JPH0819565B2 - Method for producing fine denier polyester fiber - Google Patents
Method for producing fine denier polyester fiberInfo
- Publication number
- JPH0819565B2 JPH0819565B2 JP60034540A JP3454085A JPH0819565B2 JP H0819565 B2 JPH0819565 B2 JP H0819565B2 JP 60034540 A JP60034540 A JP 60034540A JP 3454085 A JP3454085 A JP 3454085A JP H0819565 B2 JPH0819565 B2 JP H0819565B2
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- polyester fiber
- fine denier
- stress
- heating zone
- 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 - Lifetime
Links
- 239000000835 fiber Substances 0.000 title claims description 36
- 229920000728 polyester Polymers 0.000 title claims description 32
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 40
- 230000009477 glass transition Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 description 21
- 239000002759 woven fabric Substances 0.000 description 16
- 239000004744 fabric Substances 0.000 description 11
- 238000009987 spinning Methods 0.000 description 10
- 230000000704 physical effect Effects 0.000 description 6
- 230000007547 defect Effects 0.000 description 5
- 238000012360 testing method Methods 0.000 description 3
- 206010040954 Skin wrinkling Diseases 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 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 description 1
- 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 description 1
- -1 Polyethylene terephthalate Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000011077 uniformity evaluation Methods 0.000 description 1
Landscapes
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
Description
【発明の詳細な説明】 <技術分野> 本発明は、単糸間の斑が大巾に改善され、織成したと
きには強撚織物として良好な品位を有するフアインデニ
ールポリエステル繊維に関するものである。Description: TECHNICAL FIELD The present invention relates to a fine denier polyester fiber in which unevenness between single yarns is greatly improved and, when woven, has a good quality as a strongly twisted woven fabric.
<従来技術とその問題点> 単糸デニールが1.4d以下、フイラメント数が36以上の
フアインデニールポリエステル繊維は、近年ポリエステ
ル繊維の衣料用分野でその需要が拡大し、特に強撚シボ
織物用原糸として広く利用されている。<Prior art and its problems> Huain denier polyester fiber having a single yarn denier of 1.4d or less and a filament number of 36 or more has recently been in growing demand in the field of polyester fiber garment, and particularly for raw twisted textured fabrics. Widely used as thread.
このようなフアインデニールポリエステル繊維は、一
般に低配向の未延伸糸を製造した後、別工程で延伸する
ことにより得られている。しかし、その方法では、糸が
集束された状態で加熱延伸される際、フアインデニール
糸のようにフイラメント数が多くなると、各単糸に加わ
る熱が不均一となり、単糸間の糸斑が増大する。この傾
向は、フアインデニール糸においては糸が細いため熱に
対する感受性が高くなるので、さらに増長されている。
この延伸糸は、糸条を構成する各単糸のS−S曲線を測
定した際の5%伸長時の応力バラツキ(CV%)が10%以
上となることで特徴づけられるように、単糸間の均一性
に問題があり、しばしば織物としての風合を悪化させた
り、染色斑により織物品位が低下したりするというよう
な問題を起こしている。さらに、このように単糸間斑の
大きい糸は、織成して強撚織物とするとトルク斑が発現
し、品位が低下する。従つて、従来の未延伸糸紡糸−延
伸法では、十分に均一性が満足され得ず、品位良好な強
撚織物用原糸としてのフアインデニールポリエステル繊
維は得られていない。Such a fine denier polyester fiber is generally obtained by producing a low orientation undrawn yarn and then drawing it in a separate step. However, in that method, when the filaments are heated and drawn in a bundled state and the number of filaments is large like the fine denier yarn, the heat applied to each single yarn becomes non-uniform, and the yarn unevenness between the single yarns increases. To do. This tendency is further increased in fine denier yarns because the yarns are finer and more sensitive to heat.
This drawn yarn is characterized by a stress variation (CV%) of 10% or more at 5% elongation when the S-S curve of each single yarn constituting the yarn is measured. There is a problem in the uniformity of the woven fabric, which often causes problems such as deterioration of the texture of the woven fabric and deterioration of the woven fabric quality due to uneven dyeing. Further, when such a yarn having a large single-yarn unevenness is woven into a strongly twisted woven fabric, torque unevenness is developed and the quality is degraded. Therefore, in the conventional undrawn yarn spinning-drawing method, the homogeneity cannot be sufficiently satisfied, and a fine denier polyester fiber as a raw yarn for a strong twist woven fabric with good quality has not been obtained.
