JPH0473217A - Highly shrinkable polyester fiber - Google Patents
Highly shrinkable polyester fiberInfo
- Publication number
- JPH0473217A JPH0473217A JP18610190A JP18610190A JPH0473217A JP H0473217 A JPH0473217 A JP H0473217A JP 18610190 A JP18610190 A JP 18610190A JP 18610190 A JP18610190 A JP 18610190A JP H0473217 A JPH0473217 A JP H0473217A
- Authority
- JP
- Japan
- Prior art keywords
- sheath
- core
- mol
- polyester
- fiber
- 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.)
- Pending
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 34
- 229920000728 polyester Polymers 0.000 title claims abstract description 26
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 13
- -1 polyethylene terephthalate Polymers 0.000 claims abstract description 6
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 6
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 6
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000000470 constituent Substances 0.000 claims abstract description 4
- 239000002131 composite material Substances 0.000 claims description 15
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 6
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical compound C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 230000004520 agglutination Effects 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract description 2
- 230000021615 conjugation Effects 0.000 abstract 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract 1
- 239000005977 Ethylene Substances 0.000 abstract 1
- ORLQHILJRHBSAY-UHFFFAOYSA-N [1-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1(CO)CCCCC1 ORLQHILJRHBSAY-UHFFFAOYSA-N 0.000 abstract 1
- 230000007547 defect Effects 0.000 abstract 1
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 12
- 238000007334 copolymerization reaction Methods 0.000 description 10
- YIMQCDZDWXUDCA-UHFFFAOYSA-N [4-(hydroxymethyl)cyclohexyl]methanol Chemical compound OCC1CCC(CO)CC1 YIMQCDZDWXUDCA-UHFFFAOYSA-N 0.000 description 9
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 9
- 229920000642 polymer Polymers 0.000 description 7
- 238000000034 method Methods 0.000 description 5
- 238000009987 spinning Methods 0.000 description 5
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 3
- ADCOVFLJGNWWNZ-UHFFFAOYSA-N antimony trioxide Chemical compound O=[Sb]O[Sb]=O ADCOVFLJGNWWNZ-UHFFFAOYSA-N 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 150000001991 dicarboxylic acids Chemical class 0.000 description 2
- 150000002009 diols Chemical class 0.000 description 2
- VVTXSHLLIKXMPY-UHFFFAOYSA-L disodium;2-sulfobenzene-1,3-dicarboxylate Chemical compound [Na+].[Na+].OS(=O)(=O)C1=C(C([O-])=O)C=CC=C1C([O-])=O VVTXSHLLIKXMPY-UHFFFAOYSA-L 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 2
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 2
- MMINFSMURORWKH-UHFFFAOYSA-N 3,6-dioxabicyclo[6.2.2]dodeca-1(10),8,11-triene-2,7-dione Chemical group O=C1OCCOC(=O)C2=CC=C1C=C2 MMINFSMURORWKH-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- VSGNNIFQASZAOI-UHFFFAOYSA-L calcium acetate Chemical compound [Ca+2].CC([O-])=O.CC([O-])=O VSGNNIFQASZAOI-UHFFFAOYSA-L 0.000 description 1
- 229960005147 calcium acetate Drugs 0.000 description 1
- 235000011092 calcium acetate Nutrition 0.000 description 1
- 239000001639 calcium acetate Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- QQVIHTHCMHWDBS-UHFFFAOYSA-L isophthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC(C([O-])=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-L 0.000 description 1
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 1
- SLCVBVWXLSEKPL-UHFFFAOYSA-N neopentyl glycol Chemical compound OCC(C)(C)CO SLCVBVWXLSEKPL-UHFFFAOYSA-N 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 238000007665 sagging Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Multicomponent Fibers (AREA)
Abstract
Description
【発明の詳細な説明】 (発明の利用分野) 本発明は高収縮性ポリエステル系繊維に関する。[Detailed description of the invention] (Field of application of the invention) The present invention relates to highly shrinkable polyester fibers.
詳しくは、他の糸と混繊し、熱水処理した場合に、嵩高
性が極めて大きい混繊糸とし得、且つ、融着膠着のない
超高収縮性ポリエステル系繊維に関する。Specifically, the present invention relates to an ultra-high shrinkage polyester fiber that can be mixed with other yarns and treated with hot water to form a mixed yarn with extremely high bulkiness, and which is free from fusing and sticking.
