abstract description 41
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000000835 fiber Substances 0.000 claims abstract description 44
- 239000000178 monomer Substances 0.000 claims abstract description 33
- 230000008961 swelling Effects 0.000 claims abstract description 28
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 27
- 238000010559 graft polymerization reaction Methods 0.000 claims abstract description 13
- 239000000243 solution Substances 0.000 claims abstract description 13
- 238000005530 etching Methods 0.000 claims abstract description 12
- 239000012670 alkaline solution Substances 0.000 claims abstract description 6
- 229920001519 homopolymer Polymers 0.000 claims abstract description 5
- 238000005406 washing Methods 0.000 claims abstract description 4
- 229920000578 graft copolymer Polymers 0.000 claims description 16
- 208000028659 discharge Diseases 0.000 claims description 14
- 230000005865 ionizing radiation Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 24
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 8
- 238000010894 electron beam technology Methods 0.000 abstract description 6
- 150000001732 carboxylic acid derivatives Chemical class 0.000 abstract description 4
- 238000009832 plasma treatment Methods 0.000 abstract description 3
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 abstract description 2
- 239000012528 membrane Substances 0.000 abstract description 2
- 239000002344 surface layer Substances 0.000 abstract 3
- 150000001408 amides Chemical class 0.000 abstract 1
- 150000008064 anhydrides Chemical class 0.000 abstract 1
- 239000003814 drug Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 229910001868 water Inorganic materials 0.000 description 13
- 239000007789 gas Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 238000007654 immersion Methods 0.000 description 9
- 239000007864 aqueous solution Substances 0.000 description 8
- 210000003491 skin Anatomy 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 7
- 229920000642 polymer Polymers 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 6
- 238000009987 spinning Methods 0.000 description 6
- 208000012886 Vertigo Diseases 0.000 description 5
- 125000000524 functional group Chemical group 0.000 description 5
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000005904 alkaline hydrolysis reaction Methods 0.000 description 4
- 238000007385 chemical modification Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 230000009477 glass transition Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 3
- 229920000742 Cotton Polymers 0.000 description 3
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 3
- 125000004429 atom Chemical group 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 239000000975 dye Substances 0.000 description 3
- 210000002615 epidermis Anatomy 0.000 description 3
- 238000001125 extrusion Methods 0.000 description 3
- 239000000314 lubricant Substances 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- 230000004580 weight loss Effects 0.000 description 3
- -1 1.1-dichloroethane Chemical compound 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 150000001244 carboxylic acid anhydrides Chemical class 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000009998 heat setting Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- UKDOTCFNLHHKOF-FGRDZWBJSA-N (z)-1-chloroprop-1-ene;(z)-1,2-dichloroethene Chemical group C\C=C/Cl.Cl\C=C/Cl UKDOTCFNLHHKOF-FGRDZWBJSA-N 0.000 description 1
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- RELMFMZEBKVZJC-UHFFFAOYSA-N 1,2,3-trichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1Cl RELMFMZEBKVZJC-UHFFFAOYSA-N 0.000 description 1
- OCJBOOLMMGQPQU-UHFFFAOYSA-N 1,4-dichlorobenzene Chemical compound ClC1=CC=C(Cl)C=C1 OCJBOOLMMGQPQU-UHFFFAOYSA-N 0.000 description 1
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- OFNISBHGPNMTMS-UHFFFAOYSA-N 3-methylideneoxolane-2,5-dione Chemical compound C=C1CC(=O)OC1=O OFNISBHGPNMTMS-UHFFFAOYSA-N 0.000 description 1
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical group C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 description 1
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 229920006266 Vinyl film Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000002473 artificial blood Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000004204 blood vessel Anatomy 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- MVPPADPHJFYWMZ-UHFFFAOYSA-N chlorobenzene Chemical compound ClC1=CC=CC=C1 MVPPADPHJFYWMZ-UHFFFAOYSA-N 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 229910000365 copper sulfate Inorganic materials 0.000 description 1
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 1
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 1
- 238000003869 coulometry Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 229940117389 dichlorobenzene Drugs 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 229910001872 inorganic gas Inorganic materials 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012567 medical material Substances 0.000 description 1
- 238000002074 melt spinning Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- PYWVYCXTNDRMGF-UHFFFAOYSA-N rhodamine B Chemical compound [Cl-].C=12C=CC(=[N+](CC)CC)C=C2OC2=CC(N(CC)CC)=CC=C2C=1C1=CC=CC=C1C(O)=O PYWVYCXTNDRMGF-UHFFFAOYSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 230000035936 sexual power Effects 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- 235000011008 sodium phosphates Nutrition 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Landscapes
- Chemical Or Physical Treatment Of Fibers (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、ポリエステル系繊維構造物およびその製造方
法に関し、特に表面活性ポリエステル系繊維構造物およ
びその製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a polyester fiber structure and a method for producing the same, and particularly to a surface-active polyester fiber structure and a method for producing the same.
(従来の技術)
ポリエステル系繊維は、今日衣料用素材並びに産業用素
材等として全盛を誇っている。また医療用素材、例えば
人口血管といった特殊な分野にも適ご性があることが判
ってきている。この理由は、階れた機械的性質並びに化
学的性質を有しているからである6反面、親水性が乏し
い為、吸湿性、吸水性がなく、帯電しゃすい、汚れやす
い等の欠点があり、これを改善しようとする研究がポリ
エステル系繊維の発明以来続けられている。(Prior Art) Polyester fibers are now at their peak as materials for clothing, industrial materials, and the like. It has also been found that they are suitable for special fields such as medical materials, such as artificial blood vessels. The reason for this is that it has superior mechanical and chemical properties6, but on the other hand, it has poor hydrophilicity, so it has disadvantages such as lack of hygroscopicity and water absorption, and being easily charged and dirty. Research to improve this problem has continued since the invention of polyester fibers.
n1水性が乏しい理由は、ポリエステル高分子をti4
成する分子構造が高結晶のために水の浸入を阻止してい
ること及び官能基が無いために水を吸着させないことに
よるとされている。The reason for the poor n1 aqueous property is that the polyester polymer is
This is said to be due to the highly crystalline molecular structure that prevents water from entering, and the lack of functional groups that prevents water from being adsorbed.
これらの欠点を改良する為に、従来、次の各方法がとら
れてきた。In order to improve these drawbacks, the following methods have been used in the past.
(1) 高結晶性を乱す第二、第三の高分子成分を配
合したり、官能基を有する成分を添加したりすることが
紡糸の段階においてなされている。(1) Blending second and third polymer components that disrupt high crystallinity or adding components having functional groups is done at the spinning stage.