未延伸糸紡糸−延伸法以外でフアインデニール糸を得
る方法としては、例えば特開昭55−93816号公報などに
記載されている高速紡糸による方法がある。しかし、こ
のような高速紡糸法では紡糸糸切れが増加し、安定に生
産できないばかりでなく、得られる糸の機械的性質、特
に降伏点応力が低いという問題点を有し、高次加工の際
に種々の問題が発生する。As a method for obtaining a fine denier yarn other than the undrawn yarn spinning-drawing method, for example, there is a method by high-speed spinning described in JP-A-55-93816. However, such a high-speed spinning method has a problem that the yarn breakage increases, stable production is not possible, and the mechanical properties of the obtained yarn, in particular, the yield point stress is low. Various problems occur.
また、別の方法として、特開昭56−4715号公報に溶融
紡糸した糸条をいつたんガラス転移温度以下まで冷却し
た後、再び加熱帯域中を通過せしめ熱延伸し、染色性良
好なフアインデニール糸を得る例が開示されている。Further, as another method, in JP-A-56-4715, the melt-spun yarn is cooled to a temperature below the glass transition temperature, then again passed through a heating zone and hot-drawn to obtain a fine dye having good dyeability. An example of obtaining a denier yarn is disclosed.
しかし、このような延伸方法では、加熱帯域中で糸に
加わる熱と張力(紡糸張力)とを十分に制御しないと、
均一な延伸を行ない得ない。すなわち、特開昭56−4715
号公報に開示されているフアインデニール繊維も、十分
な均一性、特に単糸間斑が満足できるレベルには至つて
いないのが現状である。However, in such a drawing method, unless heat and tension (spinning tension) applied to the yarn in the heating zone are sufficiently controlled,
Uniform stretching cannot be performed. That is, JP-A-56-4715
In the present situation, the fine denier fiber disclosed in Japanese Patent Publication has not reached a level where sufficient homogeneity, in particular, single-yarn unevenness is satisfactory.
<発明の目的> 本発明の目的は、単糸間の斑が減少し、かつ、高次工
程通過性が良好な機械的性質および良好な風合を有する
品位の高い織物、特に強撚用途で高品位の織物の原糸と
なり得る、新規なフアインデニールポリエステル繊維を
提供することにある。<Objects of the Invention> An object of the present invention is to reduce the unevenness between single yarns and to provide high-quality woven fabrics having good mechanical properties and good handability in high-order processability, especially in strong twist applications. It is an object of the present invention to provide a novel fine denier polyester fiber which can be used as a raw yarn for a high-quality woven fabric.
<発明の構成> 本発明は、単糸デニールが1.4d以下、フィラメント数
が36以上のファインデニールポリエステル繊維を製造す
るに際して、溶融紡糸したポリエステル繊維を一旦ガラ
ス転移温度以下まで冷却した後、口金から0.8〜2.0mに
設置した入口と内部の断面積の比が4以上である加熱帯
域に該糸条を導入し、該加熱帯域中で該糸条の周囲から
加熱気体を導入して熱延伸し、給油し、5000m/分以上で
引取ることを特徴とするファインデニールポリエステル
繊維の製造方法である。<Structure of the Invention> In the present invention, when a fine denier polyester fiber having a single yarn denier of 1.4d or less and a filament number of 36 or more is produced, the melt-spun polyester fiber is once cooled to a glass transition temperature or lower and then from a spinneret. The yarn is introduced into a heating zone having a cross-sectional area ratio between the inlet and the interior of 0.8 to 2.0 m of 4 or more, and heated gas is introduced from the periphery of the yarn in the heating zone to perform hot drawing. A method for producing a fine denier polyester fiber, which comprises refueling and collecting at 5000 m / min or more.
以下、本発明について更に詳細に説明する。 Hereinafter, the present invention will be described in more detail.
本発明におけるポリエステルとは、エチレンテレフタ
レートを主たる繰り返し単位とするポリエステルを主に
対象とするが、ブチレンテレフタレートを繰り返し単位
とするポリエステルであつても良い。また、15モル%以
下の量で他の成分を一種以上共重合したポリエステル、
または少量の添加剤を含有したポリエステルであつても
良い。The polyester in the present invention is mainly a polyester having ethylene terephthalate as a main repeating unit, but may be a polyester having butylene terephthalate as a repeating unit. Also, a polyester obtained by copolymerizing one or more other components in an amount of 15 mol% or less,
Alternatively, it may be polyester containing a small amount of additives.
また、フアインデニールポリエステル繊維とは、糸条
を構成する単糸のデニールが1.4d以下かつフイラメント
数が36以上の繊維をいう。さらに、単糸デニールが1.1d
以下、フイラメント数が48以上であると、特にその効果
が著しい。また断面形状については特に限定はなく、円
・三角など種々の断面を対象とする。Further, the fine denier polyester fiber means a fiber having a denier of 1.4d or less and a filament number of 36 or more as a single yarn constituting a yarn. In addition, single yarn denier is 1.1d
Below, the effect is particularly remarkable when the number of filaments is 48 or more. The cross-sectional shape is not particularly limited, and various cross-sections such as circles and triangles are targeted.