(従来技術)
ポリエステル繊維を用いた織編物の風合、特に嵩高性を
向上させる目的で、異収縮混繊糸とする手法が一般に用
いられている。これは、収縮性の大きい繊維と収縮性の
小さい繊維を混繊して得られる。収縮性の小さいポリエ
ステル系繊維を得る方法は高温熱セントして結晶化させ
る及び/又は延伸後に弛緩熱処理する方法であり、収縮
性の大きい繊維を得るには、延伸時に熱セットしない及
び/又はポリエチレンテレフタレートに別種の酸成分又
はグリコール成分を共重合したポリエステル系ポリマー
の繊維とする方法がある。これら2つの方法を組合せる
と嵩高性混繊糸とすることが出来、例えば特開昭63−
126934号が挙げられる。(Prior Art) For the purpose of improving the feel, especially the bulkiness, of woven or knitted fabrics using polyester fibers, a method of using different shrinkage mixed fiber yarns is generally used. This is obtained by mixing fibers with high shrinkage and fibers with low shrinkage. A method for obtaining polyester fibers with low shrinkage is to perform crystallization using high-temperature heat centrifugation and/or a relaxation heat treatment after drawing.To obtain fibers with large shrinkage, polyester fibers are not heat set during drawing and/or polyester fibers are not heat-set during drawing. There is a method of making fibers of a polyester polymer by copolymerizing terephthalate with another type of acid component or glycol component. By combining these two methods, a bulky mixed fiber yarn can be obtained.
No. 126934 is mentioned.
嵩高性が極めて大きい混繊糸を得ようとするならば、超
高収縮性繊維を用いれば良い、しかしながら、前述の方
法だけでは、衣料用として有効な超高収縮性ポリエステ
ル系繊維は得ることは出来ない、何故ならば、延伸時の
熱セット温度を低くしてもある程度の強度を保持させる
とポリエチレンテレフタレートでは15〜20%程度の
湧水収縮率にしかならない。又、イソフタル酸やジエチ
レングリコール等の第3.第4成分を共重合させたポリ
エチレンテレフタレートは、その共重合比率を上げるに
従い収縮率は大きくなり、70%の湧水収縮率も可能で
ある。しかし共重合比率が上がるに従い、そのポリマー
融点は低下し、熱水中でも膠着して硬くなり、衣料用と
して用をなさないことになる。If you want to obtain a blended yarn with extremely high bulk, you can use ultra-high shrinkage fibers.However, it is not possible to obtain ultra-high shrinkage polyester fibers that are effective for clothing using the above method alone. This is not possible, because even if the heat setting temperature during stretching is lowered, if a certain degree of strength is maintained, polyethylene terephthalate will only have a shrinkage rate of about 15 to 20%. Also, tertiary substances such as isophthalic acid and diethylene glycol. The shrinkage rate of polyethylene terephthalate copolymerized with the fourth component increases as the copolymerization ratio increases, and a spring water shrinkage rate of 70% is also possible. However, as the copolymerization ratio increases, the polymer's melting point decreases, and it becomes sticky and hard even in hot water, making it useless for clothing.
(発明が解決しようとする問題点)
本発明は上記欠点を改善し、湧水中に於る収縮率が極め
て高く、且つポリエステルmW物の通常の製造工程での
熱膠着、融着のない、高収縮性ポリエステル系繊維を提
案しようとするものである。(Problems to be Solved by the Invention) The present invention improves the above-mentioned drawbacks, and has a highly shrinkage rate in spring water that is extremely high and does not undergo thermal agglutination or fusion in the normal manufacturing process of polyester mW products. This paper attempts to propose a shrinkable polyester fiber.
(問題点を解決するための手段)
本発明の高収縮性ポリエステル繊維は、芯鞘型のポリエ
ステル系複合繊維であって、単糸横断面に於る芯部はグ
リコール成分の15〜35モル%がシクロヘキサリンメ
タノール(以下CHDMと略記)で共重合されたポリエ
チレンテレフタレト(以下PETと略記)であり、鞘部
は構成単位の88モル%以上がエチレンテレフタレート
からなるポリエステルであり、芯部と鞘部との複合比が
10=1〜2:1であることを特徴とする。(Means for Solving the Problems) The highly shrinkable polyester fiber of the present invention is a core-sheath type polyester composite fiber, and the core portion in the cross section of the single filament contains 15 to 35 mol% of the glycol component. is polyethylene terephthalate (hereinafter abbreviated as PET) copolymerized with cyclohexaline methanol (hereinafter abbreviated as CHDM), the sheath is a polyester in which 88 mol% or more of the constituent units are ethylene terephthalate, and the core and It is characterized in that the composite ratio with the sheath part is 10=1 to 2:1.
