JPH0359112A - Elastic yarn for separation - Google Patents
Elastic yarn for separationInfo
- Publication number
- JPH0359112A JPH0359112A JP19047389A JP19047389A JPH0359112A JP H0359112 A JPH0359112 A JP H0359112A JP 19047389 A JP19047389 A JP 19047389A JP 19047389 A JP19047389 A JP 19047389A JP H0359112 A JPH0359112 A JP H0359112A
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- elastic yarn
- separation
- spinning chamber
- splitting
- 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
- 238000000926 separation method Methods 0.000 title claims description 31
- 239000004814 polyurethane Substances 0.000 claims description 23
- 229920002635 polyurethane Polymers 0.000 claims description 23
- 238000009987 spinning Methods 0.000 abstract description 36
- 238000004804 winding Methods 0.000 abstract description 10
- HQKMJHAJHXVSDF-UHFFFAOYSA-L magnesium stearate Chemical compound [Mg+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O HQKMJHAJHXVSDF-UHFFFAOYSA-L 0.000 abstract description 6
- 239000004205 dimethyl polysiloxane Substances 0.000 abstract description 3
- 235000013870 dimethyl polysiloxane Nutrition 0.000 abstract description 3
- 235000019359 magnesium stearate Nutrition 0.000 abstract description 3
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 abstract description 3
- 239000000919 ceramic Substances 0.000 abstract description 2
- 238000001816 cooling Methods 0.000 description 14
- 239000000835 fiber Substances 0.000 description 11
- 238000000034 method Methods 0.000 description 11
- 229920000642 polymer Polymers 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 239000000344 soap Substances 0.000 description 6
- 239000000567 combustion gas Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 3
- 235000013539 calcium stearate Nutrition 0.000 description 3
- 239000008116 calcium stearate Substances 0.000 description 3
- 238000001612 separation test Methods 0.000 description 3
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-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
- 230000000694 effects Effects 0.000 description 2
- 238000009940 knitting Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000005639 Lauric acid Substances 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 229920002334 Spandex Polymers 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 235000013351 cheese Nutrition 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 239000004759 spandex Substances 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は整経機、カバリング機、合撚機、コアースパン
精紡機、編機などにおいて分繊しながら使用できるポリ
ウレタン弾性糸に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a polyurethane elastic yarn that can be used while being divided in a warping machine, a covering machine, a twisting machine, a core-span spinning machine, a knitting machine, etc.
(従来技術)
一般にポリウレタン弾性糸は紡糸室下部より出て来た複
数のマルチフィラメントを粘着性のある状態でフィラメ
ント相互を接合させた一本の接合マルチフィラメント、
あるいは−本のモノフィラメントを一個のパッケージに
巻いたものが従来のポリウレタン弾性糸の製品となって
いる。(Prior art) Polyurethane elastic yarn is generally a single bonded multifilament made by bonding multiple multifilaments coming out of the lower part of the spinning chamber with each other in an adhesive state.
Alternatively, a conventional polyurethane elastic yarn product consists of a book of monofilament wound into a single package.
このようにして巻かれたポリウレタン弾性糸は一個のボ
ビンに一本の糸が巻かれたものである為に整経機、コア
ースパン精紡機、カバリング機、合撚機あるいは編機に
直接かける場合、必要な糸の本数だけパッケージの個数
が必要でありパッケージを取付けるクレードル、送り出
しロール、送り出し装置など設備が大がかりなものにな
らざるを得ない。Since the polyurethane elastic yarn wound in this way is a single thread wound around a single bobbin, when it is directly applied to a warping machine, core-span spinning machine, covering machine, twisting machine, or knitting machine, The number of packages required is equal to the number of threads required, and equipment such as a cradle for mounting the packages, a delivery roll, and a delivery device must be large-scale.
従来、ナイロンあるいはポリエステル繊維などの非弾性
のフィラメント数十本を一個のボビンに巻き取り、分繊
用に供することがなされていることは周知のところであ
る。しかし高い弾性と粘着性を有するポリウレタン弾性
糸において分繊可能な製品として実用化された例は無く
、特公昭47−17086号公報が唯−知られている。It is well known that several tens of inelastic filaments such as nylon or polyester fibers have been wound around a single bobbin and used for fiber separation. However, there is no example of polyurethane elastic yarn having high elasticity and adhesiveness being put into practical use as a splittable product, and the only known example is Japanese Patent Publication No. 47-17086.