(2)これと全く原理を異にするが、繊維表面に凹凸を
付与したり、繊維に連続した穴を付り、したりして水の
吸着浸入を容易にすること等も紡糸の段階とその後の染
色加工等の組合せ等でなされている。(2) Although the principle is completely different from this, it is also possible to make it easier for water to absorb and enter at the spinning stage by adding irregularities to the fiber surface or making continuous holes in the fiber. This is done through a combination of subsequent dyeing processes, etc.
(3)紡糸段階以後の処理手段として、官能基を持った
モノマーをグラフト重合せしめて親水化しようとする事
も出来る。(3) As a treatment after the spinning step, it is also possible to graft polymerize a monomer having a functional group to make it hydrophilic.
(4)界面活性剤をベースとする親水化剤や、樹脂成分
をベースとする親水化剤の付与することもできる。(4) A hydrophilic agent based on a surfactant or a hydrophilic agent based on a resin component can also be applied.
(発明が解決しようとする課題)
しかし、(1)(2)の方法は紡糸の段階に施される手
段であり、小廻りのきく手段とは云い難い。(Problems to be Solved by the Invention) However, the methods (1) and (2) are methods applied at the spinning stage, and cannot be said to be flexible means.
又、(3)の方法においては、通常のグラフト法のみで
はグラフト重合型がある1以上にならなければ親水性能
が発揮できない、この場合ポリエステル本来の機械的性
質の低下は余儀なくされる。In addition, in method (3), hydrophilicity cannot be exhibited only by the usual grafting method unless the graft polymerization type is 1 or more, and in this case, the inherent mechanical properties of the polyester are inevitably degraded.
さらに、(4)の方法は耐久性の点で不合理であること
は云うまでもない。Furthermore, it goes without saying that method (4) is unreasonable in terms of durability.
従って、本発明は、上記課題を解消し、本来のポリエス
テルの性質を変化させずして耐久性に富む親水性、帯電
防止性能等を有するポリエステル繊維を紡糸手段以外で
作り出す方法及びこの方法によって製造された繊維構造
物を提−供することを00勺とする。Therefore, the present invention solves the above-mentioned problems, and provides a method for producing polyester fibers that are durable, have hydrophilic properties, antistatic properties, etc. without changing the original properties of polyester, and that can be manufactured by this method. Our aim is to provide a fiber structure made of fibers.
(課題を解決するための手段)
上記課題を解決するために、本発明においては、ポリエ
ステル系繊維を膨潤剤処理後のモノマー溶液又は膨潤剤
共存下のモノマー溶液に浸漬し、電離性放射線を照射し
てグラフト重合反応を施し、次いで弱アルカリ溶液洗浄
によって表面ホモポリマーを除去し、低温プラズマ放電
処理にてエツチングをなしてグラフト重合を高度に露出
せしめ、同時に化学修飾された凹凸を造成せしめること
によって表面活性ポリエステル系繊維構造物ITA造す
るようになされている。(Means for Solving the Problems) In order to solve the above problems, in the present invention, polyester fibers are immersed in a monomer solution treated with a swelling agent or in a monomer solution in the coexistence of a swelling agent, and then irradiated with ionizing radiation. Then, the surface homopolymer is removed by washing with a weak alkaline solution, etching is performed by low-temperature plasma discharge treatment to highly expose the graft polymerization, and at the same time, chemically modified irregularities are created. A surface active polyester fiber structure ITA is made.
(作用)
本発明におけるポリエステル系UN tltとは主たる
構成単位がエチレンテレフタレートであるポリマーから
なる繊維をいい、艶消剤、変色防止剤、色素等必要なら
ば加えてもよい。(Function) The polyester-based UN tlt in the present invention refers to a fiber made of a polymer whose main structural unit is ethylene terephthalate, and a matting agent, anti-discoloration agent, dye, etc. may be added if necessary.
また、本発明でいう繊維構造物とは、ポリエステル系繊
維素材でありさえすればよく、その形態に制約を受けな
い。例えば、モノフィラメント、トウ、ステーブル、ワ
タ、糸、布帛(&i l!物、不織布)などがあげられ
る。均一なる処理効果を本発明に求めるならば、モノフ
ィラメ〉′1・、ステーブル、ワタの様に、構成する単
糸が分離した状態時にほどこすことが、最も有効的であ
る。糸状あるいは織物、編物状に至ると単糸が隼きされ
、さらにこれらが交叉した状態になって均一性の低下が
まぬがれない。一般にポリエステル系繊維は熔融紡糸法
で得られるが、紡糸工程はノズルからの押出し固化、延
伸、加熱熱セットの3過程を経るが、本発明の処理は何
れの段階の後においてもなすことが出来る0本発明の処
理は、グラフ1−重合処理とプラズマ処理の両者より構
成されるが、前者が必ず先行しなければならない。Moreover, the fiber structure as used in the present invention only needs to be a polyester fiber material, and its form is not restricted. Examples include monofilament, tow, stable, cotton, yarn, fabric (&i l! material, non-woven fabric), and the like. If a uniform treatment effect is desired in the present invention, it is most effective to perform the treatment when the constituent single yarns are separated, such as monofilament, stable, and cotton. When it becomes thread-like, woven, or knitted, the single threads become thinner, and furthermore, these threads intersect, resulting in a loss of uniformity. Generally, polyester fibers are obtained by melt spinning, and the spinning process involves three steps: extrusion from a nozzle, solidification, stretching, and heating and heat setting, but the treatment of the present invention can be performed after any step. 0 The treatment of the present invention consists of both graph 1 - polymerization treatment and plasma treatment, but the former must always take precedence.
まず、グラフト重合処理に就いて説明する。グラフト重
合とは「接木」という意味であり、主幹にない性質を枝
の部分に接木で補なおうとするものである。今回の場合
、ポリエステル繊維が主幹であり、モノマーより生じた
重合物が枝となる訳である。「接木」が意味する様に、
主幹と技は結合した一体fヒ物である。このように主幹
にない性で1を接木で補なうことは紡糸手段以外の方法
として有用である。First, the graft polymerization treatment will be explained. Graft polymerization means ``grafting'' and is an attempt to supplement the properties that the main stem lacks by grafting onto the branches. In this case, the polyester fiber is the main fiber, and the branches are polymers produced from monomers. As "grafting" means,
The master and technique are combined into one body. In this way, supplementing 1 by grafting which is not present in the main stem is useful as a method other than spinning.
さて、ポリエステルill Inはガラス転移温度を5
0°C〜80°Cの範囲内に有している。グラフト重合
を容易に且つ効率的に実施するにはこのガラス転移温度
以上の温度領域で成すことが良い、ただfitにグラフ
ト重合せしめる温度を当該温度領域内に設定する場合も
あるが、ポリエステルを膨潤せしめる薬品はガラス転移
温度を低下せしめる効果を発揮してさらに低温で実施で
きるメリッI・がある。この低温化はエネルギー消費、
作業のしやすさ等にも有利である。しかしガラス転移温
度以上の温度と膨潤剤の併用はその効果を(n乗的に有
効にすることは云うまでもない。膨潤剤としては、ジク
ロルメタン、1.1−ジクロルエタン、1.2−ジクロ
ルエタン、1.2−ジクロルエチレン、1,1.2−)
−ジクロルエタン、トリクロルエチレン、1.1,1.
