JPH083817A - Method of multi-strand spinning of polyether-ester elastic yarn - Google Patents
Method of multi-strand spinning of polyether-ester elastic yarnInfo
- Publication number
- JPH083817A JPH083817A JP15522194A JP15522194A JPH083817A JP H083817 A JPH083817 A JP H083817A JP 15522194 A JP15522194 A JP 15522194A JP 15522194 A JP15522194 A JP 15522194A JP H083817 A JPH083817 A JP H083817A
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- yarns
- polyether
- spinning
- spinneret
- 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
- 238000009987 spinning Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims description 17
- -1 poly(ethylene terephthalate) Polymers 0.000 claims abstract description 10
- 229920000139 polyethylene terephthalate Polymers 0.000 claims abstract description 8
- 239000005020 polyethylene terephthalate Substances 0.000 claims abstract description 8
- 238000007711 solidification Methods 0.000 claims abstract description 5
- 230000008023 solidification Effects 0.000 claims abstract description 5
- 229920001515 polyalkylene glycol Polymers 0.000 claims abstract description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 14
- 229920001707 polybutylene terephthalate Polymers 0.000 claims description 8
- 150000002148 esters Chemical class 0.000 claims description 5
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 4
- 229920000570 polyether Polymers 0.000 claims description 4
- 239000013013 elastic material Substances 0.000 claims description 2
- 238000011084 recovery Methods 0.000 abstract description 9
- 230000000704 physical effect Effects 0.000 abstract description 5
- 229920000642 polymer Polymers 0.000 abstract description 5
- 239000000126 substance Substances 0.000 abstract description 4
- WSQZNZLOZXSBHA-UHFFFAOYSA-N 3,8-dioxabicyclo[8.2.2]tetradeca-1(12),10,13-triene-2,9-dione Chemical compound O=C1OCCCCOC(=O)C2=CC=C1C=C2 WSQZNZLOZXSBHA-UHFFFAOYSA-N 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 229920000728 polyester Polymers 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000004804 winding Methods 0.000 description 4
- BJZYYSAMLOBSDY-QMMMGPOBSA-N (2s)-2-butoxybutan-1-ol Chemical compound CCCCO[C@@H](CC)CO BJZYYSAMLOBSDY-QMMMGPOBSA-N 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- WOZVHXUHUFLZGK-UHFFFAOYSA-N dimethyl terephthalate Chemical compound COC(=O)C1=CC=C(C(=O)OC)C=C1 WOZVHXUHUFLZGK-UHFFFAOYSA-N 0.000 description 2
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000012770 industrial material Substances 0.000 description 2
- 238000002074 melt spinning Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920002635 polyurethane Polymers 0.000 description 2