特公昭47−17086号公報によれば、通常法に従っ
て引揃えて巻きとる方法では分離性の良い分繊用弾性糸
が得られない為、斜め溝付きガイドにより糸を実質的に
並列に並べて巻き取る特殊な方法を採っている。この為
、ガイド及びゴデツトロールでの糸間距離の制約が多く
、紡糸速度を上げることができない、ゴデツトロールと
フリクションロールが平行に配置されたパラレル型ワイ
ンダーは使用できない、斜溝からの糸の飛出し外れや、
オイリングロール、ゴデツトロール上を通過する糸本数
が多数となるため糸切れ確率の増加など多くの問題を有
し実用化に至っていないのが実状である。According to Japanese Patent Publication No. 47-17086, since it is not possible to obtain elastic threads for splitting with good separability by the usual method of aligning and winding the threads, the threads are wound substantially in parallel using a diagonally grooved guide. A special method is used to remove For this reason, there are many restrictions on the distance between the yarns in the guide and godet rolls, making it impossible to increase the spinning speed.Parallel winders with godet rolls and friction rolls arranged in parallel cannot be used.The yarn comes off from the diagonal grooves. or,
As the number of threads passing over the oiling roll and godet roll increases, there are many problems such as an increased probability of thread breakage, and the actual situation is that this method has not been put into practical use.
近年、加工分野における生産性向上から弾性糸の走行速
度も大巾に上昇し200m/分を超える場合もある。糸
間の相互の分離性は弾性糸の走行速度が増すほど悪くな
り、従来技術では数十111分では使用可能であったが
100m/分を超える走行速度では使用できなかった。In recent years, due to improved productivity in the processing field, the running speed of elastic yarn has increased significantly, sometimes exceeding 200 m/min. The mutual separability between the yarns worsens as the running speed of the elastic yarn increases, and in the prior art, it could be used at a running speed of several tens of 111 minutes, but it could not be used at a running speed exceeding 100 m/min.
(発明が解決しようとする課R)
本発明はこのような従来の分線用ポリウレタン弾性糸の
製造面又は分離性能面の課題を解決し高速度の使用にお
いても優れた性能を持つ分繊用ポリウレタン弾性糸を提
供しようとするものである。(Problem R to be solved by the invention) The present invention solves the problems in terms of production and separation performance of conventional polyurethane elastic yarns for separating fibers, and provides a polyurethane elastic yarn for dividing fibers that has excellent performance even when used at high speeds. It is intended to provide a polyurethane elastic yarn.
(課題を解決するための手段)
すなわち、本発明は複数本の接合マルチフィラメントあ
るいはモノフィラメントが一個のボビンに巻かれたポリ
ウレタン弾性糸で引き揃えて巻かれた接合マルチフィラ
メントあるいはモノフィラメントの相互の分離応力が1
5■以下である分繊用ポリウレタン弾性糸である。(Means for Solving the Problem) That is, the present invention solves the mutual separation stress of a plurality of bonded multifilaments or monofilaments wound in parallel with a polyurethane elastic thread wound around a single bobbin. is 1
This is a polyurethane elastic yarn for splitting that has a particle diameter of 5 or less.
本発明でいう弾性糸としては少くとも85%がセグメン
ト重合したポリウレタンである繊維から形成されたいわ
ゆるスパンデックスをあげられる。The elastic yarn used in the present invention includes so-called spandex, which is formed from fibers of which at least 85% are segmentally polymerized polyurethane.
接合マルチフィラメントとはフィラメント相互が簡単に
分離しない状態に接着されたマルチフィラメントであり
、分離応力が20■以上好ましくは100■以上である
マルチフィラメントである。A bonded multifilament is a multifilament in which the filaments are bonded together such that they cannot be easily separated from each other, and is a multifilament having a separation stress of 20 or more, preferably 100 or more.
本発明でいう分繊とは複数本の分離しないように接合し
たマルチフィラメント、または複数本のモノフィラメン
トが一個のボビンに引揃えて巻いたものを巻き返しによ
り各々に単独のマルチフィラメント又はモノフィラメン
トとすることである。In the present invention, fiber splitting refers to multiple multifilaments joined together so that they do not separate, or multiple monofilaments wound together on a single bobbin, each of which is wound back into a single multifilament or monofilament. It is.
この分繊時に分離応力が15+g以下好ましくは10に
以下であれば150m/分の走行速度においてもスムー
ズに糸の張力むらもなく分離することができる。If the separation stress is 15+g or less, preferably 10 or less, the fibers can be separated smoothly even at a running speed of 150 m/min without uneven yarn tension.