2−テトラクロルエタン、1.1,2.2−テトラクロ
ルエタン、1.1.2.2−テトラクロルエタン、モノ
クロルベンゼン、ジクロルベンゼン、トリクロルベンゼ
ン等の塩素化炭化水素が好ましい。モノマーとしては、
不飽和カルボン酸、不飽和カルボン酸無水物もしくは不
飽和カルボン酸アミド類のいずれかを成分として用いね
ばならない。例えば、アクリル酸、メタクリル酸、マレ
イン酸、フマール酸、イタコン酸の様な不飽和カルボン
酸、無水マレイン酸、無水イタコン酸の様な不飽和カル
ボン酸無水物、アクリルアミド、メタクリルアミドの様
な不飽和カルボン酸アミドがあり、これらは単独または
2種以上の併用で用いられる。更にアクリロニトリル、
ビニルピロリドン、ビニルクロライド等と共グラフト重
合してもよい、膨潤剤単独による浸漬処理についで、モ
ノマー単独による浸漬処理を施す方12:とMD5潤剤
とモノマーの混合浴にして浸漬処理する方法との何れで
もその効果は変わらない、膨潤剤は水、界面活性剤等で
希釈して用いる事があるが、膨潤剤百パーセントの浴か
ら処理する事は付’J、′装置や回収の点から有利であ
る。jノ潤剤での処理は浸漬温度と浸漬時間によって膨
潤度を調整する事が出来る。このjfij潤作用は被処
理材であるポリニスデルの結晶構造の状態によって異な
る。ノスルからの押出し固化状態はもっとも結晶構造が
少ない領域しかなくもっとも容易に大なる膨潤を示し、
以下過程を経るに従って結晶構造の多い領域のものとな
り、膨潤む難しくて小さい膨潤となる。本発明に於ては
L5j潤が大きくても決して良い結果につながらない。Now, polyester ill In has a glass transition temperature of 5
It has within the range of 0°C to 80°C. In order to carry out graft polymerization easily and efficiently, it is best to carry out the graft polymerization in a temperature range above this glass transition temperature.However, the temperature at which the graft polymerization is carried out may be set within this temperature range; This chemical has the advantage of lowering the glass transition temperature and can be carried out at lower temperatures. This lower temperature consumes energy,
It is also advantageous in terms of ease of work. However, it goes without saying that the combination of a temperature higher than the glass transition temperature and a swelling agent increases the effect to the nth power. Examples of swelling agents include dichloromethane, 1.1-dichloroethane, 1.2-dichloroethane, 1,2-dichloroethylene, 1,1.2-)
-dichloroethane, trichlorethylene, 1.1,1.
Chlorinated hydrocarbons such as 2-tetrachloroethane, 1.1,2.2-tetrachloroethane, 1.1.2.2-tetrachloroethane, monochlorobenzene, dichlorobenzene, and trichlorobenzene are preferred. As a monomer,
Either an unsaturated carboxylic acid, an unsaturated carboxylic acid anhydride or an unsaturated carboxylic acid amide must be used as a component. For example, unsaturated carboxylic acids such as acrylic acid, methacrylic acid, maleic acid, fumaric acid, itaconic acid, unsaturated carboxylic anhydrides such as maleic anhydride, itaconic anhydride, unsaturated acids such as acrylamide, methacrylamide, etc. There are carboxylic acid amides, and these are used alone or in combination of two or more. Furthermore, acrylonitrile,
A method in which dipping treatment is performed with a swelling agent alone, which may be co-graft polymerized with vinyl pyrrolidone, vinyl chloride, etc., followed by dipping treatment with a monomer alone; and a method in which a dipping treatment is performed in a mixed bath of an MD5 lubricant and a monomer. The effect remains the same no matter what. Swelling agents may be diluted with water, surfactants, etc., but processing from a bath containing 100% swelling agent is not recommended from the standpoint of equipment and recovery. It's advantageous. In the treatment with a lubricant, the degree of swelling can be adjusted by adjusting the immersion temperature and immersion time. This moisturizing effect differs depending on the state of the crystal structure of polynisder, which is the material to be treated. The solidified state extruded from Nosuru has the least amount of crystalline structure and exhibits the greatest swelling most easily.
As the process progresses, it becomes a region with more crystalline structure, and the swelling becomes difficult and small. In the present invention, even if the L5j moisture is large, it does not lead to good results.
グラフト重合物を表皮層に高密度に分布させるためには
、極端に表現すれば、表皮層のみを膨潤させればよい訳
である。しかし、この様な膨潤の調節は不可能に近く、
これに近づく様に膨潤剤並びにその濃度、浸漬温度、浸
漬時間等で調整される。In order to distribute the graft polymer at high density in the epidermal layer, to put it in an extreme way, only the epidermal layer needs to be swollen. However, this kind of swelling control is nearly impossible;
The swelling agent, its concentration, immersion temperature, immersion time, etc. are adjusted so as to approach this value.
膨潤剤での処理は膨潤剤百パーセントの時は0℃〜80
℃の温度範囲で30秒〜180分間の浸漬が成され、次
いで120℃以下の常圧もしくは真空乾燥で膨潤剤の除
去がなされる。これよりも高温を使用すると熱処理効果
によって膨潤部分の減少につながる。When treating with a swelling agent, the temperature is 0°C to 80°C when the swelling agent is 100%.
C. for 30 seconds to 180 minutes, and then the swelling agent is removed by normal pressure or vacuum drying at 120.degree. C. or lower. Using a higher temperature than this will lead to a reduction in the swollen area due to the heat treatment effect.
膨潤剤とモノマーを混合浴にして用いる場合には、その
相溶性を確認しなければならない。完全な相溶性のある
状!ぷで用いないと均一な付与が難かしいからである。When a swelling agent and a monomer are used in a mixed bath, their compatibility must be confirmed. Perfectly compatible state! This is because it is difficult to apply it uniformly unless it is used in a vacuum.
この相溶性が許す限り、水、有機酸等で希釈が可能であ
る。場合によってはホモボリメリゼーションを阻止する
薬品(例えば硫酸銅、塩化銅の様な金属塩)を添加して
もよい。Dilution with water, organic acids, etc. is possible as long as this compatibility allows. In some cases, chemicals that inhibit homovolimerization (for example, metal salts such as copper sulfate and copper chloride) may be added.