フアインデニールポリエステル繊維が、良好な織物品
位を与え、強撚用途に展開した時に良好な特性を与える
得るためには、糸条を構成する単糸一本一本の均一性が
重要である。この単糸間の均一性が悪く、糸条を構成す
る各単糸間の機械的性質や熱セツト性などに単糸間差が
大きいと、織物とした時にタテスジ,ヨコスジが発生し
たり、風合斑を生じたり、染め斑欠点が発生したりする
のに加え、強撚織物のシボ質、品位低下を招く。単糸間
の均一性を評価するためには、従来からよく用いられて
いる繊維軸方向の巨視的な均一性評価手段(例えば、ウ
スター斑、ストレツチテンシヨンなど)では不完全であ
り、各単糸各々の物性バラツキをミクロに調べる必要が
ある。本発明者らの知見によれば、単糸間の物性バラツ
キを的確に調べる評価手段としては、繊維を構成する各
単糸のS−S曲線の5%伸長時の応力バラツキ(CV%)
が最も有効であり、この応力バラツキをあるレベル以下
に制御して初めてフアインデニールポリエステル繊維の
織物品位向上、強撚特性の向上が図れることがわかつ
た。すなわち、この応力バラツキ以外の物性値では、フ
アインデニールポリエステル繊維の織物品位の均一性や
強撚織物としての特徴は明確に評価できないのである。In order for the fine denier polyester fiber to give good woven quality and good properties when developed in a strong twist application, the uniformity of each single yarn constituting the yarn is important. If the uniformity between the single yarns is poor, and if there is a large difference between the single yarns that make up the yarn in terms of mechanical properties and heat-setting properties, there will be vertical streaks and weft stripes when the fabric is made, and wind In addition to the occurrence of spots and defects of dyeing spots, the texture of the strongly twisted woven fabric is deteriorated and the quality is deteriorated. In order to evaluate the uniformity between single yarns, macroscopic uniformity evaluation means in the fiber axis direction (for example, Worcester spots, stretch tension, etc.) that have been conventionally used are incomplete. It is necessary to microscopically check the variation in the physical properties of each single yarn. According to the knowledge of the present inventors, as an evaluation means for accurately examining the variation in physical properties between single yarns, stress variation (CV%) at 5% elongation of the SS curve of each single yarn constituting the fiber
Was most effective, and it was found that the fabric quality of the fine denier polyester fiber and the high twisting property can be improved only by controlling the stress variation below a certain level. In other words, the physical property values other than the stress variation cannot clearly evaluate the uniformity of the fabric quality of the fine denier polyester fiber and the characteristics of the strongly twisted fabric.
本発明者らの知見によると、上述の繊維を構成する各
単糸のS−S曲線の5%伸長時の応力バラツキ(CV%)
が7%以下であることが、強撚用途としての織物品位を
高め、かつ種々織物欠点を無くすための必須の要件であ
る。なお、好ましくは、5%以下がよい。According to the knowledge of the present inventors, the stress variation (CV%) at the time of 5% elongation of the SS curve of each single yarn constituting the above fiber.
Is 7% or less, which is an essential requirement for improving the fabric quality for strong twist applications and eliminating various fabric defects. In addition, 5% or less is preferable.
本発明のフアインデニールポリエステル繊維は、高次
工程の通過性などから降伏点応力が2g/d以上である必要
がある。降伏点応力が2g/d未満であると、製織時に糸が
伸び、織物品位が低下する。The fine denier polyester fiber of the present invention is required to have a yield stress of 2 g / d or more in view of the passability in high-order processes. If the stress at yield point is less than 2 g / d, the yarn will be stretched during weaving and the fabric quality will be degraded.
さらに、本発明では、ポリエステル繊維の伸度は30%
以上である必要がある。伸度が30%未満であると紡糸時
の毛羽が増加するし製織時の糸切れも増加する。Furthermore, in the present invention, the elongation of the polyester fiber is 30%.
It must be above. When the elongation is less than 30%, the fluff during spinning increases and the yarn breakage during weaving also increases.