- 239000004814 polyurethane Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- XGIAHMUOCFHQTI-UHFFFAOYSA-N Cl.Cl.Cl.Cl.CC Chemical compound Cl.Cl.Cl.Cl.CC XGIAHMUOCFHQTI-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000004611 light stabiliser Substances 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000412 polyarylene Polymers 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 239000012744 reinforcing agent Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
Abstract
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は衣料用及び産業資材用と
して用いられる、優れた弾性回復性を有し、かつ、耐薬
品性、耐候(光)性、耐熱性の優れたポリエーテルエス
テル系弾性糸を効率的に製造することのできる多条紡糸
法に関するものである。
【0002】
【従来の技術】従来、衣料や産業資材用の弾性糸として
は、ポリウレタン系のものが最も一般的に使用されてい
る。しかしながら、ポリウレタン系弾性糸は優れた弾性
回復性を有するものの、耐熱性、耐薬品性、耐候(光)
性が劣るという欠点を有している。また、これらの問題
を解決すべく、近年、ポリエチレンテレフタレートやポ
リブチレンテレフタレートのような高結晶性ポリエステ
ルをハードセグメントとし、ポリアリキレングリコール
をソフトセグメントとするポリエーテルエステル系弾性
糸が開発され、実用化されている。しかし、ポリエーテ
ルエステル系弾性糸は、通常のポリエステル繊維に比べ
て製造方法が繁雑であったり、紡糸速度が低いため、生
産性が極端に劣るという問題を有している。生産性を向
上する手段として、一つの紡糸口金から複数の糸条を紡
出し、分割して巻き取る多条紡糸法が有効であるが、糸
条同士の密着や糸条間の物性斑等が生ずるという問題が
ある。
【0003】
【発明が解決しようとする課題】本発明は、優れた弾性
回復性能及び耐熱性、耐薬品性、耐候(光)性を有する
ポリエーテルエステル系弾性糸を通常の衣料用ポリエス
テルの製造設備を用いて効率的に製造することのできる
多条紡糸法を提供しようとするものである。
【0004】
【課題を解決するための手段】本発明者らは上記問題を
解決するために鋭意研究を重ねた結果、本発明に到達し
た。すなわち、ポリエチレンテレフタレート及び/又は
ポリブチレンテレフタレートをハードセグメントとし、
直鎖状ポリアルキレングリコールをソフトセグメントと
するポリエーテルエステル系弾性体を300m/分以上の紡
糸速度で一つの紡糸口金から4本以上の糸条を溶融紡糸
し、分割して巻き取る多条紡糸法において、糸条の固化
点より下方、紡糸口金吐出面から2500mm以内の位置で糸
分けガイドを用いて個々の糸条に分割した後、油剤を付
与することを特徴とするポリエーテルエステル系弾性糸
の多条紡糸法を要旨とするものである。
【0005】以下、本発明について詳細に説明する。本
発明の弾性糸を構成するポリエーテルエステルは、ポリ
エチレンテレフタレート(PET)及び/又はポリブチ
レンテレフタレート(PBT)をハードセグメントとす
る必要がある。PETとPBTの比率は特に限定されな
いが、PBTが多くなると弾性回復性が優れたものとな
り、PETが多くなると強伸度特性が優れたものとな
る。したがって、目的に応じて両者のモル比を100/0〜
0/100の範囲で選定すればよい。
【0006】一方、ソフトセグメントとしては、直鎖状
ポリアルキレングリコールが用いられるが、実用上、分
子量 500〜3000のポリテトラブチレンテレフタレート
(PTMG)が最適である。
【0007】ハードセグメントとソフトセグメントとの
割合は、特に限定されないが、通常、重量比で80/20〜
20/80の範囲で選定される。ハードセグメントが多けれ
ば強伸度特性は優れるが弾性回復性が劣り、ソフトセグ
メントの量が多ければ性能はその逆となるので、この点
を考慮して目的に合わせて適当な割合を選定すればよ
い。
【0008】また、ポリエーテルエステルは、酸化防止
剤、顔料、耐光剤、補強剤、改質剤等の添加剤を含有し
てしてもよい。
【0009】本発明は、ポリエーテルエステル系弾性糸
を効率的に製造することを目的としており、ポリエーテ
ルエステル系弾性体を300m/分以上の紡糸速度で一つの
紡糸口金から4本以上の糸条を溶融紡糸し、分割して巻
き取る多条紡糸法を対象とする。
【0010】本発明の最も重要な点は、このような多条
紡糸法において、糸条同士の密着や糸条間の物性斑を防
止するため、特定の位置で糸分けガイドで個々の糸条に
分割し、油剤を付与することにある。
【0011】すなわち、糸分けガイドを糸条の固化点よ
り下方、紡糸口金吐出面から2500mm以内で、かつ、油剤
付与装置の前に配設することが必要である。糸分けガイ
ドの位置が紡糸口金吐出面に近すぎると糸条が冷却固化
しておらず、ガイドに接触した時点で糸条が融着し糸切
れが発生する。本発明者らの経験によればポリエーテル
エステル系弾性体の場合、ポリマーの溶融粘度や融点に
関係なく、紡糸口金吐出後 600〜1000mm付近に固化点が
位置するように紡糸温度や冷却条件を調整すると安定な
紡糸が可能である。一方、紡糸口金吐出面から糸分けガ