この混合浴でのモノマーの濃度は希望するグラフト重合
基によって左右されるが、10〜90容1パーセン1−
内でXPJnされる0本発明に於いてはモノマー浴のみ
からのモノマー付与も可能であるが、本発明に示す様な
特徴ある表皮層に高密度に分布するグラフト重合物を1
yるには、先に示す2つの方法の回れかを用いる事が好
ましい。The concentration of monomer in this mixed bath depends on the desired grafting groups, but ranges from 10 to 90 volumes 1% 1-
In the present invention, it is also possible to apply the monomer only from the monomer bath, but it is possible to apply the monomer only from the monomer bath.
To do this, it is preferable to use one of the two methods shown above.
モノマー浴あるいは膨潤剤とモノマーの混合浴への浸漬
は、均一なモノマー付与をなすべく洛中の溶液を撹拌し
たり、あるいは、被処理物に動揺を与えたりしながら充
分時間をかける。この場合にも浸漬温度と浸漬時間が調
整されることは申すまでしない、ずでに膨潤剤処理がな
されているものはモノマーの浸入が容易でモノマー浴へ
の浸漬は短時間で良い、ここでの適正な温度は10℃〜
80℃を云い、時間は5秒〜30分で設定可能である。Immersion in a monomer bath or a mixed bath of a swelling agent and a monomer takes a sufficient amount of time while stirring the solution in the liquid or agitating the object in order to uniformly apply the monomer. Needless to say, the immersion temperature and immersion time are adjusted in this case as well.Items that have already been treated with a swelling agent allow the monomer to penetrate easily, and immersion in the monomer bath only takes a short time. The appropriate temperature is 10℃~
The temperature is 80°C, and the time can be set from 5 seconds to 30 minutes.
膨潤剤とモノマーの混合浴の浸漬は先の膨潤剤での処理
に準じて行われる。Immersion in the mixed bath of the swelling agent and monomer is carried out in the same manner as the treatment with the swelling agent described above.
この(、uにして処J!Ijされた被処理物は充分モノ
マーを吸収しているが、次の工程である電量性放射線!
(((対中に蒸発散しない様にしなければならない。The treated object has sufficiently absorbed the monomer, but the next step is coulometric radiation!
((It must be ensured that it does not evaporate into the air.
その方法として過剰量の上記処FJ−液を与えるか、照
射反応室を小さくする事等が良い。電離性放射線として
は、工業的に普及している加速器によって得られる電子
線照射が本発明を達成するには必要である。他のエネル
ギー源を用いた場合はエネルギーが不足で本発明の目的
にきったグラフ1−Thは得られない。A good way to do this is to provide an excess amount of the above treatment FJ solution or to make the irradiation reaction chamber smaller. As the ionizing radiation, electron beam irradiation obtained by an industrially widespread accelerator is necessary to achieve the present invention. If another energy source is used, the graph 1-Th suitable for the purpose of the present invention cannot be obtained due to insufficient energy.
照射は窒素ガス雰囲気下で01〜5MeVエネルギーの
電子線(加速器)を用いる事が好ましく、線量率1.0
X10”ラッド/秒〜1.0X10’ラッド/秒が用い
られ、照射線量は0.1〜10メガラツトが好ましい。For irradiation, it is preferable to use an electron beam (accelerator) with an energy of 01 to 5 MeV in a nitrogen gas atmosphere, and the dose rate is 1.0.
X10'' rad/sec to 1.0X10' rad/sec is used, and the irradiation dose is preferably 0.1 to 10 megarats.
照射によって液処理物上にモノマー溶液は完全に固化し
てグラフ1〜反応は完了する。The monomer solution is completely solidified on the liquid treated material by irradiation, and the reaction in graph 1 is completed.
この様なグラフト反応に於いて、ホモボリメリゼーショ
ンの同時進行は避ける事は出来ず、これによる生成物で
あるホモボマーを溶解除去しなければならない。これに
は弱アルカリ溶液が用いられる。アルカリとは水酸化物
MOHの形式をとり、水に溶解する物質と定義できる。In such a grafting reaction, the simultaneous progress of homobolimerization cannot be avoided, and the resulting homobomerization product must be dissolved and removed. A weak alkaline solution is used for this. Alkali can be defined as a substance that takes the form of hydroxide MOH and dissolves in water.
この場合のMはアルカリ金民やアンモニウム塩をさすが
、広義には炭酸ナトリウム、炭酸水素ナトリウム、炭酸
アンモニウム、リン酸ナトリウム等も含まれる。ここで
弱アルカリ溶液は上記のホモポリマーの溶解除去を目的
にしており、この目的が達成される濃度の水溶液であれ
ば特別の限定はない、その−例として炭酸水素ナトリウ
ム水溶液が用いられ、0.1〜1%の水溶液を浴比1:
100〜200にユIIn、40℃〜80℃の温度で1
〜20分の処理分なす事によって終える0次いで100
〜200″Cの雰囲気中で乾燥、場合によっては熱処理
を同時に施す、ここでmMを計測すればグラフト処理前
!fX1tより重量増加が見られ、この増加分がグラフ
ト重合物に相当するものである。この重合物による増加
分をグラフト率として示すが、その率は0.2〜15重
址パ重上パーセントしくは044〜7重証パーセントで
ある。In this case, M refers to alkali metals and ammonium salts, but in a broader sense it also includes sodium carbonate, sodium bicarbonate, ammonium carbonate, sodium phosphate, etc. Here, the purpose of the weakly alkaline solution is to dissolve and remove the above-mentioned homopolymer, and there is no particular limitation as long as the aqueous solution has a concentration that achieves this purpose. .1 to 1% aqueous solution in a bath ratio of 1:
100-200 at a temperature of 40℃-80℃
Finish by doing ~20 minutes of processing 0 then 100
Dry in an atmosphere of ~200"C, and in some cases heat treatment at the same time. If you measure the mm here, you will see an increase in weight compared to before the graft treatment!fX1t, and this increase corresponds to the graft polymer. The increase due to this polymer is shown as the grafting rate, which is 0.2 to 15 percent or 0.44 to 7 percent.
この様にして得られたポリエステルへのグラフト重合物
はポリエステル表面には顔を出しておらず、表皮層と云
われる外皮より少し内部に最も高密度でそして中心部に
向かって徐々に低密度なる様に分布している事がアルカ
リ加水分解法と呈色法の組合わせで確認する事が出来る
。The graft polymer to polyester obtained in this way does not appear on the surface of the polyester, but has the highest density slightly inside the outer skin, called the skin layer, and gradually becomes less dense toward the center. The similar distribution can be confirmed by a combination of alkaline hydrolysis method and coloring method.
これらを詳しく説明すれば次の様になる。A detailed explanation of these is as follows.
