JPS6223082B2 - - Google Patents
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- Publication number
- JPS6223082B2 JPS6223082B2 JP55103993A JP10399380A JPS6223082B2 JP S6223082 B2 JPS6223082 B2 JP S6223082B2 JP 55103993 A JP55103993 A JP 55103993A JP 10399380 A JP10399380 A JP 10399380A JP S6223082 B2 JPS6223082 B2 JP S6223082B2
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- Prior art keywords
- spinneret
- yarn
- speed
- fibers
- 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.)
- Expired
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- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Description
(産業上の利用分野)
本発明は新規な巻縮繊維の製造方法に関し、特
に溶融紡糸法によつて巻縮した合成繊維を製造す
る新規な製造方法を提供するものである。
(従来の技術)
従来より熱可塑性合成高分子からなる巻縮繊維
の製造法に関し生産コストの低減、生産性の向上
を目的として、紡糸−延伸−巻縮付与の連続化の
検討がさかんに行われている。しかし、紡糸速度
を1000m/min付近にする場合、延伸倍率を数倍
にする必要上巻縮付与速度としてはどうしても
3000〜4000m/minとなり、現状では満足すべき
巻縮付与が行えないため、実質上紡糸速度を1000
m/minよりもはるかに低く設定せざるをえず、
結局所期の目的を達成することができなかつた。
本発明者等はかかる現状に鑑み高速の巻縮付与
方法について鋭意検討した結果、現行の技術レベ
ルでは機械的な巻縮付与装置のみでは充分な巻縮
付与は困難でありなんらかの補助的手段が必要で
あること、またたとえば機械的に充分な巻縮付与
が可能であつても設備的に非常に高価なものとな
り、現実的でないという考えに至つた。
(発明が解決しようとする問題点)
本発明は強伸度、初期ヤング率などの力学的性
質並びに嵩高性に優れた熱化塑性合成繊維の巻縮
繊維を、設備的に簡略化された手段により、製糸
操業性良く3000m/min以上の高速度で製造する
新規な方法を提供せんとするものである。
(問題点を解決するための手段)
すなわち、本発明は、溶融紡出後紡糸口金直下
で一旦冷却した熱化塑性合成繊維を、紡糸口金と
表面周速度を3000m/min以上となした高速回転
引取ロール間で加熱帯域を通過させて延伸し、次
いで必要に応じて再延伸および/または熱処理を
行つた後、連続的に引き取るかまたは切断する合
成繊維の製造法において、紡糸口金として中空繊
維を製造することが可能な紡糸孔を有するものを
使用し、また加熱帯域を非接触の加熱装置で構成
し、かつ紡糸口金直下で糸条を横断面方向に非対
称的に冷却することにより、下記に定義する潜在
巻縮性1/ρが少なくとも1.5以上となるような
巻縮能を有する新規な巻縮繊維の製造方法であ
る。
潜在巻縮性1/ρ:延伸後の単繊維を160℃乾
熱で60秒間自由収縮熱処理した際に発現する螺旋
状巻縮10個当りの平均螺旋半径ρ(単位mm)の逆
数で定義する。
ここで熱化塑性合成繊維とは、溶融紡糸可能な
すでに公知の高分子より形成されるものであれば
いずれでも良いが、繊維としてのすぐれた特性を
考慮すればポリアミドおよびポリエステル系高分
子が好ましい。勿論、特殊な性能を付与するため