イドまでの距離が2500mmを超えると糸搖れが大きく、糸
条同士の密着が生ずるため、分割巻取りができなくな
る。
【0012】これらの点を考慮すると、糸分けガイド
は、上記固化点より 100mm程度下方である紡糸口金吐出
面から2500mm以内の位置に設けるのが好ましい。また、
糸分けガイドは、油剤付与装置の前に設置することが必
要である。油剤付与装置の前で糸条の分割を行わない
と、紡出糸条が直接、油剤付与装置に入るため、特に回
転ローラ式油剤付与装置を用いる場合、糸道規制ができ
ないため回転ローラとの接触長が変わり、油剤の付着斑
が起こったり、張力斑による物性の変化が生じたりして
好ましくない。
【0013】本発明で用いられる油剤付与装置として
は、回転ローラ式やスリット式が好ましく、特に回転ロ
ーラ式が好ましい。
【0014】なお、油剤付与装置と第1ゴデットローラ
との間に第2糸分けガイドを設置すると糸分けがしやす
くなって好ましい。
【0015】本発明の方法の一実施態様の概略工程図を
図1に示す。紡糸口金1から吐出された糸条は、冷却筒
2で冷却されて固化した後、糸分けガイド3に入り、糸
分けされる。次いで、油剤付与装置4で給油された後、
第2糸分けガイド5、糸条幅出しガイド6を通り、第1
ゴデットローラ7で引き取られ、次いで第2ゴデットロ
ーラ8、糸道ガイド9を経て、巻取機10で巻き取られ
る。
【0016】
【実施例】次に、実施例により本発明を具体的に説明す
る。なお、例中の測定及び評価法は次のとおりである。
極限粘度
フェノールと四塩化エタンとの等重量混合物を溶媒とし
て、温度20℃で測定した。
弾性回復率
オリエンティック社製テンシロン UTM-4-100型を用い、
試料長10cm、引張速度10cm/分で100%又は200%まで伸
長した後、同速度で元の長さまで戻し、再度伸長した
時、応力が現れた時の長さを求め、次式によって弾性回
復率を求めた。なお、測定回数は10回とし、その平均値
で表した。
弾性回復率(YE)=〔 (E0ーE1)/E0 〕×100
E0:伸ばした長さ
E1:再度伸ばした時応力が現れた時の長さ
強伸度
オリエンティック社製テンシロン UTM-4-100型を用い、
試料長10cm,引張速度10cm/分で測定した。なお、測定
回数は10回とし、その平均値で表した。
【0017】実施例1〜4及び比較例1〜5
反応缶にテレフタル酸ジメチル19.4kg、1,4−ブタンジ
オール11.7kgを仕込み、触媒としてテトラブチルチタネ
ート10gを加え、常圧下 210℃で 2.5時間エステル交換
反応を行った。得られた反応物を重合缶に移送し、分子
量2000のPTMG33kgを添加し、次いで、250 ℃で4時
間、1トル以下の減圧下で重縮合反応を行った。得られ
たポリマーは、極限粘度〔η〕2.35、融点(Tm ) 185
℃であった。なお、このポリマーのPBTとPTMGと
の重量比は約5/5である。このポリマーを減圧乾燥
後、通常の溶融紡糸機を用い、紡糸温度を 260℃とし、
紡糸口金として直径 0.5mmの紡糸孔12個が円形に配列し
たものを用い、吐出量、第1ゴデットローラ(第1G
R)及び第2ゴデットローラ(第2GR)の速度並びに
巻取速度を表1のように設定して多条紡糸し、40デニー
ルの糸条12本を得た。この際、糸分けガイドの位置及び
油剤付与装置の位置も表1のように変化させた。(ただ
し、比較例1では、糸分けガイドの代わりに直径10mmの
梨地バーガイドを用いた。)
なお、油剤付与装置としては、回転ローラ式のものを用
い、油剤としては、シリコーン系水エマルジョンタイプ
のものを用い、巻取機としては、帝人製機社製AW 307型
巻取機を用いた。5日間連続紡糸を行い、一日当りの糸
切れ回数を調べるとともに、糸条の強伸度とそれらのば
らつき(標準偏差)及び弾性回復率を求めた。結果を表
1に示す。
【0018】
【表1】【0019】実施例6〜7及び比較例5〜6
紡糸口金の孔数を4又は6とした以外は実施例4及び比
較例3と同条件で吐出量を調整し、40デニールの糸条を
得た。この時の紡糸条件、得られた糸条の性能及び糸切
れ回数を表2に示す。
【0020】
【表2】
【0021】
【発明の効果】本発明によれば、ポリエーテルエステル
系弾性糸を多条溶融紡糸する際、糸搖れや糸条同士の密
着が防止され、物性斑の少ないポリエーテルエステル系
弾性糸を生産性よく製造することができる。また、本発
明の方法は、通常のポリエステル繊維を製造する紡糸装
置に若干の改良を加えた装置で容易に実施することが可
能である。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is used for clothing and industrial materials and has excellent elastic recovery, chemical resistance and weather (light) resistance. The present invention relates to a multi-spindle spinning method capable of efficiently producing a polyetherester-based elastic yarn having excellent heat resistance. Polyurethane-based elastic yarns have been most commonly used as elastic yarns for clothing and industrial materials. However, although polyurethane elastic yarns have excellent elastic recovery properties, they are heat resistant, chemical resistant, and weather resistant (light).