分離応力を15■以下にする手段は、例えば、糸条が紡
糸室を出るとき、又は出たあとに強制的に冷却する方法
を採る。糸条が第1ゴデツトロールに到達するまでに静
止ガイドで引揃えて巻取る方法において糸条温度と糸条
相互の分離応力の関係について鋭意検討の結果、糸条温
度が60℃以下では糸条相互に接着性が殆んどなく、発
明の狙いとする分離性の良好な分繊用弾性糸が得られる
。The means for reducing the separation stress to 15 .mu. or less is, for example, a method in which the yarn is forcibly cooled when it leaves the spinning chamber or after it leaves the spinning chamber. As a result of intensive studies on the relationship between the yarn temperature and the separation stress between the yarns in the method of winding the yarns by pulling them together with a stationary guide before reaching the first godet roll, we found that when the yarn temperature is 60°C or less, the yarns do not separate from each other. An elastic yarn for splitting with almost no adhesiveness and good separability, which is the aim of the invention, can be obtained.
しかし乍ら、糸条の冷却速度は糸条の速度、デニールで
変わるものであり、太いデニールあるいは糸条速度が速
い場合には、第1ゴデツトロールまでの間で糸条温度を
60℃以下に冷却するには冷却ゾーンが不足し製造上、
支障が生じる場合がある。However, the cooling rate of the yarn varies depending on the speed and denier of the yarn, and if the denier is thick or the yarn speed is fast, the yarn temperature will be cooled to 60°C or less before the first godet roll. Due to manufacturing, there is insufficient cooling zone to
Problems may occur.
例えば、70デニールで550m/分の紡糸速度の場合
、10″Cの冷風で糸条温度を60℃以下に冷却するに
は、冷却ゾーンが105cm必要となる。一般に紡糸室
出口から第1ゴデツトロールまでの距離は1m前後であ
り、短い冷却距離で糸条の冷却を達成できなければなら
ない。For example, in the case of 70 denier and a spinning speed of 550 m/min, a cooling zone of 105 cm is required to cool the yarn temperature to below 60°C with cold air at 10"C. Generally, from the exit of the spinning chamber to the first godet roll. The distance is approximately 1 m, and cooling of the yarn must be achieved with a short cooling distance.
更に、本発明者等は、従来公知の離形剤をポリウレタン
重合体の溶液中へ配合し同様の方法で糸条温度と糸条相
互の分離応力について種々検討を行ったところ微量の金
属石鹸を配合することにより糸条温度が75℃以下で本
発明の狙いとする糸条間の分離性能が得られる。Furthermore, the present inventors mixed a conventionally known mold release agent into a polyurethane polymer solution and conducted various studies on yarn temperature and separation stress between yarns using the same method, and found that a trace amount of metal soap was released. By blending, the separation performance between yarns that is the aim of the present invention can be obtained at a yarn temperature of 75° C. or lower.
糸条温度が75℃以上で引揃えた場合、糸条相互の接着
現象が現われ分離応力が高くなる。糸条温度を低くする
には紡糸室を出たあとの強制冷却と糸条が紡糸室を出る
段階で出来る丈、糸条温度を低くしておくことが有利で
あり、紡糸室下部からの向流空気量を増すことが好まし
い。When the yarns are pulled together at a temperature of 75° C. or higher, a phenomenon in which the yarns adhere to each other occurs and separation stress increases. In order to lower the yarn temperature, it is advantageous to forcibly cool the yarn after it leaves the spinning chamber, to lower the length of the yarn when it leaves the spinning chamber, and to lower the yarn temperature. It is preferable to increase the flow rate.
本発明はポリウレタン重合体の溶液への金属石鹸の配合
と糸条を引揃えるときの糸条温度を組合わせる事にまり
分繊用弾性糸としての優れた糸条相互の分離性能と効率
的な製造方法を達成することができる。The present invention combines the addition of metal soap to the polyurethane polymer solution and the yarn temperature when pulling the yarns together, resulting in excellent separation performance and efficient yarn separation as elastic yarn for fiber splitting. The manufacturing method can be achieved.
ポリウレタン重合体?8iへ配合する好ましい金属石鹸
としては、リチウム、カルシウム、マグネシウム、亜鉛
、アルミニウムなどの金属とラウリン酸、ステアリン酸
などの脂肪酸との組合せが挙げられる。配合する金属石
鹸の量はポリウレタン重量に対し0.01%〜5%、好
ましくは0.03%〜0.5%の配合が好ましい。Polyurethane polymer? Preferred metal soaps to be added to 8i include combinations of metals such as lithium, calcium, magnesium, zinc, and aluminum and fatty acids such as lauric acid and stearic acid. The amount of metal soap to be blended is preferably 0.01% to 5%, preferably 0.03% to 0.5%, based on the weight of the polyurethane.