さらに本発明のフアインデニールポリエステル繊維
は、先に述べた特開昭55−93816号公報などに開示され
ている高速紡糸法による糸とは明らかに内部構造が異な
る。内部構造の差を表わす性質として、本発明のフアイ
ンデニールポリエステル繊維は、糸を昇温しながら測定
した収縮応力のピーク値を示す温度が130℃以上にある
ことで上記高速紡糸法による糸とは区別される。高速紡
糸の糸は、収縮応力のピーク値を示す温度が130℃未満
であり、強撚用途でのシボ発現能力が本発明のポリエス
テル繊維に比べ大変に劣るものである。Further, the fine denier polyester fiber of the present invention has an apparently different internal structure from the yarn produced by the high-speed spinning method disclosed in the above-mentioned JP-A-55-93816. As a property showing the difference in internal structure, the fine denier polyester fiber of the present invention has a temperature showing a peak value of shrinkage stress measured while heating the yarn at a temperature of 130 ° C. or higher, and thus the yarn is obtained by the high-speed spinning method. Are distinguished. The high speed spun yarn has a temperature at which the peak value of shrinkage stress is less than 130 ° C., and is very inferior to the polyester fiber of the present invention in the wrinkle development ability in the strong twist application.
本発明のポリエステル繊維の製造方法の必須の第1要
件は、溶融紡糸したポリエステル繊維をいったん、ガラ
ス転移温度以下まで冷却した後、再び加熱帯域に導入
し、加熱帯域中で熱延伸し給油して引取ることである。
この方法によりはじめて、各単糸を集束せず、各々の単
糸に均一に熱を加えながら延伸することができ、延伸時
に単糸が集束している従来の延伸方法では、加えられた
熱が全単糸に均一に伝わらず単糸間斑が出て、本発明の
糸は得られない。本発明のような均一性良好なフアイン
デニール糸を得るためには、加熱帯域内での延伸に関与
するいくつかの条件を厳格にコントロールする必要があ
り、従来公知の加熱帯域中での延伸方法では本発明の糸
は得られない。The essential first requirement of the method for producing a polyester fiber of the present invention is that once melt-spun polyester fiber is cooled to a glass transition temperature or lower, it is again introduced into a heating zone, and hot drawing is performed in the heating zone to supply oil. It is to take over.
Only by this method, it is possible to draw each single yarn while uniformly applying heat to each single yarn without bundling, and in the conventional drawing method in which the single yarns are bundled at the time of drawing, the applied heat is The yarns of the present invention cannot be obtained because they are not evenly distributed to all the single yarns, resulting in single yarn unevenness. In order to obtain a fine denier yarn having good uniformity as in the present invention, it is necessary to strictly control some conditions involved in the drawing in the heating zone, and the drawing in the conventionally known heating zone is necessary. The method does not yield the yarn of the invention.
本発明の製造方法の第2の要件は引取速度であり、引
取速度を5000m/分以上とすることである。5000m/分に満
たない場合、各単糸のS−S曲線の5%伸長時の応力バ
ラツキ(CV%)が7%を越え、強撚織物のシボ質が不良
となる。第3の要件は加熱帯域の形態であり、加熱帯域
の入口(好ましくは出入口)と内部の断面積の比が4以
上、好ましくは10以上225以下である。この断面積の比
が4に満たない場合には、各単糸のS−S曲線の5%伸
長時の応力バラツキ(CV%)が7%を越えてしまう。第
4の要件は、加熱帯域を、その入口が口金からの距離で
0.8mに満たない場合には降伏点応力が2g/dを下回ってし
まい、2mを越えると伸度が30%をきる糸質になってしま
う。本発明では以上の4つの条件とすることにより、は
じめて本発明のような単糸間の均質性が良好で、かつ伸
度30%以上、降伏点応力2g/d以上の糸条を安定して製造
できるのである。なお、上記本発明の製造方法において
は更に加熱帯域中で糸の周囲から加熱気体を導入する必
要があり、その流量は10〜80N1/分・糸条にコントロー
ルことが好ましい。また、本発明の繊維を得るための加
熱帯域は、糸条が走行する空間が加熱されておれば良
く、特に限定はしないが、例えば筒状または横断面が矩
形状のチユーブなどを用いることが出来る。加熱帯域の
雰囲気を高温化させる手段としては、加熱帯域の周囲を
電熱又は熱媒加熱する方法が一般的であるが、これに限
られない。加熱帯域の雰囲気温度は100℃〜200℃が好ま
しく、長さは1〜2mが好ましい。The second requirement of the manufacturing method of the present invention is the take-up speed, and the take-up speed is 5000 m / min or more. If it is less than 5000 m / min, the stress variation (CV%) at 5% elongation of the SS curve of each single yarn exceeds 7%, and the texture of the strong twist woven fabric becomes poor. The third requirement is the form of the heating zone, and the ratio of the cross-sectional area between the inlet (preferably the outlet) of the heating zone and the inside is 4 or more, preferably 10 or more and 225 or less. If the ratio of the cross-sectional areas is less than 4, the stress variation (CV%) at 5% elongation of the SS curve of each single yarn exceeds 7%. The fourth requirement is that the heating zone be the distance of its inlet from the base.