ポリエステル繊維を繊維軸に直角に切断すると断面が現
れる。この断面は円形もしくは特定の形をしている。説
明を解り易くするために断面を円形と仮定する。この断
面の外周すなわち外皮は外気と触れている所であり、膨
潤剤処理あるいはモノマー処理でもっとも先に接触する
所である。これに対し断面の中心部はこれよりもっとも
遠い部分であり、これらに接触するのがもっとも遅い所
である。これよりモノマーが吸着し、それらのグラフト
重合が起こる確率は、断面の中心を中心とする断面上の
同心円ではほぼ等しいとみなす事が出来る。ポリエステ
ル繊維はアルカリ加水分解によって外皮が均一に溶解さ
れる特異な性質を有しており、原形を保ちながら細くす
る事が容易に出来る。一方、グラフト重合物中には官能
基として持ち込まれたーC0OHが存在している。これ
はアニオン基でありカチオン性色素と定置的に結合する
反応を利用し、グラフト重合物の存在とその燵をall
l定する事が出来る。カチオン性色素による測定を具体
的に示せば、カラーインデックスナンバー、ベーシック
バイオレット10を1重量%と+’il二酸(80%)
を0 、5 cc / Lを含む浴で浴比1:200.
90℃で20分呈色後、酢酸(80%)0.5σ/L水
溶液にて60℃×10分の洗滌を2回bi’JAし、次
いで水洗して乾燥をなす、もし、このポリエステルがバ
イオレット色に呈色すればグラフト重合物の存在を示し
、分光光度計で濃度を測定し、グラフト率との相関関係
よりグラフト重合物の)Lを推定する事が出来る6本発
明の実施例に示すデーターに基づくとポリエステル繊!
、1にの繊維軸と平行に繊維の中心を通る用にカツトシ
た面でその分布を示すと殆んど0字型からV字型に近い
事が[認されている。When a polyester fiber is cut perpendicular to the fiber axis, a cross section appears. This cross section may be circular or have a specific shape. To make the explanation easier to understand, assume that the cross section is circular. The outer periphery of this cross section, that is, the outer skin, is the part that is in contact with the outside air, and is the part that comes into contact first during swelling agent treatment or monomer treatment. On the other hand, the center of the cross section is the part farthest from this, and the part that comes into contact with them is the slowest. From this, the probability that monomers will be adsorbed and their graft polymerization will occur can be considered to be approximately equal in concentric circles on the cross section centered on the center of the cross section. Polyester fibers have the unique property that their outer skin is uniformly dissolved by alkaline hydrolysis, and can be easily made thin while maintaining their original shape. On the other hand, in the graft polymer, -C0OH is present as a functional group. This is an anionic group, which utilizes the reaction of stationary bonding with a cationic dye to detect the presence of a graft polymer and its effect on all
It is possible to determine Specifically, measurements using cationic dyes include color index number, 1% by weight of basic violet 10 and +'il diacid (80%).
in a bath containing 0.5 cc/L at a bath ratio of 1:200.
After coloring at 90°C for 20 minutes, wash twice at 60°C for 10 minutes with an acetic acid (80%) 0.5σ/L aqueous solution, then wash with water and dry. If it develops a violet color, it indicates the presence of a graft polymer, and the concentration can be measured with a spectrophotometer, and the L of the graft polymer can be estimated from the correlation with the grafting rate.6 Examples of the present invention Based on the data shown, polyester fiber!
It has been recognized that when the distribution is shown in a plane cut to pass through the center of the fiber parallel to the fiber axis of 1, it is almost 0-shaped to V-shaped.
次に低温プラズマ放電処理について説明する。Next, low temperature plasma discharge treatment will be explained.
低温プラズマとは、低圧下において気体に強い電場をか
けて放電を起こさせるものである。ここで、気体として
空気、−酸化炭素、二酸化炭素、酸素、窒素、水素、ア
ルゴン、ヘリウム等の無機ガス群が用いられる。中でも
空気、酸素、アルゴンの3種類がよく用いられる。放電
処理はこの放電された場に被処理物を置くことによって
なされる。これによって表面に凹凸が造成されるくこれ
をエツチングという)、この凹凸の大きさ、深さは用い
られる気体によって差が生ずる事は知られている。Low-temperature plasma is one in which a strong electric field is applied to a gas under low pressure to cause a discharge. Here, inorganic gases such as air, carbon oxide, carbon dioxide, oxygen, nitrogen, hydrogen, argon, and helium are used as the gas. Among these, three types are often used: air, oxygen, and argon. Discharge treatment is performed by placing the object to be treated in this discharged field. This creates irregularities on the surface (this is called etching), and it is known that the size and depth of these irregularities vary depending on the gas used.
低温プラズマ放電処理による凹凸の大きさは微小である
。この凹凸の大きさ、深さの表示方法は次の様にする事
にする。すなわち凹部から次に隣接する凹部の最低点ま
で平均的平面距離、もしくは凸部から次に隣接する凸部
の最高点までの平均的平面距離と、凸部の最高点と四部
の最低点間の平均的距雛すなわち深さとの両者で表示す
る。そして、この凹凸がどれだけ存在するかを表示する
為に単位面積当りにある個数ずなわち、密度で表示する
。本発明ではこの凹凸の大きさ、深さは直接重要要素で
ないが、結果的に得られる数値であるので記するが、こ
れらはSEMから得られる写真からカウントされる。The size of the unevenness caused by the low-temperature plasma discharge treatment is minute. The method of displaying the size and depth of this unevenness is as follows. In other words, the average plane distance from a concave part to the lowest point of the next adjacent concave part, or the average plane distance from a convex part to the highest point of the next adjacent convex part, and the distance between the highest point of the convex part and the lowest point of the four parts. Both the average distance and depth are displayed. In order to indicate how many unevennesses exist, the number of unevennesses per unit area, that is, the density, is displayed. In the present invention, the size and depth of the unevenness are not directly important factors, but are described because they are numerical values obtained as a result, and these are counted from the photograph obtained from the SEM.
この凹凸の造成の外に、表面において化学豹変1ヒも同
11冒こ進行する事も知られている(これを化′;セ修
飾という)、これは用いる気体の原子と被処理物の原子
の新しい反応が、その表面上でプラズマ放電処理下で行
われる説と、プラズマ放電処理後空気中に取り出した時
、活性ラジカルと空気中の酸素、二酸化炭素、水等との
反応が行われる説とがいわれているが、本発明の場合に
は確かな証明がなされていない、ともかく、これらの生
成物が官能基の一部分の様に働き、水分子の吸着を促が
ず親水性向上や接着性向上等につながる。これを化学修
飾効果と称することにする。In addition to the formation of this unevenness, it is also known that chemical changes occur on the surface (this is called chemical modification), which is caused by the atoms of the gas used and the atoms of the material to be treated. One theory is that a new reaction takes place on the surface under plasma discharge treatment, and the other theory that when taken out into the air after plasma discharge treatment, reactions occur between active radicals and oxygen, carbon dioxide, water, etc. in the air. However, in the case of the present invention, no reliable proof has been made.In any case, these products act like part of the functional group and do not promote the adsorption of water molecules, but improve hydrophilicity and adhesion. This leads to improved sexual performance, etc. This will be referred to as a chemical modification effect.