に共重合なりブレンド等により改質したものや、
添加剤等を付与したものであつてもよい。これら
溶融紡糸可能な高分子は通常公知の紡糸機により
紡糸口金から押し出され糸条を形成されるが重合
直接紡糸方法等の手段を用いるときさらに効果が
発揮される。
本発明で使用する紡糸口金は、通常一般に使用
されている円形(丸断面)紡糸孔を有するもので
はなく、中空繊維を製造することが可能な紡糸孔
を有するものである。かかる紡糸口金を使用する
理由は、紡出糸条を紡糸口金直下で冷却気流によ
つて糸条の横断面方向に非対称的に冷却すること
により、糸条に高度の潜在巻縮性能を付与するた
めである。かかる紡糸口金としては従来種々のも
のが提案されており、本発明でもそれら公知のも
のを使用することができる。その場合、中空繊維
を製造することが可能な紡糸孔としては繊維の中
空率(繊維横断面の中空部の面積/中空部を含む
繊維横断面全面積)が5〜40%、特に10〜35%と
なるようなものがよい。
そして、紡糸口金における紡糸孔の配列状態
は、各単繊維間にできるだけ斑を生じないよう考
虜されたものが望ましく、例えば本発明者等が先
に特願昭50−48813号および特願昭50−71078号で
提案したような口金を用いると良い。
紡糸口金より吐出された糸条は、紡糸口金直下
で冷却気流によつて糸条の横断面方向に非対称的
に冷却されて固化した後、紡糸口金と高速回転引
取ロール間に設置した加熱帯域を通過する際に延
伸される。この延伸は温度勾配下空気との摩擦力
によつて行なわれる。
紡出糸条の非対称冷却は既に公知であるが、本
発明のような3000m/min以上の高速紡糸の場合
には、糸条に対する冷却気流の吹当速度を強化す
ることが高度の潜在巻縮性能を付与する上で重要
であり、冷却気流の吹当速度は約0.5m/sec以
上、特に0.5〜2.5m/secとするのがよい。冷却
気流は熱経済的観点から通常室温の空気が使用さ
れる。冷却気流が糸条に当る上下方向の帯域長は
約20〜100cmであることが好ましい。
加熱帯域は製糸操業性、毛羽発生防止等の観点
より非接触の加熱装置で構成される。
そして非接触の加熱装置としては種々考えられ
るが、特に高温電気炉、高温ガス炉等が好まし
い。また加熱温度としては特に限定されないが、
延伸後の強伸度特性や1/ρを考慮して設定する
ことが肝要で、好ましくは1/ρが1.5以上で破
断伸度が70%以下、より好ましくは50%以下にな
るようにするのがよい。
また加熱帯域に入る糸条の速度が速い場合、糸
条に同伴する冷却気体(空気)の量が著しく増大
し、加熱帯域における糸条への伝熱効果が低下す
るため、同伴冷却気体を分離する分離装置を併設
することが好ましい。
本発明における潜在巻縮性1/ρは、溶融紡糸
されるポリマーの種類、単繊維のデニール、冷却
気流の温度および吹当速度、糸条の引取速度等に
よつて変化するが、機械巻縮を付与しなくても申
し分のない嵩高性を有する巻縮繊維を製造するた
めには、1/ρが1.5以上、特に2.0以上となるよ
うに上記変動因子を適宜選定する必要がある。
かくして潜在巻縮を付与され加熱延伸された糸
条は次いで必要に応じて油剤処理を行つた後高速
で回転する引取ロールにより少なくとも3000m/
min以上の速度で引取られるが、潜在巻縮性が引
取速度とともに増大することにより、好ましくは
この引取ロールによる引取速度は3500m/min以
上の高速とするのがよい。この引取ロールにより
引き取られた糸条は必要に応じて引き続き再延伸
および/または熱処理を行うことも可能である
が、好ましくはそのまま/または引続き潜在巻縮
を発現させるために高温処理を施した後、巻取機
で巻き取られフイラメントとして供されるか、ふ
り落し装置でふり落した後、短繊維に切断されて
又は切断後ふり落されてステープル用途に供され
る。短繊維に切断後ふり落される態様の中には、
切断装置が前記高速回転引取ロールとしての能力
を併有している場合も含まれる。