If it is less than 0.8 m, the stress at yield point will be less than 2 g / d, and if it exceeds 2 m, the elongation will be less than 30%. In the present invention, by setting the above four conditions, the homogeneity among the single yarns as in the present invention is first achieved, and the yarn having the elongation of 30% or more and the yield point stress of 2 g / d or more is stabilized. It can be manufactured. In the production method of the present invention, it is necessary to further introduce heated gas from around the yarn in the heating zone, and the flow rate thereof is preferably controlled to 10 to 80 N1 / min. Yarn. The heating zone for obtaining the fiber of the present invention is not particularly limited as long as the space in which the yarn runs is heated, but for example, a tube or a tube having a rectangular cross section is used. I can. As a means for increasing the temperature of the atmosphere in the heating zone, a method of electrically heating or heating a heating medium around the heating zone is generally used, but is not limited thereto. The atmosphere temperature in the heating zone is preferably 100 ° C to 200 ° C, and the length is preferably 1 to 2 m.
本発明では加熱帯域に加熱気体を導入するのである
が、加熱気体の導入は、走行する糸条の周囲から均一に
低流速で吹き出させることが好ましく、例えば金属繊維
の不織布や整流用フイルター、ポーラスメタルなどを通
して導入することが好ましい。加熱気体の温度は80℃以
上であれば良いが、特に100〜300℃が好ましい。さら
に、加熱気体の導入は加熱帯域の上部で糸条の走行方向
に対しほぼ直行する様に実施し、次いで糸の走行方向に
沿つて加熱気体を走らせることが糸条の均一性を高める
上で効果的であり好ましい。In the present invention, the heating gas is introduced into the heating zone, but the introduction of the heating gas is preferably blown out uniformly around the running yarn at a low flow rate. For example, a nonwoven fabric of metal fibers, a rectifying filter, or a porous material. It is preferable to introduce it through metal or the like. The temperature of the heated gas may be 80 ° C or higher, but 100 to 300 ° C is particularly preferable. Furthermore, the introduction of the heated gas is performed in the upper part of the heating zone so as to be substantially orthogonal to the running direction of the yarn, and then the heated gas is run along the running direction of the yarn in order to improve the uniformity of the yarn. Is effective and preferable.
なお前述のように、従来の未延伸糸紡糸−延伸法のフ
アインデニール糸や、特開昭56−4715号公報に開示され
ている紡糸工程中の加熱帯域による延伸法によるフアイ
ンデニール糸は、本発明で規定する繊維を構成する単糸
のS−S曲線の5%伸長時の応力のバラツキ(CV%)が
9〜10%以上あり、本発明には及ばない。As described above, the conventional undrawn yarn spinning-drawing fine denier yarns and the fine denier yarns drawn by the heating zone during the spinning process disclosed in JP-A-56-4715 are The variation in stress (CV%) at 5% elongation of the S-S curve of the single yarn constituting the fiber defined in the present invention is 9 to 10% or more, which does not reach the present invention.
これは従来の未延伸糸の延伸法ではフアインデニール
糸の様にフイラメント数が増加して来ると、加熱延伸時
に各単糸が重なり合つてしまい単糸間に温度差が生じ、
延伸点が各単糸間で異なるためと考えられる。This is because in the conventional drawing method of undrawn yarn, when the number of filaments increases like a fine denier yarn, the individual yarns overlap each other during heating and drawing, resulting in a temperature difference between the single yarns.
It is considered that the drawing points are different among the single yarns.
特開昭56−4715号公報に開示されている紡糸工程中で
の延伸法においてはローラ間で単糸各々が把持されてい
ないため、少しでも単糸間に昇温挙動の差があれが必然
的に延伸挙動の差となり、単に加熱帯域を設けただけで
は均一性に優れたフアインデニールマルチフイラメント
糸が得られないためである。In the drawing method in the spinning process disclosed in Japanese Patent Application Laid-Open No. 56-4715, since each single yarn is not gripped between the rollers, it is inevitable that there is a difference in temperature rising behavior between the single yarns. This is because there is a difference in the drawing behavior, and a fine denier multifilament yarn excellent in uniformity cannot be obtained simply by providing a heating zone.