この範囲未満では糸条相互の分離応力が高くなり分繊用
弾性糸としての効果が不充分となる。−方、上記範囲を
超えると糸条相互の分離応力は優れるが弾性糸のもつ物
性の低下、スカムの発生、動摩擦性の低下など後工程の
トラブル発生の原因となる。If it is less than this range, the separation stress between the yarns will be high and the effect as an elastic yarn for splitting will be insufficient. - On the other hand, if it exceeds the above range, although the separation stress between the yarns is excellent, it causes problems in subsequent processes such as deterioration of the physical properties of the elastic yarn, generation of scum, and deterioration of dynamic friction properties.
本発明の分繊用弾性糸の製造方法の一例を示す。An example of the method for manufacturing the elastic yarn for fiber splitting of the present invention will be shown.
第1図は3フィラメント接合マルチフィラメントを4本
形威し、4本の糸を2本づつ引揃え2個のボビンに巻き
とる接合マルチフィラメントの分繊用弾性糸の製造方法
である。FIG. 1 shows a method for producing elastic yarn for splitting a bonded multifilament, in which four 3-filament bonded multifilaments are formed, and the four yarns are aligned two by two and wound around two bobbins.
金属石鹸を含むポリウレタン重合体の溶液を紡糸室1に
取付けられた紡糸アセンブリー2へ圧入する。紡糸口金
のオリフィス3からt8i1が押出され、これに熱風人
口4を通って紡糸室に導入される高温燃焼筒@燃焼ガス
を並流に当てる。A solution of polyurethane polymer containing metal soap is forced into a spinning assembly 2 attached to a spinning chamber 1 . The t8i1 is extruded from the orifice 3 of the spinneret, and is exposed to a cocurrent flow of high-temperature combustion tube@combustion gas, which is introduced into the spinning chamber through the hot air outlet 4.
ポリウレタン重合体の溶媒は蒸発し連続フィラメント1
3が形威される。The solvent of the polyurethane polymer evaporates and the continuous filament 1
3 is expressed.
連続フィラメントは紡糸室出口に取りつけられた撚糸機
16により撚りがかけられ紡糸室内に撚り点14がくる
よう調整され接合マルチフィラメント15が形威される
。蒸発した溶媒は高温燃焼ガスとともに熱風出口5より
排出されるが紡糸室1の下部の穴より溶媒が出ないよう
通常導入した高温燃焼ガスと蒸発した溶媒の総量より多
く排出し紡糸室下部より空気が向流に流れるようにして
いる。The continuous filaments are twisted by a twisting machine 16 installed at the outlet of the spinning chamber, and the twisting points 14 are adjusted to be within the spinning chamber to form a bonded multifilament 15. The evaporated solvent is discharged from the hot air outlet 5 together with the high-temperature combustion gas, but in order to prevent the solvent from coming out from the hole at the bottom of the spinning chamber 1, a larger amount than the total amount of the high-temperature combustion gas and evaporated solvent that is normally introduced is discharged, and air is discharged from the lower part of the spinning chamber. flows countercurrently.
接合マルチフィラメントの糸条温度は紡糸室下部からの
向流空気量で調整されるが、更に接合マルチフィラメン
トが紡糸室を出たあとスリットより冷風が吹出す冷却装
置6により糸条温度が75℃以下になるよう調整された
後、静止ガイド7で引揃えられ第1ゴデツトロール8と
第2ゴデツトロール10の中間に設けられた油剤ロール
9により油剤を付与し、フリクションロール11により
分繊用弾性糸12として巻き取られる。The yarn temperature of the bonded multifilament is adjusted by the amount of countercurrent air flowing from the bottom of the spinning chamber, and after the bonded multifilament leaves the spinning chamber, a cooling device 6 that blows cold air from the slit keeps the yarn temperature at 75°C. After the adjustment is made so that It is wound up as.
第2図は複数のモノフィラメントが1個のチーズに巻か
れたモノフィラメント分繊用弾性糸の製造方法を示した
ものである。FIG. 2 shows a method for manufacturing an elastic yarn for monofilament splitting, in which a plurality of monofilaments are wound around one piece of cheese.