ウエブを製造する場合は、気体ジエツトにより
該繊維を吸引後適宜開繊してネツトコンベア等に
落す。既に公知のスパンボンド方式を用いる場
合、該繊維が有する室温弾性巻縮の効果とあいま
ち、非常に良好な巻縮ウエブを作成することが可
能であり、また必要に応じ引き続き熱処理を施す
ことも可能である。
本発明によつて製造される巻縮繊維は、紡糸口
金と高速回転引取ロール間に加熱帯域を設けない
で、潜在巻縮性繊維を高速紡糸する従来一般の高
速紡糸法による巻縮繊維にくらべ、同一紡糸速度
下では強伸度、初期ヤング率などの力学的性質並
びに嵩高性が優れており、特に初期ヤング率が大
きいために巻縮のへたりが少なく、長時間の使用
によつても嵩高性が低下しないという特長を有し
ており、実用性の極めて高いものである。
実施例 1
常法によつて製造した極限粘度0.62(フエノー
ル/テトラクロルエタン=6/4の混合溶媒中30
℃で測定)のポリエチレンテレフタレートを、内
径0.36mmφ、外径0.56mmφ、ブリツジ幅0.1mmのC
形スリツトのノズルオリフイスを30個有する紡糸
口金より溶融紡出し、紡糸口金直下で室温の冷却
気流を糸条の片側より糸条に直交して吹きあてて
一旦冷却し、次いで電気ヒーターで加熱した加熱
筒内を通過させて延伸し、油剤付与後、高速度で
回転する引取ロールで引き取つた後高速度カツタ
ーで長さ70mmのステープルに切断して巻縮繊維を
製造した。得られた繊維の中空率は約25%であつ
た。
本例における製糸条件、潜在巻縮性および得ら
れた巻縮繊維の性質を第1表に示した。
なお比較のために、孔径0.3mmφの円形紡糸孔
を24個有する紡糸口金を使用し、その他はすべて
本例と同一条件で製造して得た巻縮繊維の性能を
第1表に併記した。
対照例 1
電気ヒーターのような加熱体を使用しなかつた
以外は実施例1の実験No.2と同一の条件で製造し
て得た巻縮繊維の糸質は、次の通りであつた。潜
在巻縮性1/ρ=0.9mm-1、単糸デニール=
2.5d、初期ヤング率=24g/d、強度=2.1g/
d、破断伸度=69%、巻縮数CN=8個/イン
チ、巻縮率CI=13%。この結果も第1表に併記
した。
(Industrial Application Field) The present invention relates to a novel method for producing crimped fibers, and particularly provides a novel method for producing crimped synthetic fibers by a melt spinning method. (Prior art) Regarding the manufacturing method of crimped fibers made of thermoplastic synthetic polymers, studies have been actively conducted on continuous spinning, drawing, and crimping for the purpose of reducing production costs and improving productivity. It is being said. However, when the spinning speed is around 1000 m/min, it is necessary to increase the draw ratio several times, and the crimp application speed is unavoidable.
3,000 to 4,000 m/min, and as it is currently not possible to provide satisfactory crimp, the spinning speed is actually reduced to 1,000 m/min.