すなわち、前述した方法によつてマルチフイラメント
を構成する各単糸を実質的に等しい位置で同じ温度に昇
温させ、等しい張力を加えて延伸することによつて各単
糸が等しい物性値をもつ様に調節され、そのことによつ
て、初めて均一な糸が得られるのである。このような特
徴を有する糸を正しく把握するためには、前述の応力バ
ラツキ(CV%)を用いることが重要であり、これを7%
以下に制御することで、本発明の目的が達せられるので
ある。That is, the single yarns constituting the multifilament are heated to the same temperature at substantially the same position by the above-mentioned method, and the single yarns have the same physical property value by applying the same tension. This is the only way that a uniform yarn can be obtained. It is important to use the above-mentioned stress variation (CV%) in order to correctly grasp the yarn having such characteristics.
The object of the present invention can be achieved by controlling the following.
<発明の効果> 以上説明したように、本発明のフアインデニールポリ
エステル繊維は単糸間の糸斑が著く小さく制御された均
一性良好な繊維であり、かつ良好な機械的性質を有し、
以下のような利点を有する。<Effects of the Invention> As described above, the fine denier polyester fiber of the present invention is a fiber in which unevenness between single yarns is significantly small and controlled to have good uniformity, and has good mechanical properties.
It has the following advantages.
1. 紡糸時に毛羽・糸切れもなく安定して、しかも低コ
ストでの生産が可能である。1. Stable with no fluff or yarn breakage during spinning, and low-cost production is possible.
2. 良好な高次工程通過性を有し品位の高い織編物の製
造が可能である。2. It is possible to manufacture high-quality woven and knitted products with good high-order process passing properties.
3. 強撚シボ織物として使用すると良好なシボ質を有し
品位の高い強撚織物が得られる。3. When used as a strong twist textured fabric, a high quality strong twist textured fabric with good texture is obtained.
なお本発明で規定する物性値は以下の測定条件により
得られるものである。The physical property values specified in the present invention are obtained under the following measurement conditions.
A. 各単条のS−S曲線の5%伸長時の応力バラツキ
(CV%)ポリエステル繊維を構成する各単糸に分割し各
々の単糸について試長2cm、引張り速度2cm/分でS−S
曲線を測定し各単糸のS−S曲線の5%伸長時の応力を
求め、下式によりCV%を算出する。A. Stress variation at 5% elongation of each single-thread S-S curve (CV%) Divide into each single yarn that constitutes polyester fiber, and test each single yarn with a test length of 2 cm and a pulling speed of 2 cm / min. S
The curve is measured, the stress at 5% elongation of the SS curve of each single yarn is obtained, and the CV% is calculated by the following formula.
B. 伸度,降伏点応力 東洋ボールドウイン社製テンシロン引張り試験機を用
いて試長20cm、引張り速度10cm/分の条件でS−S曲線
を求め、伸度、降伏点応力を求める。 B. Elongation and yield point stress An SS curve is obtained using a Tensilon tensile tester manufactured by Toyo Baldwin Co., Ltd. under the conditions of a test length of 20 cm and a pulling speed of 10 cm / min, and the elongation and yield point stress are obtained.
C. 熱収縮応力のピーク値の温度 カネボウエンジニアリング製熱収縮応力測定装置を用
いて試長10cm(ループ実長20cm)、昇温速度150℃/
分、荷重0.03g/dの条件で熱収縮応力曲線を求め、該曲
線の応力値の最大値に対応する温度を読み取ることによ
り求める。C. Temperature of peak value of heat shrinkage stress Using a heat shrinkage stress measuring device manufactured by Kanebo Engineering, trial length 10 cm (loop actual length 20 cm), heating rate 150 ° C /
The heat shrinkage stress curve is obtained under the conditions of a load of 0.03 g / d and the temperature is read by reading the temperature corresponding to the maximum stress value of the curve.
実施例1 ポリエチレンテレフタレートを290℃で溶融し、孔数4
8個の口金(孔径0.18mmφ)から吐出した。吐出量は毎
分27.8gとした。口金から吐出した糸条に25m/分、20℃
の冷却風を長さ1mに渡つて吹き当て糸条を室温まで冷却
した後口金下1.2mに設けられた長さ1m、入口径6mmφ、
内部径32mmφ(入口と内部の断面積比28.4)の加熱筒に
糸条を導入した。加熱筒の壁温度は200℃とし加熱筒の
口金に近い側(上部)から整流用フイルターを通して加
熱空気を導入した。加熱空気の設定温度は250℃とし流
量は25N/分とした。Example 1 Polyethylene terephthalate was melted at 290 ° C. and the number of holes was 4
Ejection was performed from 8 nozzles (hole diameter 0.18 mmφ). The discharge rate was 27.8 g / min. 25m / min, 20 ℃ for the yarn discharged from the die
After cooling the blown yarn to a room temperature by blowing the cooling air of 1 m, the length of 1 m provided at 1.2 m below the mouthpiece, the inlet diameter 6 mmφ,
A yarn was introduced into a heating cylinder with an internal diameter of 32 mmφ (cross-sectional area ratio of the inlet and the interior was 28.4). The wall temperature of the heating cylinder was 200 ° C., and heated air was introduced from the side (upper part) of the heating cylinder close to the base (upper part) through a rectifying filter. The set temperature of the heated air was 250 ° C and the flow rate was 25 N / min.