本発明の高収縮性ポリエステル系繊維の横断面は、第1
図の如く芯鞘型複合繊維である。芯部は超高収縮成分で
あり、グリコール成分の15〜35モル%がCHDMで
共重合されたPETである。好ましい共重合率は20〜
30モル%である。The cross section of the high shrinkage polyester fiber of the present invention is
As shown in the figure, it is a core-sheath type composite fiber. The core is an ultra-high shrinkage component, and is PET in which 15 to 35 mol% of the glycol component is copolymerized with CHDM. The preferred copolymerization rate is 20~
It is 30 mol%.
15モル%未満では収縮性が小さく、又35モル%を超
えると収縮性はほとんど変らず、又紡糸前のポリマー乾
燥時にオコシ現象(ポリマー粒体の融着)を生したりし
て、かえってトラブルを多くすることになる。芯部の該
共重合PETは、CHDMだけでなく、他のジオール成
分やテレフタル酸以外のジカルボン酸が共重合されてい
ても良いが、構成単位の60モル%以上はエチレンテレ
フタレート単位からなることが望ましい。If it is less than 15 mol%, the shrinkage will be small, and if it exceeds 35 mol%, the shrinkage will hardly change, and the sagging phenomenon (fusion of polymer granules) may occur when drying the polymer before spinning, which may cause trouble. This will result in a large number of The copolymerized PET of the core may be copolymerized with not only CHDM but also other diol components and dicarboxylic acids other than terephthalic acid, but 60 mol% or more of the constituent units may be composed of ethylene terephthalate units. desirable.
CHDM以外の共重合成分としてはジエチレングリコー
ル、トリエチレングリコール、テトラメチレングリコー
ル、ネオペンチルグリコールが挙げられ、テレフタル酸
以外のジカルボン酸としてはイソフタル酸、ソジュウム
スルホイソフタル酸ナフタレンジカルボン酸等が挙げら
れる。Examples of copolymerization components other than CHDM include diethylene glycol, triethylene glycol, tetramethylene glycol, and neopentyl glycol, and examples of dicarboxylic acids other than terephthalic acid include isophthalic acid, sodium sulfoisophthalate, naphthalene dicarboxylic acid, and the like.
CHDMを15〜35モル%共重合したPETは、繊維
に成形した時、湧水に浸漬すると極めて大きい収縮率を
示す、しかしこれらの多くの共重合PETは融点、軟化
点が低下し、一部のポリマーは全くの非晶体となり融点
を測定出来ないものもある。そして湧水浸漬中に膠着を
生しることさえある。PET copolymerized with 15 to 35 mol% CHDM exhibits an extremely large shrinkage rate when immersed in spring water when formed into fibers.However, many of these copolymerized PETs have lower melting points and softening points, and some Some polymers are completely amorphous and their melting points cannot be measured. And it may even form a stalemate during soaking in spring water.
その為、該CHDM共重合PETを繊維として用いるに
は、該CHDM共重合PETを芯部とし、その外周を取
り囲む様に比較的高融点の鞘部を形成させるのである。Therefore, in order to use the CHDM copolymer PET as a fiber, the CHDM copolymer PET is used as a core, and a sheath having a relatively high melting point is formed surrounding the outer periphery of the core.
鞘部のポリマーは、構成単位の88モル%以上がエチレ
ンテレフタレートからなるポリエステルである。PET
でもよいし、又イソフタル酸、ソジュウムスルホイソフ
タル酸CHDM、ジエチレングリコール、トリエチレン
グリコール等が12モル%未満であれば共重合していて
も良い、12モル%を超えるとmW物の精練や、熱セツ
ト時に膠着を生じてしまうことがある。The polymer of the sheath portion is a polyester in which 88 mol% or more of the structural units are ethylene terephthalate. PET
Alternatively, if isophthalic acid, sodium sulfoisophthalate CHDM, diethylene glycol, triethylene glycol, etc. are less than 12 mol%, they may be copolymerized. A stalemate may occur during setting.