It has the drawback of being poor in performance. Further, in order to solve these problems, in recent years, a polyetherester-based elastic yarn having a highly crystalline polyester such as polyethylene terephthalate or polybutylene terephthalate as a hard segment and polyarylene glycol as a soft segment has been developed and put into practical use. Has been converted. However, the polyetherester elastic yarn has a problem that the productivity is extremely poor because the production method is complicated and the spinning speed is low as compared with ordinary polyester fiber. As a means of improving productivity, a multiple-spinning method in which multiple threads are spun from one spinneret and divided and wound is effective, but adhesion of the threads to each other and unevenness of physical properties between the threads may occur. There is a problem that it will occur. DISCLOSURE OF THE INVENTION The present invention uses a polyester ester elastic yarn having excellent elastic recovery performance, heat resistance, chemical resistance, and weather (light) resistance to produce polyester for ordinary clothing. An object of the present invention is to provide a multi-thread spinning method that can be efficiently manufactured using equipment. The present inventors have arrived at the present invention as a result of intensive studies to solve the above problems. That is, polyethylene terephthalate and / or polybutylene terephthalate as a hard segment,
A multi-spindle spinning method in which a polyetherester-based elastic body having a linear polyalkylene glycol as a soft segment is melt-spun from a single spinneret to four or more yarns at a spinning speed of 300m / min or more, and divided and wound. In this method, the polyether ester-based elastic material is characterized in that it is divided into individual yarns using a yarn dividing guide at a position below the solidification point of the yarns and within 2500mm from the spinneret discharge surface, and then an oil agent is applied. The main point is the multi-spinning method of yarn. The present invention will be described in detail below. The polyether ester constituting the elastic yarn of the present invention needs to have polyethylene terephthalate (PET) and / or polybutylene terephthalate (PBT) as a hard segment. The ratio of PET to PBT is not particularly limited, but when the PBT is large, the elastic recovery property is excellent, and when the PET is large, the strength / elongation property is excellent. Therefore, depending on the purpose, the molar ratio of both should be 100 / 0-
It may be selected in the range of 0/100. On the other hand, linear polyalkylene glycol is used as the soft segment, but in practical use, polytetrabutylene terephthalate (PTMG) having a molecular weight of 500 to 3000 is most suitable. The ratio of the hard segment to the soft segment is not particularly limited, but usually 80/20 by weight.
It is selected in the range of 20/80. If the hard segment is large, the strength / elongation property is excellent, but the elastic recovery is inferior, and if the amount of the soft segment is large, the performance is the opposite.Therefore, if this is taken into consideration, select an appropriate ratio according to the purpose. Good. Further, the polyether ester may contain additives such as an antioxidant, a pigment, a light stabilizer, a reinforcing agent and a modifier. The present invention is intended to efficiently produce a polyetherester-based elastic yarn, and a polyetherester-based elastic body is spun at a spinning speed of 300 m / min or more from one spinneret to four or more yarns. The target is the multi-spinning method in which a filament is melt-spun, divided and wound. The most important point of the present invention is that in such a multi-spinning method, in order to prevent the yarns from adhering to each other and the physical properties between the yarns to be prevented, individual yarns are guided by a yarn separating guide at a specific position. Divide into and apply the oil agent. That is, it is necessary to dispose the yarn separating guide below the solidification point of the yarn, within 2500 mm from the spinning nozzle discharge surface, and in front of the oil agent applying device. If the position of the yarn splitting guide is too close to the ejection face of the spinneret, the yarn is not cooled and solidified, and the yarn is fused and broken when it comes into contact with the guide. According to the experience of the present inventors, in the case of a polyetherester-based elastic body, the spinning temperature and cooling conditions are set so that the solidification point is located near 600 to 1000 mm after the spinning nozzle is discharged, regardless of the melt viscosity and melting point of the polymer. If adjusted, stable spinning is possible. On the other hand, if the distance from the spinneret discharge surface to the yarn separating guide exceeds 2500 mm, the yarn wobble becomes large and the yarns come into close contact with each other, so that the split winding cannot be performed. Considering these points, it is preferable that the yarn separating guide is provided at a position within 2500 mm from the spinneret discharge surface, which is about 100 mm below the solidifying point. Also,