第2図では、6本のモノフィラメント13を形威し、お
互いのフィラメントが接触しない状態で紡糸室1を引出
し6本のフィラメントを3本づつ2個のボビンに巻きと
る方法を例示しである。FIG. 2 shows an example of a method in which six monofilaments 13 are formed, the spinning chamber 1 is pulled out in a state where the filaments do not contact each other, and the six filaments are wound onto two bobbins, three each.
モノフィラメントの分繊用弾性糸を作る場合は第1図に
示される紡糸室下部の撚糸機を必要としない。紡糸室か
ら引出されたフィラメントは静止ガイド7で引揃えられ
巻き取られる。この場合もフィラメント相互の分離応力
を15■以下にする為に静止ガイド7で引揃えられる時
の糸条温度は接合マルチフィラメントと同様、75°C
以下に調整される。When producing elastic yarn for monofilament splitting, the twisting machine at the bottom of the spinning chamber shown in FIG. 1 is not required. The filaments pulled out from the spinning chamber are aligned by a stationary guide 7 and wound up. In this case as well, the yarn temperature when the filaments are pulled together by the stationary guide 7 is 75°C, which is the same as in the bonded multifilament, in order to keep the separation stress between the filaments below 15cm.
Adjusted below.
冷却装置6は5〜15°Cの冷風を糸が乱れない程度の
吹出し量で調整される。糸条速度、デニールにより冷却
速度が早く、紡糸室の下部からの向流空気量調整と紡糸
室外の雰囲気温度のみで糸条温度を75°C以下に調整
できる場合は冷却装置6を使用しなくても本発明を達成
することができる。The cooling device 6 blows out cold air at a temperature of 5 to 15°C at an amount that does not disturb the threads. If the cooling rate is fast depending on the yarn speed and denier, and the yarn temperature can be adjusted to 75°C or less only by adjusting the amount of countercurrent air from the bottom of the spinning chamber and the ambient temperature outside the spinning chamber, the cooling device 6 is not used. The present invention can also be achieved.
静止ガイド7は、摩擦抵抗の小さいアルξす、チタン等
のセラミックガイドが好ましく、引揃えた糸条が外れな
い構造のものがあれば良い。The stationary guide 7 is preferably a ceramic guide made of aluminum, titanium, or the like, which has low frictional resistance, and any guide that has a structure that prevents the aligned threads from coming off is sufficient.
本発明において静止ガイドで引揃えられた糸条は、第1
ゴデツトロールと第2ゴデントロールの中間で油剤を付
与し巻き取られる。In the present invention, the yarns aligned by the stationary guide are
An oil agent is applied between the godet roll and the second godet roll and the product is wound up.
油剤の種類は、−iに使用されるジメチルポリシロキサ
ン、あるいは、ステアリン酸マグネシウムを分散配合し
たジメチルポリシロキサンが好ましい。As for the type of oil agent, dimethylpolysiloxane used in -i or dimethylpolysiloxane in which magnesium stearate is dispersed is preferable.
本発明で用いた測定方法について説明する。The measurement method used in the present invention will be explained.
分離応力の測定は東洋ボールドウィン社製のテンシロン
引張試験機によって行った。2本の接合マルチフィラメ
ント又はモノフィラメントの場合、長さ方向にまず分離
しテンシロン試験機のクランプに把持し50cm/分の
速度で引離し分離に要した応力を測定する。The separation stress was measured using a Tensilon tensile tester manufactured by Toyo Baldwin. In the case of two bonded multifilaments or monofilaments, they are first separated in the length direction, held in the clamps of a Tensilon tester, pulled apart at a speed of 50 cm/min, and the stress required for separation is measured.
2本以上の接合マルチフィラメント又はモノフィラメン
トの場合は、まず−本を手で分離し、これと残る複数本
の群とを上記方法でクランプに把持し測定しすべてが分
離される迄くり返し測定する。In the case of two or more bonded multifilaments or monofilaments, first separate the books by hand, hold this and the remaining group in a clamp using the method described above, and measure repeatedly until all are separated.
第3図に走行時の分離試験装置の概略図を示した。Figure 3 shows a schematic diagram of the separation testing device during running.
送り出しロール17上に分繊用弾性糸12を接し、これ
より糸を引き出して、糸条を分離し巻き取りロール19
上に接したボビン18へ分離した糸条を巻付は巻き返す
装置である。The elastic thread 12 for splitting is brought into contact with the sending roll 17, the thread is pulled out from this, the threads are separated, and the winding roll 19
This is a device for winding and rewinding the separated yarn onto the bobbin 18 that is in contact with the upper part.