I had to set it much lower than m/min,
In the end, it was not possible to achieve the intended purpose. In view of the current situation, the inventors of the present invention have conducted intensive studies on high-speed crimp application methods, and have found that with the current level of technology, it is difficult to apply sufficient crimp with a mechanical crimp application device alone, and some kind of auxiliary means is required. For example, even if it were possible to provide sufficient crimp mechanically, the equipment would be extremely expensive, leading to the idea that this would be impractical. (Problems to be Solved by the Invention) The present invention provides a means for producing crimped thermoplastic synthetic fibers having excellent mechanical properties such as strength and elongation and initial Young's modulus, as well as bulkiness, using simplified equipment. The aim is to provide a new method for producing silk at a high speed of 3000 m/min or more with good operability. (Means for Solving the Problems) That is, the present invention provides thermoplastic synthetic fibers that have been melt-spun and then cooled immediately below the spinneret, and are spun together with the spinneret at high speed rotation at a surface circumferential speed of 3000 m/min or more. A process for producing synthetic fibers in which hollow fibers are drawn by passing through a heating zone between take-off rolls and then, if necessary, re-drawn and/or heat treated before being taken off or cut continuously. By using a spinning hole that can be manufactured, configuring the heating zone with a non-contact heating device, and cooling the yarn asymmetrically in the cross-sectional direction directly below the spinneret, the following can be achieved. This is a method for producing a novel crimped fiber having a crimping ability such that the defined potential crimping property 1/ρ is at least 1.5. Latent crimpability 1/ρ: Defined as the reciprocal of the average helical radius ρ (unit: mm) per 10 spiral crimps that occurs when the stretched single fiber is subjected to free shrink heat treatment at 160°C for 60 seconds. . Here, the thermoplastic synthetic fibers may be any fibers made from known polymers that can be melt-spun, but polyamide and polyester polymers are preferred in view of their excellent properties as fibers. . Of course, there are those modified by copolymerization or blending to give special performance,
It may be added with additives or the like. These melt-spun polymers are usually extruded from a spinneret using a known spinning machine to form yarns, but even more effects are exhibited when means such as a direct polymerization spinning method are used. The spinneret used in the present invention does not have a generally used circular (round cross-section) spinning hole, but has a spinning hole that can produce hollow fibers. The reason for using such a spinneret is that the spun yarn is cooled asymmetrically in the cross-sectional direction of the yarn by a cooling air flow directly under the spinneret, thereby imparting a high degree of latent crimp performance to the yarn. It's for a reason. Various types of spinnerets have been proposed in the past, and these known spinnerets can be used in the present invention. In that case, the spinning hole capable of producing hollow fibers should have a fiber hollowness ratio (area of the hollow part of the cross section of the fiber/total area of the cross section of the fiber including the hollow part) of 5 to 40%, especially 10 to 35%. % is better. It is desirable that the arrangement of the spinning holes in the spinneret be carefully considered to avoid unevenness between each single fiber as much as possible. It is best to use a cap like the one suggested in No. 50-71078. The yarn discharged from the spinneret is cooled and solidified asymmetrically in the cross-sectional direction of the yarn by a cooling air flow directly below the spinneret, and then passed through a heating zone installed between the spinneret and a high-speed rotating take-up roll. It is stretched as it passes through. This stretching is performed by frictional force with air under a temperature gradient. Asymmetric cooling of spun yarn is already known, but in the case of high-speed spinning of 3000 m/min or more as in the present invention, it is necessary to increase the blowing speed of the cooling air flow to the yarn to prevent a high degree of latent crimp. This is important in imparting performance, and the blowing speed of the cooling air stream is preferably about 0.5 m/sec or more, particularly 0.5 to 2.5 m/sec. Room temperature air is usually used as the cooling air stream from a thermoeconomic standpoint. The length of the zone in the vertical direction in which the cooling airflow hits the yarn is preferably about 20 to 100 cm. The heating zone is configured with a non-contact heating device from the viewpoint of silk reeling operability and prevention of fuzz generation. Various types of non-contact heating devices are possible, but high-temperature electric furnaces, high-temperature gas furnaces, etc. are particularly preferred. Also, the heating temperature is not particularly limited, but
It is important to set the strength and elongation characteristics after stretching and 1/ρ, preferably 1/ρ is 1.5 or more and the elongation at break is 70% or less, more preferably 50% or less. It is better. In addition, when the speed of the yarn entering the heating zone is high, the amount of cooling gas (air) accompanying the yarn increases significantly and the heat transfer effect to the yarn in the heating zone decreases, so the entrained cooling gas is separated. It is preferable to provide a separation device for this purpose. The potential crimpability 1/ρ in the present invention varies depending on the type of polymer to be melt-spun, the denier of the single fiber, the temperature and blowing speed of the cooling air stream, the take-up speed of the yarn, etc. In order to produce crimped fibers that have satisfactory bulk even without imparting , it is necessary to appropriately select the above-mentioned variable factors so that 1/ρ is 1.5 or more, particularly 2.0 or more. The heated and drawn yarn with latent crimp is then treated with an oil agent if necessary, and then stretched for at least 3000 m/s by a take-up roll rotating at high speed.