The thread dividing guide needs to be installed in front of the oil agent applying device. If the yarn is not divided in front of the oil agent applying device, the spun yarn will directly enter the oil agent applying device. The contact length is changed, uneven adhesion of the oil agent occurs, and physical properties change due to uneven tension, which is not preferable. The oil agent applying device used in the present invention is preferably a rotary roller type or a slit type, and particularly preferably a rotary roller type. It is preferable that a second yarn splitting guide is provided between the oil agent applying device and the first godet roller because the yarn splitting is facilitated. A schematic process diagram of one embodiment of the method of the present invention is shown in FIG. The yarn discharged from the spinneret 1 is cooled by the cooling cylinder 2 and solidified, then enters the yarn separating guide 3 and is separated into yarns. Next, after being refueled by the oil agent applying device 4,
Passes through the second yarn splitting guide 5 and the yarn width guide 6 and
It is taken up by a godet roller 7, then passed through a second godet roller 8 and a yarn path guide 9, and then taken up by a winder 10. EXAMPLES Next, the present invention will be described in detail with reference to examples. The measurement and evaluation methods in the examples are as follows. The measurement was carried out at a temperature of 20 ° C using an equal weight mixture of an intrinsic viscosity phenol and ethane tetrachloride as a solvent. Elastic recovery rate Using Tensilon UTM-4-100 type manufactured by Oriental Co.,
After stretching to 100% or 200% at a sample length of 10 cm and a pulling speed of 10 cm / min, return to the original length at the same speed, and when stretching again, find the length when stress appears, and recover the elasticity by the following formula. I asked for the rate. The number of measurements was 10 and the average value was used. Elastic recovery rate (YE) = [(E 0 −E 1 ) / E 0 ] × 100 E 0 : Stretched length E 1 : Length at which stress appears when stretched again Strength Elongation Made by Oriental Using Tensilon UTM-4-100 type,
The sample length was 10 cm and the tensile speed was 10 cm / min. The number of measurements was 10 and the average value was used. Examples 1 to 4 and Comparative Examples 1 to 5 19.4 kg of dimethyl terephthalate and 11.7 kg of 1,4-butanediol were charged into a reaction vessel, 10 g of tetrabutyl titanate was added as a catalyst, and the mixture was heated under normal pressure at 210 ° C. for 2.5 hours. A transesterification reaction was performed. The obtained reaction product was transferred to a polymerization vessel, 33 kg of PTMG having a molecular weight of 2000 was added, and then a polycondensation reaction was carried out at 250 ° C. for 4 hours under a reduced pressure of 1 Torr or less. The polymer obtained has an intrinsic viscosity [η] of 2.35 and a melting point (Tm) of 185
° C. The weight ratio of PBT and PTMG in this polymer was about 5/5. After drying this polymer under reduced pressure, the spinning temperature was set to 260 ° C. using an ordinary melt spinning machine,
As the spinneret, 12 spinning holes with a diameter of 0.5 mm arranged in a circle were used, and the discharge amount, the first godet roller (first G
R) and the speed of the second godet roller (second GR) and the winding speed were set as shown in Table 1, and multi-thread spinning was performed to obtain 12 threads of 40 denier. At this time, the position of the thread dividing guide and the position of the oil agent applying device were also changed as shown in Table 1. (However, in Comparative Example 1, a satin bar guide having a diameter of 10 mm was used in place of the thread dividing guide.) A rotating roller type was used as the oil agent applying device, and a silicone water emulsion type was used as the oil agent. The AW 307 type winding machine manufactured by Teijin Seiki Co., Ltd. was used as the winding machine. Continuous spinning was carried out for 5 days, the number of yarn breakages per day was examined, and the tenacity and elongation of yarns, their variation (standard deviation), and elastic recovery rate were obtained. The results are shown in Table 1. [Table 1] Examples 6 to 7 and Comparative Examples 5 to 6 The discharge amount was adjusted under the same conditions as in Example 4 and Comparative Example 3 except that the number of holes in the spinneret was set to 4 or 6, and 40 denier yarn was prepared. Obtained. Table 2 shows the spinning conditions, the performance of the obtained yarn and the number of yarn breakages at this time. [Table 2] EFFECTS OF THE INVENTION According to the present invention, when a polyetherester-based elastic yarn is subjected to multi-thread melt-spinning, twisting and adhesion of the yarns to each other are prevented, and a polyetherester-based elastic yarn having less physical property unevenness. Can be manufactured with high productivity. Further, the method of the present invention can be easily carried out by an apparatus obtained by slightly improving a spinning apparatus for producing ordinary polyester fibers.