本発明の低温プラズマ放電処理をする条件は、周波数と
して100KH,〜10MH,あルイハ10Ml−1,
〜100MH,で好ましくは110に11.の低周波放
電プラズマ、13.56MI(□の高周波放電プラズマ
が良い、そして出力10W〜100KW、圧力2トール
以下、ガス流量10〜300 ml/ +ainで処理
時間5秒〜1800秒である。圧力は低圧側はど気体原
子の運動量を高めるから効果的であるが、ガス流量を高
める・と必然的に圧力が高圧側になる為、一定ガス流量
以上になると圧力を希望する低圧にすることか出来なく
なる。具体的に示せば、0.051・−ル下ではガス流
M 20 mf/ff1in以下、0.1トール下では
同じく20〜100+aIl/sin、0.2トール下
では40〜200mA’/+ninという具合である。The conditions for the low temperature plasma discharge treatment of the present invention are as follows: frequency: 100KH, ~10MH;
~100MH, preferably 110 to 11. A low frequency discharge plasma of 13.56 MI (□) is good, and the output is 10 W to 100 KW, the pressure is 2 torr or less, the gas flow rate is 10 to 300 ml/+ain, and the processing time is 5 seconds to 1800 seconds.The pressure is The low pressure side is effective because it increases the momentum of the gas atoms, but if you increase the gas flow rate, the pressure will inevitably become high pressure side, so if the gas flow rate exceeds a certain level, it will not be possible to make the pressure the desired low pressure. Specifically, under 0.051 Torr, the gas flow M is less than 20 mf/ff1in, under 0.1 Torr, it is 20 to 100+al/sin, and under 0.2 Torr, it is 40 to 200 mA'/+nin. That's how it is.
ポリエステル繊維は、先述のように高結晶性高分子に属
し、エツチングがされにくい。然しながら、化学的変化
(化学修飾)を付与することが出来る。これが低温プラ
ズマ放電処理の特徴である。As mentioned above, polyester fibers belong to highly crystalline polymers and are not easily etched. However, chemical changes (chemical modifications) can be applied. This is a feature of low-temperature plasma discharge treatment.
本発明ではエツチングすることを主眼においており、化
学的変化(化学修飾)は副効果として必然的に付与され
るものと解釈している。今、周波数として13.56M
H,を設定し、出力、圧力、ガス流量等を変化せしめる
と、当然最適条件を見出す事が出来る。この中で重要視
されるのは出力である。エツチング効果を出すには10
0W以上、好ましくは300W以上が必要で、これ以下
では凹凸の造成が生じないか、生じても長時間をかけざ
るを得ないであろう。The present invention focuses on etching, and it is interpreted that chemical changes (chemical modification) are inevitably imparted as a side effect. Now the frequency is 13.56M
By setting H, and changing output, pressure, gas flow rate, etc., the optimum conditions can naturally be found. Among these, the output is important. 10 ways to get the etching effect
0W or more, preferably 300W or more is required; if it is less than this, unevenness will not be created, or even if it does occur, it will take a long time.
と亡ろでポリエステル繊維はノズルからの流動押出し固
1ヒ、延伸、加熱熱セットの過程を経て得られる。この
過程後、撚をがけたり、バルキー性を与えたりする処理
が付加される。こうして得られる繊mは後になる程熱処
理を受ける機会が増え、繊t、+iの性質が少しずつ変
化する。ノズルからの流動押出し固化状態では、繊維状
を形成したばかりの段1り・!であり、結晶性も低比率
で加工しやすい。Finally, polyester fibers are obtained through the processes of fluid extrusion from a nozzle, stretching, and heat setting. After this process, processes such as twisting and adding bulkiness are added. The fiber m obtained in this way has more chances to undergo heat treatment later on, and the properties of the fibers t and +i gradually change. In the solidified state of fluid extrusion from the nozzle, the first stage that has just formed a fibrous form is... It has a low crystallinity ratio and is easy to process.
しかし、延伸することによって一気に結晶性は増大し、
一般ポリエスデル繊維性能を発揮することは公知である
。この様な事実より低温プラズマ放′、1.処理は加工
しやすい状態でする事が得策である。However, by stretching, the crystallinity increases at once,
It is known that polyester fiber exhibits general polyester fiber performance. Based on these facts, low-temperature plasma radiation, 1. It is a good idea to process the material in a state that is easy to process.
このZ、k 、目的に応じたポリエステル繊維を作る事
ら本発明では重要視される。ポリエステルの化学11!
J 1.Y性念利用目的にする時、必ずしも機械的特性
も同時にj1加する必要はない訳である。In the present invention, emphasis is placed on the production of polyester fibers tailored to the purpose of Z and k. Chemistry of polyester 11!
J1. When making use of Y sexual thoughts, it is not necessarily necessary to add mechanical properties to j1 at the same time.
(実施例) 次に実施例を示す。(Example) Next, examples will be shown.
見掛ヤング率120kg/mm2で径40ミクロン(強
度100g、伸度40%)のポリエステルモノフィラメ
ントを約2グラム用意し、非イオン界面活性剤を含む温
湯中でよく洗滌し、水洗乾燥して重量測定した。このヤ
ング率の6aはポリエステル繊維一般に云われる1 1
00 kg / +n+n2に比較して非常に小さいも
のである。Approximately 2 grams of polyester monofilament with an apparent Young's modulus of 120 kg/mm2 and a diameter of 40 microns (strength 100 g, elongation 40%) was prepared, thoroughly washed in hot water containing a nonionic surfactant, washed with water, dried, and weighed. did. This Young's modulus of 6a is generally said to be 1 1 for polyester fibers.
00 kg/+n+n2.
以下、次の処理をなした。Below, the following processing was performed.
(1) 膨潤剤百パーセンI・浴処理1.2−ジクロ
ロエタン(市販試薬−級)を20℃、40℃に設定し、
この中に先の被処理物を1時間撹拌しながら浸漬する。(1) Swelling agent 100% I bath treatment 1.2-dichloroethane (commercial reagent grade) was set at 20°C and 40°C,
The object to be treated is immersed in this solution for 1 hour while stirring.
次いで取出し室温で一昼夜放置し、表面に付着するジク
ロルメタンを取除き、さらに80℃×600分の乾燥処
理し、繊維内部に吸着した1、2−ジクロロエタンを取
除く。各々の試料をA群試料、B群試料とする。The fibers are then taken out and left at room temperature for a day and night to remove dichloromethane adhering to the surface, and are further dried at 80° C. for 600 minutes to remove 1,2-dichloroethane adsorbed inside the fibers. Let each sample be a group A sample and a group B sample.
