JP2636879B2 - Polyester fiber - Google Patents

Polyester fiber

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Publication number
JP2636879B2
JP2636879B2 JP63101340A JP10134088A JP2636879B2 JP 2636879 B2 JP2636879 B2 JP 2636879B2 JP 63101340 A JP63101340 A JP 63101340A JP 10134088 A JP10134088 A JP 10134088A JP 2636879 B2 JP2636879 B2 JP 2636879B2
Authority
JP
Japan
Prior art keywords
fiber
spinning
less
present
pill
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 - Fee Related
Application number
JP63101340A
Other languages
Japanese (ja)
Other versions
JPH01272816A (en
Inventor
裕功 濱田
小柳  正
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Kasei Corp
Original Assignee
Asahi Kasei Kogyo KK
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Application filed by Asahi Kasei Kogyo KK filed Critical Asahi Kasei Kogyo KK
Priority to JP63101340A priority Critical patent/JP2636879B2/en
Publication of JPH01272816A publication Critical patent/JPH01272816A/en
Application granted granted Critical
Publication of JP2636879B2 publication Critical patent/JP2636879B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はポリエステル繊維に関する。更に詳しくは、
高速紡糸引取法によって製造される、抗ピル性と熱安定
性に優れたポリエステル繊維に関する。
Description: TECHNICAL FIELD The present invention relates to a polyester fiber. More specifically,
The present invention relates to a polyester fiber produced by a high-speed spinning take-off method and having excellent pill resistance and heat stability.

〔従来の技術と発明が解決しようとする課題〕[Problems to be solved by conventional technology and invention]

ポリエステル繊維を編織物に供すると耐しわ性や耐久
性に優れ、且つ取扱いが容易で乾き易いなどの利点があ
る。しかしその反面、着用しているうちに摩擦によって
繊維が組織から引出されて絡みあい、毛玉(ピル)を生
じる。特にポリエステル繊維のよに高強度の繊維では、
生じたピルが脱落し難く、むしろ生長して編織物の表面
を見苦しくするという欠点があった。
When a polyester fiber is used for a knitted fabric, there are advantages such as excellent wrinkle resistance and durability, easy handling, and easy drying. However, on the other hand, the fibers are pulled out of the tissue due to friction while wearing, and the fibers are entangled with each other to produce pills. Especially for high strength fiber such as polyester fiber,
The resulting pill has a drawback that it is difficult for the pill to fall off, but rather grows and makes the surface of the knitted fabric difficult to see.

近年、ポリエステル繊維の製造は生産性向上が、強く
求められるようになり、製糸工程、特に紡糸工程で5500
m/分越える高速度の引取速度を用いる高速紡糸引取法が
試みられるようになってきた。
In recent years, there has been a strong demand for improved productivity in the production of polyester fibers.
High speed spinning take-off methods using high take-off speeds in excess of m / min have been attempted.

この為の高速紡試引取法で、上記ポリエステル繊維の
欠点であるピルの発生を抑える繊維の製造法が提案され
ている。例えば特開昭54−30923号公報では紡口下に特
別な加圧ガス室を設け、室内から紡出された繊維と加圧
空気とを共に噴出させ6000〜8000m/mの紡速を達成する
と共に抗ピル性の繊維を得ようとするものである。かか
る技術では紡口下に特別な設備を設けなければならず、
操作面でも設備コスト的にも不利である。しかも前記公
報の様に加圧空気と繊維とを共に噴出させる方法では空
気圧のわずかな変動でデニール斑や染色斑が発生し、実
用的な繊維は得られない。また得られた繊維の抗ピル性
も不充分である。
For this purpose, there has been proposed a method for producing a fiber which suppresses the generation of pills, which is a drawback of the polyester fiber, by a high-speed spinning test take-off method. For example, in Japanese Patent Application Laid-Open No. 54-30923, a special pressurized gas chamber is provided under the spinneret, and fibers spun from the chamber and pressurized air are ejected together to achieve a spinning speed of 6000 to 8000 m / m. In addition, it is intended to obtain an anti-pill fiber. In such technology, special equipment must be provided under the spout,
It is disadvantageous in terms of operation and equipment costs. Moreover, in the method in which both the pressurized air and the fiber are jetted out as described in the above-mentioned publication, denier spots and stain spots occur due to slight fluctuations in the air pressure, and practical fibers cannot be obtained. Moreover, the anti-pill property of the obtained fiber is also insufficient.