The material is taken off at a speed of 3500 m/min or more, but since the latent crimpability increases with the taking speed, it is preferable that the take-up speed by the take-off roll is 3500 m/min or more. The yarn taken up by this take-up roll can be subsequently re-stretched and/or heat-treated as necessary, but preferably it is treated as is or after being subjected to high-temperature treatment in order to develop latent crimp. The filament is wound up with a winding machine and used as a filament, or after being shaken off with a shake-off device, it is cut into short fibers, or after being cut and shaken off, it is used as a staple. Some of the ways in which short fibers are shaken off after being cut are as follows:
This also includes a case where the cutting device also has the capability of functioning as the above-mentioned high-speed rotation take-up roll. When producing a web, the fibers are sucked with a gas jet, opened as appropriate, and dropped onto a net conveyor or the like. When using the already known spunbond method, it is possible to create a very good crimped web due to the room temperature elastic crimping effect of the fibers, and it is also possible to perform subsequent heat treatment if necessary. It is. The crimped fibers produced by the present invention are superior to crimped fibers produced by the conventional high-speed spinning method in which latent crimpable fibers are spun at high speed without providing a heating zone between the spinneret and the high-speed rotation take-up roll. Under the same spinning speed, it has excellent mechanical properties such as strength and elongation, initial Young's modulus, and bulkiness.In particular, because the initial Young's modulus is high, there is little crimping set, and even after long-term use. It has the feature that bulkiness does not decrease, and is extremely practical. Example 1 A product with an intrinsic viscosity of 0.62 (in a mixed solvent of phenol/tetrachloroethane = 6/4) manufactured by a conventional method.
C) with an inner diameter of 0.36 mmφ, an outer diameter of 0.56 mmφ, and a bridge width of 0.1 mm.
The yarn is melt-spun from a spinneret with 30 shaped slit nozzle orifices, cooled by blowing a cooling air stream at room temperature directly below the spinneret from one side of the yarn perpendicular to the yarn, and then heated by an electric heater. After applying an oil agent, the fibers were taken up with a take-up roll rotating at high speed, and then cut into staples of 70 mm in length with a high-speed cutter to produce crimped fibers. The hollowness ratio of the obtained fiber was about 25%. Table 1 shows the spinning conditions, latent crimpability, and properties of the resulting crimped fibers in this example. For comparison, Table 1 also shows the performance of crimped fibers obtained by using a spinneret having 24 circular spinning holes with a hole diameter of 0.3 mmφ and otherwise producing under the same conditions as in this example. Control Example 1 The yarn quality of the crimped fiber produced under the same conditions as Experiment No. 2 of Example 1 except that no heating element such as an electric heater was used was as follows. Potential crimpability 1/ρ = 0.9mm -1 , single yarn denier =
2.5d, initial Young's modulus = 24g/d, strength = 2.1g/
d, elongation at break = 69%, number of crimp CN = 8/inch, crimp ratio CI = 13%. These results are also listed in Table 1.