途中、スネルガイド20を設は分離した糸と糸とのなす
角(θ)は10度にセットしである。A snell guide 20 is installed on the way, and the angle (θ) between the separated threads is set to 10 degrees.
走行時の分離性はこの装置を使用して送り出し速度15
0m/分、巻取り速度225m/分の条件で判断した。Separation during running was achieved using this device at a feed rate of 15
The judgment was made under the conditions of 0 m/min and winding speed of 225 m/min.
実施例1
ポリエーテル系ポリウレタン重合体のジメチルアセトア
ミド溶液にこのポリウレタンに対し0.2重量パーセン
トのステアリン酸マグネシウムを配合し真空脱泡後、口
径0.2mm孔数8ホールのノズルから230°Cの燃
焼ガスを流した紡糸室に押出し10デニールの8本フィ
ラメントを形成し、紡糸室の下部に設けた冷却装置で表
−1に示した糸条温度に冷却した後、静止ガイドで2本
づつ引揃えジメチルポリオキシロキサンを主成分とした
油剤を糸に対し5%付与しながら500m/分の紡速で
4個のボビンに巻き取ったモノフィラメントの分繊用弾
性糸を得た。Example 1 A dimethylacetamide solution of a polyether-based polyurethane polymer was mixed with 0.2% by weight of magnesium stearate based on the polyurethane, and after vacuum defoaming, the solution was heated to 230°C through a nozzle with 8 holes of 0.2 mm in diameter. Eight filaments of 10 denier were extruded into a spinning chamber through which combustion gas was flowed, and after cooling to the yarn temperature shown in Table 1 with a cooling device installed at the bottom of the spinning chamber, the filaments were pulled two by two using a stationary guide. A monofilament elastic yarn for splitting was obtained by winding it around four bobbins at a spinning speed of 500 m/min while adding 5% of an oil agent mainly composed of dimethylpolyoxyloxane to the yarn.
得られた分繊用弾性糸の分離液流と走行分離試験装置で
150m/分の速度でIO分間走行させた時に発生した
糸切れ回数を表−1に示した。Table 1 shows the separation liquid flow of the obtained elastic yarn for fiber splitting and the number of yarn breakages that occurred when the yarn was run for IO minutes at a speed of 150 m/min using a running separation testing device.
表−1
本発明で得られた分繊用弾性糸は分離応力かきわめて小
さく走行分離試験でも糸切れは認められなかった。Table 1 The elastic yarn for fiber splitting obtained by the present invention had a very small separation stress and no yarn breakage was observed even in the running separation test.
実施例2
ポリエステル系ポリウレタン重合体のジメチルアセトア
ミド溶液にポリウレタンに対し0%、0.05%、2.
0%、6.0%のステアリン酸カルシウムを配合し真空
脱泡後、口径0.2 wa、孔数32ホールのノズルか
ら250°C燃焼ガスを流した紡糸室に押出し紡糸室下
部のエアージェット撚糸機でフィラメント4本づつ束ね
て撚りをかけ8本の40デニールの接合マルチフィラメ
ントを形成した。Example 2 In a dimethylacetamide solution of a polyester-based polyurethane polymer, 0%, 0.05%, 2.
After blending 0% and 6.0% calcium stearate and vacuum degassing, the yarn was extruded into a spinning chamber in which 250°C combustion gas was flowed through a nozzle with a diameter of 0.2 wa and 32 holes, and air-jet twisted yarn was created at the bottom of the spinning chamber. Four filaments were bundled and twisted using a machine to form eight 40-denier bonded multifilaments.
紡糸室下方の排気口より導入した高温燃焼ガスと蒸発し
た溶剤の総量の1.7倍の排出を行ない紡糸室の下部か
らの向流空気で糸条を冷却した後、エアージェット撚糸
機の下部に設けた冷却装置により接合マルチフィラメン
トの糸条温度を75°Cに冷却し静止ガイドで2本づつ
引揃え、2%のステアリン酸マグネシウムを分散配合せ
しめたジメチルポリシロキサン主成分とした油剤を糸に
付し4%付与しながら550m/分の紡速で4個のボビ
ンに巻き取った接合マルチフィラメントの分繊用弾性糸
を得た。After exhausting 1.7 times the total amount of high-temperature combustion gas and evaporated solvent introduced from the exhaust port at the bottom of the spinning chamber and cooling the yarn with countercurrent air from the bottom of the spinning chamber, The temperature of the spliced multifilament yarns was cooled to 75°C using a cooling device installed at An elastic yarn for splitting a spliced multifilament was obtained by winding it around four bobbins at a spinning speed of 550 m/min while adding 4% to the yarn.