(II) モノマー浴処理
(+)で得られたA、B群試料をメタクリル酸(市販試
薬)40℃に設定し、この中で浸漬撹拌を1時間なした
。(II) Samples of groups A and B obtained by monomer bath treatment (+) were immersed and stirred in methacrylic acid (commercially available reagent) at 40° C. for 1 hour.
(III ) 155潤剤/モノマ一混合浴処理容積
比で6=4に配合した1、2−ジクロロエタン(市販二
に薬ンとメタクリル酸(7F7版試薬)の混合液を50
℃に設定し、この中に先の被処理物を2時間t11拝し
ながら浸漬した。これを0群試料とする。(III) A mixed solution of 1,2-dichloroethane (commercially available dichloroethane) and methacrylic acid (7F7 version reagent) blended at a treatment volume ratio of 6=4 in a 155 lubricant/monomer mixture bath was mixed at 50%
℃, and the object to be treated was immersed therein for 2 hours at 11°C. This is designated as the 0 group sample.
(IV) (n)で処理されたA、 Bngil
(Ill)で処理された0群試料とを各々別個にステン
レスパレット上に移す、生地重量に対し5倍の処理液で
浸し、バレットをビニルフィルムで覆い、窒素カスで空
気を置換する。(IV) A treated with (n), Bngil
The 0 group samples treated with (Ill) were each transferred onto a stainless steel pallet, immersed in a treatment solution 5 times the weight of the dough, covered with a vinyl film, and the air replaced with nitrogen gas.
(V) 照射はヴアン・デ・グラーフ電子線照射装置
を用い、1.5MeV、50mA、0.17M rad
/秒で総線旦6Mrad成した。(V) Irradiation was performed using a Van de Graaf electron beam irradiation device, 1.5 MeV, 50 mA, 0.17 M rad.
The total line speed was 6 Mrad per second.
(Vl) 洗)條は炭酸氷水ナトリウム10 ii/
L水溶液で80°C×20分を2回成した。(Vl) Washing) Sodium carbonate ice water 10 ii/
The mixture was heated twice at 80°C for 20 minutes using L aqueous solution.
(■) 熱風乾燥機を用いて100℃×60分の乾燥隣
重量を測定し、グラフト率を各々算出した。(■) The weight of each sample after drying at 100° C. for 60 minutes using a hot air dryer was measured, and the grafting ratio was calculated for each sample.
A 肝; 4 、3 % r3 J+’T ; 4
、7% 0群;465%となった。これらの試料を先に
示したベーシックバイレッI・10水溶液にて呈色させ
たが、極淡い呈色であり、グラフト重合物が表面に存在
す−ると判断しがたい程度のものであった。又、これら
の試料を同じく先に示したアルカリ加水分解処f1(炭
酸ナトリウム10 g/L水溶液、浴比1:20010
0℃x15,30.45.60分)後、これに伴う重量
減少量を測定し、ベーシックバイレット10水溶液によ
る呈色を施した。この呈色で何れの試料もアルカリ加水
分解処理時間15分と30分処理試料で最も濃く呈色し
、グラフト重合物が露出存在すると判断出来た。即ち、
この時の減量率からこの場所が表面から何処にあるか計
算してみると、0.15〜0.2ミクロンだけ表面より
繊維軸中心に向かった同心円状である事が判った。そし
て、この分布状態の模式図は、図−1に示す様である。A Liver; 4, 3% r3 J+'T; 4
, 7% Group 0; 465%. These samples were colored with the above-mentioned Basic Baylet I/10 aqueous solution, but the color was very pale and it was difficult to determine that a graft polymer was present on the surface. Ta. In addition, these samples were subjected to the same alkaline hydrolysis treatment f1 (sodium carbonate 10 g/L aqueous solution, bath ratio 1:20010).
After 15 minutes at 0° C. for 30, 45, and 60 minutes, the amount of weight loss accompanying this was measured and colored with an aqueous solution of Basic Vilet 10. In this coloration, the coloration of all the samples was the darkest in the samples treated with alkaline hydrolysis for 15 minutes and 30 minutes, and it was determined that the graft polymer was exposed and present. That is,
When calculating the location of this location from the surface based on the weight loss rate at this time, it was found that it was a concentric circle extending 0.15 to 0.2 microns from the surface toward the center of the fiber axis. A schematic diagram of this distribution state is shown in Figure 1.
これより本発明において得られたポリエステルグラフト
重合物を外気と接する表面に露出せしめるには、0.1
5〜2ミクロンまで低温プラズマ放電処理にてエツチン
グを施ず必要がある事が判った。これは重fIk減量率
からみると1〜2.5%の数値となる。From this, in order to expose the polyester graft polymer obtained in the present invention on the surface in contact with the outside air, the amount of 0.1
It has been found that it is necessary to perform low-temperature plasma discharge treatment without etching down to 5 to 2 microns. This is a value of 1 to 2.5% in terms of weight loss rate of fIk.
(■) これら試1′4を周波数13.56MI[z、
出カフ00W、圧力0.21−−ル、酸素ガスのガス流
延190 tJ / rainの条件下で2分及び4分
の照射処理を施した。こうして得られた試料は、先述の
ベーシックバイオレフ1〜10水溶液にて呈色させると
明白なグラフl−重合物の露出を示す)♂い呈色反応を
見る事が出来た。(■) These trials 1'4 were set at a frequency of 13.56 MI [z,
Irradiation treatment was performed for 2 minutes and 4 minutes under the conditions of an output cuff of 00W, a pressure of 0.21-L, and an oxygen gas flow rate of 190 tJ/rain. When the sample thus obtained was colored with the aqueous solution of Basic Bioref 1 to 10 described above, a clear color reaction could be seen (graph 1 (indicating exposure of polymer)).
(IX ) 又、これらの試1:lのSEM撮影を繊
維の0111面、先端部に於いてなし、両部に凹凸の造
成を=2めな、その大きさは、0.08〜1.2ミクロ
ンのらのが90%以上でその池に1.8〜3.0ミクロ
ンの巨大なものが10%位カウントされた。深さは0.
06〜1.0ミクロンであった。(IX) In addition, these test 1:1 SEM images were taken on the 0111 side and the tip of the fiber, and unevenness was created on both sides, and the size was 0.08 to 1. More than 90% of the ponds were 2 micron larvae, and around 10% were 1.8 to 3.0 micron giant ones. Depth is 0.
It was 0.06 to 1.0 microns.