【表】【table】
【表】
第1表に示すように本発明によつて得られた中
空繊維の場合(実験No.1〜3)は潜在巻縮性
(1/ρ)が高く熱処理することにより良好な巻
縮が発現したが、比較例の中実繊維の場合(実験
No.4〜8)は潜在巻縮性が低く、冷却気流吹付速
度を上げても糸切れが発生しない領域で1/ρ≧
1.5となることはなかつた。また対照例1の場合
は、巻縮糸の強伸度、ヤング率等の機械的性質が
劣り、巻縮性能も本発明に比べ劣つている。
(発明の効果)
本発明によれば、強伸度、初期ヤング率などの
力学的性質並びに嵩高性に優れた熱可塑性合成繊
維の巻縮繊維を、設備的に簡略化された手段によ
り製糸操業性良く3000m/min以上の高速度で製
造することができる。[Table] As shown in Table 1, the hollow fibers obtained by the present invention (Experiments Nos. 1 to 3) have a high potential crimpability (1/ρ) and can be easily crimped by heat treatment. However, in the case of the solid fiber of the comparative example (experimental
Nos. 4 to 8) have low latent crimp properties, and are in the region where yarn breakage does not occur even if the cooling air blowing speed is increased, with 1/ρ≧
It never reached 1.5. Furthermore, in the case of Comparative Example 1, the mechanical properties such as strength and elongation of the crimped yarn and Young's modulus are inferior, and the crimping performance is also inferior to that of the present invention. (Effects of the Invention) According to the present invention, crimped fibers made of thermoplastic synthetic fibers having excellent mechanical properties such as strength and elongation and initial Young's modulus, as well as bulkiness, can be produced in silk-spinning operations using simplified equipment. It has good performance and can be manufactured at high speeds of 3000m/min or more.
Claims (1)
塑性合成繊維を、紡糸口金と表面周速度を3000
m/min以上となした高速回転引取ロール間で加
熱帯域を通過させて延伸し、次いで必要に応じて
再延伸および/または熱処理を行つた後、連続的
に引き取るかまたは切断する合成繊維の製造法に
おいて、紡糸口金として中空繊維を製造すること
が可能な紡糸孔を有するものを使用し、また加熱
帯域を非接触の加熱装置で構成し、かつ紡糸口金
直下で糸条を横断面方向に非対称的に冷却するこ
とにより、下記に定義する潜在巻縮性1/ρが少
なくとも1.5以上となるような巻縮能を有する新
規な巻縮繊維の製造方法。 潜在巻縮性1/ρ:延伸後の単繊維を160℃乾
熱で60秒間自由収縮熱処理した際に発現する螺旋
状巻縮10個当りの平均螺旋半径ρ(単位mm)の逆
数で定義する。[Claims] 1. After melt spinning, thermoplastic synthetic fibers are cooled immediately below the spinneret, and the surface circumferential speed is set to 3000.
Manufacture of synthetic fibers by stretching by passing through a heating zone between high-speed rotating take-off rolls at m/min or more, then re-stretching and/or heat treatment as necessary, and then continuously taking off or cutting. In the method, a spinneret with a spinning hole capable of producing hollow fibers is used, the heating zone is configured with a non-contact heating device, and the yarn is asymmetrically shaped in the cross-sectional direction directly under the spinneret. A method for producing a novel crimped fiber having a crimping ability such that a latent crimping property 1/ρ defined below becomes at least 1.5 by cooling the fiber. Latent crimpability 1/ρ: Defined as the reciprocal of the average helical radius ρ (unit: mm) per 10 spiral crimps that occurs when the stretched single fiber is subjected to free shrink heat treatment at 160°C for 60 seconds. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10399380A JPS5637308A (en) | 1980-07-28 | 1980-07-28 | Production of novel type crimped yarn |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10399380A JPS5637308A (en) | 1980-07-28 | 1980-07-28 | Production of novel type crimped yarn |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12857275A Division JPS5253027A (en) | 1975-10-24 | 1975-10-24 | Preparation of novel crimped yarn |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5637308A JPS5637308A (en) | 1981-04-11 |
| JPS6223082B2 true JPS6223082B2 (en) | 1987-05-21 |
Family
ID=14368814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10399380A Granted JPS5637308A (en) | 1980-07-28 | 1980-07-28 | Production of novel type crimped yarn |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5637308A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5540553B2 (en) * | 1973-05-15 | 1980-10-18 | ||
| JPS5253027A (en) * | 1975-10-24 | 1977-04-28 | Toyobo Co Ltd | Preparation of novel crimped yarn |
-
1980
- 1980-07-28 JP JP10399380A patent/JPS5637308A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5637308A (en) | 1981-04-11 |
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