この条件で加熱帯域中で延伸した糸条を加熱帯域から
導き出し引取速度5000m/分で引取り50デニール48フイラ
メントの糸条を得た。Under this condition, the yarn drawn in the heating zone was drawn out from the heating zone and was taken up at a take-up speed of 5000 m / min to obtain a yarn of 50 denier 48 filament.
得られた糸条の各単糸のS−S曲線の5%伸長時の応
力バラツキ(CV%)は4.53%、強度4.9g/d、伸度36%、
降伏点応力2.6g/d、熱収縮応力のピーク値の温度168℃
であつた。The stress variation (CV%) at 5% elongation of the SS curve of each single yarn of the obtained yarn is 4.53%, the strength is 4.9 g / d, the elongation is 36%,
Yield point stress 2.6g / d, temperature of peak value of heat shrinkage stress 168 ℃
It was.
又、このフアインデニールポリエステル繊維を平織に
した織物は良好な品位を有した。又、強撚織物として使
用してもシボ質も良好で欠点の無い良好な品位を有して
いた。The woven fabric obtained by plain-fabricating the fine denier polyester fiber had good quality. Even when used as a strongly twisted fabric, it had a good texture and a good quality with no defects.
比較実施例1 実施例1で加熱帯域を取り外し、それ以外は実施例1
と同一の条件で吐出量を24.8g/分、引取速度を1500m/分
とし未延伸糸を得た後、この未延伸糸を倍率3倍、温度
83℃でホツトローラー延伸し50デニール48フイラメント
の延伸糸を得た。この延伸糸の各単糸のS−S曲線の5
%延伸時の応力バラツキは10.35%であり伸度35%、降
伏点応力3.0g/dであつた。この糸を用いて平織にした織
物は所々に風合斑の欠点を有していた。又、この糸を用
いて製造した強撚織物はシボ斑が随所に見られ品位が低
かつた。Comparative Example 1 In Example 1, the heating zone was removed, otherwise Example 1 was used.
Under the same conditions as above, the discharge rate was set to 24.8 g / min, the take-up speed was set to 1500 m / min, and an undrawn yarn was obtained.
Hot roller drawing was carried out at 83 ° C. to obtain a drawn yarn of 50 denier 48 filament. 5 of the SS curve of each single yarn of this drawn yarn
The stress variation during the% stretching was 10.35%, the elongation was 35% and the yield stress was 3.0 g / d. A plain-woven fabric using this yarn had defects of uneven spots in some places. In addition, the strongly twisted woven fabric produced by using this yarn was found to have wrinkled spots everywhere and was of low quality.
比較実施例2 実施例1で加熱帯域をとり外し、それ以外は実施例1
と同一の条件で吐出量を33.1g/分、引取速度を6000m/分
とし高速紡糸法で50デニール48フイラメントの糸条を得
た。Comparative Example 2 The heating zone in Example 1 was removed, otherwise Example 1 was used.
Under the same conditions as above, the discharge rate was 33.1 g / min, the take-up speed was 6000 m / min, and a 50-denier 48 filament yarn was obtained by the high-speed spinning method.
この糸条の各単糸のS−S曲線の5%伸長時の応力バ
ラツキは3.59%であり伸度は50%、降伏点応力1.3g/dで
あつた。又、熱収縮応力のピーク値の温度は99℃であつ
た。The stress variation at 5% elongation of the SS curve of each single yarn of this yarn was 3.59%, the elongation was 50%, and the stress at yield point was 1.3 g / d. The temperature of the peak value of heat shrinkage stress was 99 ° C.
この糸条を用いて平織した織物は、本発明の降伏点応
力の範囲を外れているため、タテ、ヨコにスジ状の欠点
が目立ち品位が低かつた。又、この糸による強撚織物
は、熱収縮応力のピーク値の温度が130℃未満のため、
シボがほとんど立たず品質に問題があつた。The woven fabric plain-woven using this yarn was out of the range of the stress of the yield point of the present invention, and thus the vertical and horizontal stripe defects were conspicuous and the quality was low. Moreover, the temperature of the peak value of heat shrinkage stress is less than 130 ° C.