得られた分繊用弾性糸の分離応力と走行分離試験装置で
150m/分の速度で分離させながら10分間走行させ
た時の発生した糸切れ回数及びスカム発生量を表−2に
示した。Table 2 shows the separation stress of the obtained elastic yarn for splitting, the number of yarn breakages that occurred when the yarn was run for 10 minutes while separating at a speed of 150 m/min, and the amount of scum generated using a running separation test device.
スカム発生量の測定は糸をフィード速度25m/分で3
倍に延伸し走行させ、途中安全力ξソリの刃を直角に当
て力くソリ刃に蓄積するスカム量を測定した。To measure the amount of scum generated, feed the yarn at a feed speed of 25 m/min.
It was stretched to double its original size and run, and the blade of the safety force ξ was applied at a right angle during the run, and the amount of scum accumulated on the blade was measured.
表−2
本発明で得られた分繊用弾性糸は分離応力が低く、走行
時の分離もスムーズであり、糸切れも少ない。比較例4
のステアリン酸カルシウムを配合しなかった場合は分離
応力が高くなり糸切れも多い。一方、ステアリン酸カル
シウムを多く配合した比較例7は分離応力、糸切れ回数
とも良好であるがスカムが多く発生する欠点がある。Table 2 The elastic yarn for splitting obtained according to the present invention has low separation stress, smooth separation during running, and less yarn breakage. Comparative example 4
If calcium stearate is not added, the separation stress will be high and thread breakage will occur frequently. On the other hand, Comparative Example 7, in which a large amount of calcium stearate was blended, had good separation stress and number of thread breakages, but had the disadvantage of generating a lot of scum.
(本発明の効果)
本発明は複数本の接合マルチフィラメントあるいはモノ
フィラメントを一個のボビンに巻かれるため一個の紡糸
室および捲取機から数倍の本数の糸を同時に巻きとるこ
とが可能となり生産性を著しく向上させる。(Effects of the present invention) Since the present invention allows multiple spliced multifilaments or monofilaments to be wound onto a single bobbin, it is possible to simultaneously wind several times the number of threads from a single spinning chamber and winding machine, thereby increasing productivity. significantly improves
複数本を同時に引揃える点から140デニール以下の細
デニール、特に5デニール〜70デニールの分繊用弾性
糸において特に有利性を発揮することができる。Since a plurality of yarns can be aligned at the same time, it can be particularly advantageous for fine denier yarns of 140 deniers or less, particularly for splitting elastic yarns of 5 deniers to 70 deniers.
又、ポリウレタン重合体溶液への金属石鹸の配合と糸条
を引揃えるときの糸条温度を組合わせる事により優れた
分離性能が得られる為に第1ゴデツトロール以前で引揃
えるだけで製造が可能となり従来技術の特殊ガイドの使
用、余角ピッチの制約など問題点を解決することができ
、更に分離性能の優れた分繊用弾性糸が得られる。In addition, excellent separation performance can be obtained by combining the addition of metal soap to the polyurethane polymer solution and the yarn temperature when pulling the yarns together, making it possible to manufacture the yarn by simply pulling it together before the first godet roll. The problems of the prior art, such as the use of special guides and restrictions on complementary angle pitch, can be solved, and an elastic yarn for splitting with excellent separation performance can be obtained.
第1図:接合マルチフィラメントの分繊用弾性糸の製造
装置概略図、第2図:モノフィラメントの分繊用弾性糸
の製造装置概略図、第3図二分離試験装置概略図。
1・・・紡糸室、2・・・紡糸アセンブリー、3・・・
オリフィス、4・・・熱風入口、5・・・熱風出口、6
・・・冷却装置、7・・・静止ガイド、8・・・第1ゴ
デツトロール、9・・・油剤ロール、10・・・第2ゴ
デツトロール、11・・・フリクシランロール、12・
・・分繊用弾性糸、13・・・連続フィラメント、14
・・・撚り点、15・・・接合マルチフィラメント、1
6・・・撚糸機、17・・・送り出しロール、18・・
・ボビン、19・・・巻き取りロール、20・・・スネ
ルガイド。FIG. 1: Schematic diagram of an apparatus for producing elastic yarn for splitting spliced multifilaments, FIG. 2: Schematic diagram of an apparatus for producing elastic yarn for splitting monofilaments, and FIG. 3: Schematic diagram of a two-separation test apparatus. 1... Spinning chamber, 2... Spinning assembly, 3...