【図面の簡単な説明】
【図1】本発明の方法の一実施態様を示す概略工程図で
ある。
【符号の説明】
1 紡糸口金
2 冷却筒
3 糸分けガイド
4 油剤付与装置
5 第2糸分けガイド
6 糸条幅出しガイド
7 第1ゴデットローラ
8 第2ゴデットローラ
9 糸道規制ガイド
10 巻取機BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic process drawing showing one embodiment of the method of the present invention. [Explanation of Codes] 1 Spinneret 2 Cooling Tube 3 Thread Separation Guide 4 Lubricant Applying Device 5 Second Thread Separation Guide 6 Yarn Width Guide 7 First Godet Roller 8 Second Godet Roller 9 Thread Guide Restriction Guide 10 Winder
Claims (1)
ポリブチレンテレフタレートをハードセグメントとし、
直鎖状ポリアルキレングリコールをソフトセグメントと
するポリエーテルエステル系弾性体を300m/分以上の紡
糸速度で一つの紡糸口金から4本以上の糸条を溶融紡糸
し、分割して巻き取る多条紡糸法において、糸条の固化
点より下方、紡糸口金吐出面から2500mm以内の位置で糸
分けガイドを用いて個々の糸条に分割した後、油剤を付
与することを特徴とするポリエーテルエステル系弾性糸
の多条紡糸法。Claims: 1. Polyethylene terephthalate and / or polybutylene terephthalate as a hard segment,
A multi-spindle spinning method in which a polyetherester-based elastic body having a linear polyalkylene glycol as a soft segment is melt-spun from a single spinneret to four or more yarns at a spinning speed of 300m / min or more, and divided and wound. In this method, the polyether ester-based elastic material is characterized in that it is divided into individual yarns using a yarn dividing guide at a position below the solidification point of the yarns and within 2500mm from the spinneret discharge surface, and then an oil agent is applied. Multi-thread spinning method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15522194A JPH083817A (en) | 1994-06-13 | 1994-06-13 | Method of multi-strand spinning of polyether-ester elastic yarn |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15522194A JPH083817A (en) | 1994-06-13 | 1994-06-13 | Method of multi-strand spinning of polyether-ester elastic yarn |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH083817A true JPH083817A (en) | 1996-01-09 |
Family
ID=15601177
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15522194A Pending JPH083817A (en) | 1994-06-13 | 1994-06-13 | Method of multi-strand spinning of polyether-ester elastic yarn |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH083817A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100300915B1 (en) * | 1999-07-24 | 2001-09-22 | 조민호 | Manufacturing method for elastic fibers |
| WO2008070159A3 (en) * | 2006-12-06 | 2008-12-31 | Du Pont | Melt-spun elastoester multifilament yarns |
| KR20220090738A (en) * | 2020-12-23 | 2022-06-30 | 한국세라믹기술원 | WINDING DEVICE OF RIBON TYPE PCS FIBER AND METHOD FOR MANUFACTURING RIBON TYPE SiC FIBER USING THE SAME |
-
1994
- 1994-06-13 JP JP15522194A patent/JPH083817A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100300915B1 (en) * | 1999-07-24 | 2001-09-22 | 조민호 | Manufacturing method for elastic fibers |
| WO2008070159A3 (en) * | 2006-12-06 | 2008-12-31 | Du Pont | Melt-spun elastoester multifilament yarns |
| KR20220090738A (en) * | 2020-12-23 | 2022-06-30 | 한국세라믹기술원 | WINDING DEVICE OF RIBON TYPE PCS FIBER AND METHOD FOR MANUFACTURING RIBON TYPE SiC FIBER USING THE SAME |
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