芯部と鞘部との複合比は10:1〜2;lである。鞘部
比が小さすぎると複合紡糸の断面形態安定性が悪くなる
場合があり、又鞘部比が大きいと、芯部の収縮性が損な
われるのである。The composite ratio of core and sheath is 10:1-2;l. If the sheath ratio is too small, the stability of the cross-sectional shape of the composite spinning may deteriorate, and if the sheath ratio is too large, the shrinkability of the core will be impaired.
本発明の高収縮性ポリエステルの単糸繊度は、用途に合
わせて選べば良いが、衣料用途には1〜5dが好ましい
、又、断面形状も丸断面だけでなく、三角形、四角形等
芯鞘構造をとれるのであれば自由に選ぶことが出来る。The single yarn fineness of the highly shrinkable polyester of the present invention can be selected according to the application, but 1 to 5 d is preferable for clothing applications.The cross-sectional shape is not only round, but also has triangular and square equicore sheath structures. If you can take it, you can choose freely.
(実施例) 以下、実施例により詳しく説明する。(Example) Hereinafter, this will be explained in detail with reference to examples.
実施例1
ジメチルテレフタレート(以下DMTと略記)100部
と、エチレングリコール及び1・4CHDMの合計が1
00部となる種々の組合せのジオールを混合し、重合槽
に投入し、エステル交換触媒として酢酸カルシウムを用
いてエステル化反応させ、次いで重合触媒の三酸化アン
チモンを用いて1・4−CHDMO共重合比率の異なる
6種のCHDM共重合共重合PE台し各々チップ化した
。これらのチップを真空乾燥した後、PETと組合せ複
合紡糸した。共重合PETを芯部に、PETを鞘部にし
た第1図の如き芯鞘型複合繊維で、芯部:鞘部の複合比
は5:1とし、延伸後の繊度は70−d/24f、伸度
30%として6種のフィラメントを得た。尚、延伸時に
は熱セントは施こさなかった。チップの乾燥状況及び紡
糸結果第1表
湧水収縮率は荷重2 m g / dでの値である。Example 1 A total of 100 parts of dimethyl terephthalate (hereinafter abbreviated as DMT), ethylene glycol and 1.4CHDM is 1
00 parts of various combinations of diols were mixed, put into a polymerization tank, and subjected to an esterification reaction using calcium acetate as a transesterification catalyst, and then 1,4-CHDMO copolymerization using antimony trioxide as a polymerization catalyst. Six types of CHDM copolymerization and copolymerization PE units with different ratios were prepared and each was made into chips. After vacuum drying these chips, they were combined with PET and composite spun. A core-sheath type composite fiber as shown in Fig. 1 with copolymerized PET as the core and PET as the sheath, the core:sheath composite ratio was 5:1, and the fineness after drawing was 70-d/24f. , six types of filaments were obtained with an elongation of 30%. Note that no heat centrifugation was applied during stretching. Chip drying conditions and spinning results Table 1 Spring water shrinkage percentages are values at a load of 2 mg/d.
以上の結果より、湧水中の収縮率40%以上を基準とす
ると、芯部の1・4−CHDMO共重合率は15モル%
以上が必要であり、又チップ乾燥時のトラブルの点で共
重合率は35モル%以下が妥当であることが判る。From the above results, based on a shrinkage rate of 40% or more in spring water, the 1,4-CHDMO copolymerization rate in the core is 15 mol%.
The above is necessary, and in view of troubles during chip drying, it is found that a copolymerization rate of 35 mol % or less is appropriate.
実施例2
ビスヒドロキシエチレンテレフタレートとビスヒドロキ
シエチレンイソフタレートとを適宜混合し、重合槽で真
空下縮合重合し、イソフタル酸の共重合率が、4.8.
12.16モル%の4種のイソフタル酸共重合PET
(P7〜P1゜)を得、チップ化した。これらのチップ
を乾燥後、実施例1で用いたCHDM25モル%共重合
PE共重合PE色複合し、第1図の如き芯鞘型複合繊維
とした。紡糸・延伸は実施例1と同様に実施した。結果
を第以上の結果より、鞘部ポリマーは88モル%以上が
PETで構成されているのが好ましいことが判る。Example 2 Bishydroxyethylene terephthalate and bishydroxyethylene isophthalate were appropriately mixed and subjected to condensation polymerization under vacuum in a polymerization tank, and the copolymerization rate of isophthalic acid was 4.8.