Almost no wrinkles were raised and there was a problem in quality.
実施例2 加熱筒の位置を表1の如く変更する以外は実施例1と
同一の条件で50デニール48フイラメントの糸条を得た。
得られた糸の物性値、製糸性、高次工程通過性を合わせ
て表1に記載した。Example 2 A yarn of 50 denier 48 filament was obtained under the same conditions as in Example 1 except that the position of the heating cylinder was changed as shown in Table 1.
The physical properties of the obtained yarn, the spinnability, and the ability to pass through higher-order processes are shown in Table 1.
表1から明らかな如く伸度30%未満となることで製糸
性、高次通過性が著しく低下することがわかる。 As is clear from Table 1, when the elongation is less than 30%, the spinnability and the high-order passability are remarkably reduced.
実施例3 吐出量、引取速度、加熱空気流量、加熱筒入口と内部
の断面積比を表2の如く変化させる以外は実施例1と同
一の条件で50デニール48フイラメントの糸条を得た。得
られた糸の各単糸のS−Sの5%伸長時の応力バラツキ
(CV%)伸度、降伏点応力及びその糸を用いた強撚織物
の性質を合わせて表2に記載した。Example 3 A yarn of 50 denier 48 filament was obtained under the same conditions as in Example 1 except that the discharge rate, the take-up speed, the heating air flow rate, and the cross-sectional area ratio between the heating cylinder inlet and the inside were changed as shown in Table 2. Table 2 also shows the stress variation (CV%) elongation at 5% elongation of SS of each single yarn of the obtained yarns, the yield point stress, and the properties of the strongly twisted woven fabric using the yarns.
表2から明らかな様に、各単糸のS−S曲線の5%伸
長時の応力バラツキが7%をこえるNo.5,6,7,8では、強
撚織物としての品位が悪く好ましくなかつた。 As is clear from Table 2, No. 5,6,7,8 in which the stress variation of the S-S curve of each single yarn at the time of 5% elongation exceeds 7%, the quality as a strongly twisted woven fabric is poor and unpreferable. It was
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭56−4715(JP,A) 特開 昭54−138613(JP,A) 特開 昭55−93816(JP,A) 特公 昭58−42286(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-56-4715 (JP, A) JP-A-54-138613 (JP, A) JP-A-55-93816 (JP, A) JP-B-58- 42286 (JP, B2)
Claims (1)
が36以上のファインデニールポリエステル繊維を製造す
るに際して、溶融紡糸したポリエステル繊維を一旦ガラ
ス転移温度以下まで冷却した後、口金から0.8〜2.0mに
設置した入口と内部の断面積の比が4以上である加熱帯
域に該糸条を導入し、該加熱帯域中で該糸条の周囲から
加熱気体を導入して熱延伸し、給油し、5000m/分以上で
引取ることを特徴とするファインデニールポリエステル
繊維の製造方法。1. When producing a fine denier polyester fiber having a single yarn denier of 1.4 d or less and a filament number of 36 or more, the melt-spun polyester fiber is once cooled to a glass transition temperature or less, and then 0.8 to 2.0 m from a spinneret. The yarn is introduced into the heating zone having a ratio of the cross-sectional area of the inlet to the inside of which is 4 or more, and the heated gas is introduced from the periphery of the yarn in the heating zone to thermally draw and refuel, A method for producing a fine denier polyester fiber, which is characterized in that it is collected at 5000 m / min or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60034540A JPH0819565B2 (en) | 1985-02-25 | 1985-02-25 | Method for producing fine denier polyester fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60034540A JPH0819565B2 (en) | 1985-02-25 | 1985-02-25 | Method for producing fine denier polyester fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61194213A JPS61194213A (en) | 1986-08-28 |
| JPH0819565B2 true JPH0819565B2 (en) | 1996-02-28 |
Family
ID=12417124
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60034540A Expired - Lifetime JPH0819565B2 (en) | 1985-02-25 | 1985-02-25 | Method for producing fine denier polyester fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0819565B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4380828B2 (en) * | 1999-01-13 | 2009-12-09 | 東洋紡績株式会社 | Recovered polyester filament and fiber product using the same |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5593816A (en) * | 1979-01-10 | 1980-07-16 | Unitika Ltd | Production of extremely fine polyester fiber |
| JPS564715A (en) * | 1979-06-22 | 1981-01-19 | Toyobo Co Ltd | Fine-denier polyester fiber |
| JPS5842286A (en) * | 1981-09-07 | 1983-03-11 | Mitsubishi Electric Corp | semiconductor laser equipment |
-
1985
- 1985-02-25 JP JP60034540A patent/JPH0819565B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61194213A (en) | 1986-08-28 |
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