Orifice, 4...Hot air inlet, 5...Hot air outlet, 6
... Cooling device, 7... Stationary guide, 8... First Godet roll, 9... Oil agent roll, 10... Second Godet roll, 11... Flixiran roll, 12...
... Elastic yarn for splitting, 13 ... Continuous filament, 14
... Twisting point, 15 ... Joined multifilament, 1
6... Twisting machine, 17... Delivery roll, 18...
・Bobbin, 19... Winding roll, 20... Snell guide.
Claims (1)
ントが1個のボビンに引揃えて巻かれたポリウレタン弾
性糸で引揃えて巻かれた接合マルチフィラメントあるい
はモノフィラメントの相互の分離応力が15mg以下で
ある分繊用ポリウレタン弾性糸。A polyurethane elastic yarn for splitting in which the mutual separation stress of the bonded multifilaments or monofilaments is 15 mg or less, which is a polyurethane elastic thread in which a plurality of bonded multifilaments or monofilaments are aligned and wound around a single bobbin. thread.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19047389A JP2724214B2 (en) | 1989-07-25 | 1989-07-25 | Elastic yarn for fiber separation and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19047389A JP2724214B2 (en) | 1989-07-25 | 1989-07-25 | Elastic yarn for fiber separation and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0359112A true JPH0359112A (en) | 1991-03-14 |
JP2724214B2 JP2724214B2 (en) | 1998-03-09 |
Family
ID=16258698
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19047389A Expired - Lifetime JP2724214B2 (en) | 1989-07-25 | 1989-07-25 | Elastic yarn for fiber separation and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2724214B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0756026A1 (en) * | 1995-07-27 | 1997-01-29 | Bayer Faser GmbH | Process for manufacturing divisible thanelast-yarns |
WO1998028471A1 (en) * | 1996-07-24 | 1998-07-02 | Du Pont-Toray Company, Ltd. | Coalesced multifilament spandex and method for its preparation |
US6214145B1 (en) | 1996-07-24 | 2001-04-10 | Dupont Toray Co., Ltd. | Coalesced multifilament spandex and method for its preparation |
US6232374B1 (en) | 1997-01-31 | 2001-05-15 | E. I. Du Pont De Nemours And Company | Spandex with low tackiness and process for making same |
JP2011518261A (en) * | 2008-03-20 | 2011-06-23 | インビスタ テクノロジーズ エス エイ アール エル | Multi-end package of multifilament polyester bicomponent yarn |
US9487889B2 (en) | 2010-12-28 | 2016-11-08 | Invista North America S.A.R.L. | Bi-component spandex with separable reduced friction filaments |
KR102030709B1 (en) * | 2018-10-04 | 2019-10-10 | 주식회사 티케이케미칼 | Manufacturing apparatus of thermoplastic polyester elastic filament |
-
1989
- 1989-07-25 JP JP19047389A patent/JP2724214B2/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0756026A1 (en) * | 1995-07-27 | 1997-01-29 | Bayer Faser GmbH | Process for manufacturing divisible thanelast-yarns |
WO1998028471A1 (en) * | 1996-07-24 | 1998-07-02 | Du Pont-Toray Company, Ltd. | Coalesced multifilament spandex and method for its preparation |
US6214145B1 (en) | 1996-07-24 | 2001-04-10 | Dupont Toray Co., Ltd. | Coalesced multifilament spandex and method for its preparation |
US6623585B2 (en) | 1996-07-24 | 2003-09-23 | Dupont-Toray Co. Ltd. | Coalesced multifilament spandex and method for its preparation |
US6232374B1 (en) | 1997-01-31 | 2001-05-15 | E. I. Du Pont De Nemours And Company | Spandex with low tackiness and process for making same |
JP2011518261A (en) * | 2008-03-20 | 2011-06-23 | インビスタ テクノロジーズ エス エイ アール エル | Multi-end package of multifilament polyester bicomponent yarn |
US9487889B2 (en) | 2010-12-28 | 2016-11-08 | Invista North America S.A.R.L. | Bi-component spandex with separable reduced friction filaments |
KR102030709B1 (en) * | 2018-10-04 | 2019-10-10 | 주식회사 티케이케미칼 | Manufacturing apparatus of thermoplastic polyester elastic filament |
Also Published As
Publication number | Publication date |
---|---|
JP2724214B2 (en) | 1998-03-09 |
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