12.16 mol% of 4 types of isophthalic acid copolymerized PET
(P7 to P1°) was obtained and made into chips. After drying these chips, the CHDM 25 mol % copolymer PE copolymer PE color composite used in Example 1 was applied to form a core-sheath type composite fiber as shown in FIG. Spinning and drawing were carried out in the same manner as in Example 1. From the above results, it can be seen that it is preferable for the sheath polymer to be composed of 88 mol% or more of PET.
実施例3
実施例1で用いたCHDM25モル%共重合PET (
P、 )と、実施例2で用いたイソフタル酸8モル%共
重合PET (Ps )とを、複合紡糸し、第1図の如
き芯鞘型複合糸50d/24fを得た。この際、芯部と
鞘部の複合比を適宜変化させた。紡糸・延伸は実施例1
と同様に行なった。Example 3 CHDM 25 mol% copolymerized PET used in Example 1 (
P, ) and the 8 mol % isophthalic acid copolymerized PET (Ps) used in Example 2 were composite-spun to obtain core-sheath type composite yarns 50d/24f as shown in FIG. At this time, the composite ratio of the core and sheath was changed as appropriate. Spinning/drawing is Example 1
I did the same thing.
この結果より、芯部と鞘部の複合比は2:1〜10:1
が良好である。From this result, the composite ratio of the core and sheath is 2:1 to 10:1.
is good.
(発明の効果)
本発明の高収縮性ポリエステル系繊維を用いて、他糸と
の混繊糸となし、製w1織後、熱処理又は清水処理する
ことにより、極めて嵩高性の大きい布帛となる。又、該
高収縮性ポリエステル系繊維は工程中でそれ自身の膠着
が生しない為、風合が硬くならないという利点を有する
。(Effects of the Invention) By using the highly shrinkable polyester fiber of the present invention, making it into a mixed yarn with other yarns, and performing a heat treatment or clean water treatment after weaving w1, a fabric with extremely high bulkiness can be obtained. In addition, the highly shrinkable polyester fiber does not stick to itself during the process, so it has the advantage that the texture does not become hard.
第1図〜第4図は、本発明の高収縮性ポリエステル系繊
維の横断面の形状例である。1 to 4 are examples of cross-sectional shapes of the highly shrinkable polyester fibers of the present invention.
Claims (1)
横断面に於る芯部はグリコール成分の15〜35モル%
がシクロヘキサリンメタノールで共重合されたポリエチ
レンテレフタレートであり、鞘部は構成単位の88モル
%以上がエチレンテレフタレートからなるポリエステル
であり、芯部と鞘部との複合比が10:1〜2:1であ
ることを特徴とする高収縮性ポリエステル系繊維。(1) A core-sheath type polyester composite fiber, in which the core portion in the single fiber cross section contains 15 to 35 mol% of the glycol component.
is polyethylene terephthalate copolymerized with cyclohexaline methanol, the sheath is a polyester in which 88 mol% or more of the constituent units are ethylene terephthalate, and the composite ratio of the core and sheath is 10:1 to 2:1. A highly shrinkable polyester fiber characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18610190A JPH0473217A (en) | 1990-07-12 | 1990-07-12 | Highly shrinkable polyester fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18610190A JPH0473217A (en) | 1990-07-12 | 1990-07-12 | Highly shrinkable polyester fiber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0473217A true JPH0473217A (en) | 1992-03-09 |
Family
ID=16182383
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18610190A Pending JPH0473217A (en) | 1990-07-12 | 1990-07-12 | Highly shrinkable polyester fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0473217A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995009260A1 (en) * | 1993-09-30 | 1995-04-06 | E.I. Du Pont De Nemours And Company | New fiberballs |
| US5480710A (en) * | 1993-09-30 | 1996-01-02 | E. I. Du Pont De Nemours And Company | Fiberballs |
| CN102392498A (en) * | 2011-10-19 | 2012-03-28 | 沈阳建筑大学 | Four-concave edge porous metal damper |
-
1990
- 1990-07-12 JP JP18610190A patent/JPH0473217A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1995009260A1 (en) * | 1993-09-30 | 1995-04-06 | E.I. Du Pont De Nemours And Company | New fiberballs |
| US5480710A (en) * | 1993-09-30 | 1996-01-02 | E. I. Du Pont De Nemours And Company | Fiberballs |
| CN102392498A (en) * | 2011-10-19 | 2012-03-28 | 沈阳建筑大学 | Four-concave edge porous metal damper |
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