(X) これらの試料は、水滴をその表面に落下せし
めてら直ちに拡散すなわち良い濡れ性を示した。iな、
rM擦張帯電圧ロータリースタティックテスター(興亜
商会)にて温度20’C相当湿度40%中で綿布と摩擦
2分後で測定したが各々100V以下であった。(X) These samples showed immediate diffusion or good wetting when a drop of water was allowed to fall on their surface. i,
The rM friction charge voltage was measured with a rotary static tester (Koa Shokai) at a temperature of 20'C and a humidity of 40% after 2 minutes of rubbing against a cotton cloth, and each was 100 V or less.
(訂) 強伸度は未処理に比べて強度は3%の低下、
伸度は4%の向上であった。(edited) The strength and elongation are 3% lower than untreated.
The elongation was improved by 4%.
(発明の効果)
以上の様に実施例にみる結果から本発明の説明文に記す
如く、ポリエステル繊維の表皮層にモノマーを電子線照
射によってグラフト重合せしめ、次いで低温プラズマ放
電処理にて表皮層をエツチング除去するとグラフト重合
された部分を表皮層上に露出せしめ、同時に表面に化学
11す飾された凹凸を造成せしめなる表面活性なユニー
クなポリエステル繊維を作ることが出来る事を知った。(Effects of the Invention) From the results shown in the examples above, as described in the description of the present invention, monomers are graft-polymerized onto the skin layer of polyester fibers by electron beam irradiation, and then the skin layer is formed by low-temperature plasma discharge treatment. I learned that when removed by etching, the graft polymerized portion is exposed on the epidermal layer, and at the same time, it is possible to create a unique surface-active polyester fiber that creates decorated irregularities on the surface.
そして本発明で得られた機械的特性の低下のない本来の
ポリエステル性能を保持し且つその表面に高密度に配置
されたグラフト重合物により親水性を有した上、化学修
飾された微小凹凸が付加されたいわゆる表面活性なポリ
エステル繊維構造物は、医療分野、バイオテクノロジー
分野、フィルター膜素材等に有効に応用可能である。In addition, it retains the original polyester performance without deterioration of mechanical properties obtained by the present invention, has hydrophilicity due to the graft polymer arranged at high density on its surface, and has chemically modified minute irregularities added. The resulting so-called surface-active polyester fiber structure can be effectively applied to the medical field, biotechnology field, filter membrane material, etc.
第11Aは本発明で得られるポリエステル/グラフト共
重合繊t、1構造物中の単糸を取出し、その繊維軸を通
る軸方向にカットした断面上でのグラフト重合物存在模
式図である。
ここで、1〉単糸の中心
2 ) ’it糸の外皮表面
3)グラフト重合物分布層
4)グラフト重合物の最高密度層
5)エツチング除去されるJl
6)エツチング後の新しい外皮表面
である。No. 11A is a schematic diagram of the presence of graft polymers on a cross section taken from a polyester/graft copolymer fiber t obtained in the present invention and cut in the axial direction passing through the fiber axis. Here, 1> Center of single yarn 2) Outer skin surface of 'it yarn 3) Graft polymer distribution layer 4) Highest density layer of graft polymer 5) Jl to be removed by etching 6) New outer skin surface after etching .
Claims (2)
に浸漬するか又は膨潤剤共存下のモノマー溶液に浸漬し
、電離性放射線を照射してグラフト重合反応を施こし、
次いで弱アルカリ溶液洗浄によつて表面ホモポリマーを
除去し、低温プラズマ放電処理にてエッチングをなして
グラフト重合部分を高度に露出せしめ、同時に化学修飾
された凹凸を造成せしめることからなる表面活性ポリエ
ステル/グラフト共重合繊維構造物の製造方法。(1) Polyester fibers are immersed in a monomer solution after treatment with a swelling agent, or immersed in a monomer solution in the presence of a swelling agent, and irradiated with ionizing radiation to perform a graft polymerization reaction,
Next, the surface homopolymer is removed by washing with a weak alkaline solution, and the graft polymerized portion is exposed to a high degree by etching by low-temperature plasma discharge treatment, and at the same time, chemically modified irregularities are created. A method for producing a graft copolymer fiber structure.
に浸漬するか又は膨潤剤共存下のモノマー溶液に浸漬し
、電離性放射線を照射してグラフト重合反応を施し、次
いで弱アルカリ溶液洗浄によつて表面ホモポリマーを除
去し、低温プラズマ放電処理にてエッチングをなしてグ
ラフト重合を高度に露出せしめ、同時に化学修飾された
凹凸を造成せしめることによつて形成された表面活性ポ
リエステル系繊維構造物。(2) Polyester fibers are immersed in a monomer solution after treatment with a swelling agent, or immersed in a monomer solution in the presence of a swelling agent, irradiated with ionizing radiation to perform a graft polymerization reaction, and then washed with a weak alkaline solution. A surface-active polyester fiber structure formed by removing the surface homopolymer, etching with low-temperature plasma discharge treatment to highly expose graft polymerization, and at the same time creating chemically modified irregularities.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63022314A JPH01201582A (en) | 1988-02-02 | 1988-02-02 | Surface-active polyester fibrous structure and production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63022314A JPH01201582A (en) | 1988-02-02 | 1988-02-02 | Surface-active polyester fibrous structure and production thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01201582A true JPH01201582A (en) | 1989-08-14 |
JPH048541B2 JPH048541B2 (en) | 1992-02-17 |
Family
ID=12079270
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63022314A Granted JPH01201582A (en) | 1988-02-02 | 1988-02-02 | Surface-active polyester fibrous structure and production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01201582A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2022553468A (en) * | 2019-10-24 | 2022-12-23 | サーティ・エッセ・ピ・ア | Method for making composite filter material and composite filter material obtained by this method |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS496294A (en) * | 1972-05-24 | 1974-01-19 | ||
JPS4913497A (en) * | 1972-05-22 | 1974-02-05 | ||
JPS60173170A (en) * | 1984-02-16 | 1985-09-06 | ユニチカ株式会社 | Modification of polyester fiber |
JPS60185864A (en) * | 1984-03-02 | 1985-09-21 | 住友化学工業株式会社 | Treatment of fiber |
-
1988
- 1988-02-02 JP JP63022314A patent/JPH01201582A/en active Granted
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4913497A (en) * | 1972-05-22 | 1974-02-05 | ||
JPS496294A (en) * | 1972-05-24 | 1974-01-19 | ||
JPS60173170A (en) * | 1984-02-16 | 1985-09-06 | ユニチカ株式会社 | Modification of polyester fiber |
JPS60185864A (en) * | 1984-03-02 | 1985-09-21 | 住友化学工業株式会社 | Treatment of fiber |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2022553468A (en) * | 2019-10-24 | 2022-12-23 | サーティ・エッセ・ピ・ア | Method for making composite filter material and composite filter material obtained by this method |
Also Published As
Publication number | Publication date |
---|---|
JPH048541B2 (en) | 1992-02-17 |
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