またポリエステルチップの水分率を高くし6000m/分以
上の速度で引取り紡糸することで抗ピル性繊維を得る技
術が特開昭57−133216号公報に開示されている。しかし
ながらチップ水分率を高くして得られた繊維は染色斑が
発生し易く、その欠点を解消する為には水分率を通常の
ポリエステルの紡糸と同様に低く抑えることが必要で、
その結果、強度が高くなり抗ピル性は失なわれてしまう
という問題がある。
JP-A-57-133216 discloses a technique for obtaining an anti-pill fiber by increasing the water content of a polyester chip and spinning the yarn at a speed of 6000 m / min or more. However, the fiber obtained by increasing the moisture content of the chip is liable to cause staining spots, and it is necessary to keep the moisture content low as in the case of ordinary polyester spinning in order to eliminate the disadvantages.
As a result, there is a problem that the strength is increased and the anti-pill property is lost.

従って、高速紡糸引取法によって製造され且つ抗ピル
性と熱安定性に優れたポリエステル繊維は現在迄得られ
ていなかった。
Therefore, a polyester fiber produced by a high-speed spinning take-off method and having excellent pill resistance and heat stability has not been obtained until now.

本発明の目的は高速紡糸引取法によって製造される抗
ピル性と熱安定性に優れたポリエステル繊維を提供する
ことである。
An object of the present invention is to provide a polyester fiber produced by a high-speed spinning take-off method and having excellent pill resistance and heat stability.

〔課題を解決する為の手段〕[Means for solving the problem]

本発明者らは、上記問題点を解決する為、鋭意検討を
重ねた結果、本発明に到達した。すなわち本発明による
ポリエステル繊維は固有粘度〔η〕が0.65以下、繊維の
中心から半径の0.8倍の距離にある複屈折率と繊維の中
心の複屈折率との差(δΔn)が40×10-3以上であり、
結晶性完全性パラメータが0.3以下であることを特徴と
する。かかるポリエステル繊維のタフネス(TF)は15以
下である。
The present inventors have conducted intensive studies to solve the above problems, and as a result, have reached the present invention. That is, the polyester fiber according to the present invention has an intrinsic viscosity [η] of 0.65 or less and a difference (δΔn) between the birefringence at a distance of 0.8 times the radius from the center of the fiber and the birefringence at the center of the fiber (40 × 10 ). 3 or more,
The crystalline perfection parameter is 0.3 or less. The toughness (T F ) of such polyester fibers is 15 or less.

本発明に使用するポリエステルはエチレンテレフタレ
ートの繰返し単位を90モル%以上、好ましくは95モル%
以上含有するエチレンテレフタレートであるが、得られ
る繊維の熱安定性を損なわない範囲で少量の第3成分を
含有していても良い。
The polyester used in the present invention has a repeating unit of ethylene terephthalate of 90 mol% or more, preferably 95 mol%.
Although ethylene terephthalate is contained as described above, a small amount of the third component may be contained as long as the thermal stability of the obtained fiber is not impaired.

ポリエステル繊維の抗ピル性を改善するには、繊維自
身のタフネスを小さくすることが有効であることが知ら
れている。ここでいうタフネスとは繊維が伸長によって
破断するまでのエネルギーを意味し、簡便には引張試験
によって得られる引張強度(T・S)と引張伸度(T・
E)の値から下記式で表すことができる。
It is known that reducing the toughness of the fiber itself is effective in improving the anti-pill property of the polyester fiber. The toughness here means the energy until the fiber is broken by elongation, and is simply a tensile strength (TS) and a tensile elongation (T ·) obtained by a tensile test.
From the value of E), it can be expressed by the following equation.

タフネス(TF)=(T・S)×(T・E)1/2 通常の衣料用繊維のTFが約30に対しTF=20〜25のもの
が抗ピル性繊維として用いられている。これに対し本発
明ではTF=15以下の極めてタフネスの小さい抗ピルに優
れた繊維を得ることに成功した。
Toughness (T F ) = (T · S) × (T · E) 1/2 Normal clothing fibers having a T F of about 30 and T F = 20 to 25 are used as anti-pill fibers. I have. On the other hand, in the present invention, it was possible to obtain a fiber having an extremely low toughness and an excellent anti-pill having a T F = 15 or less.

本発明のTF=15以下の抗ピル性ポリエステル繊維は固
有粘度〔η〕を0.65以下とすることと、繊維の中心から
半径の0.8倍の距離にある複屈折率と繊維の中心の複屈
折率との差δ(Δn)を40×10-3以上とすることの組合
せによって初めて達成される。これらのいずれか一方が
この条件を外れた場合にはTFが15を越え本発明の目的と
する抗ピル性の優れたポリエステル繊維とはなりえな
い。
The anti-pill polyester fiber of the present invention having T F = 15 or less has an intrinsic viscosity [η] of 0.65 or less, and has a birefringence and a birefringence at the center of the fiber at a distance of 0.8 times the radius from the center of the fiber. This is achieved for the first time by a combination of setting the difference δ (Δn) from the ratio to 40 × 10 −3 or more. If any one of these conditions deviates from this condition, the TF exceeds 15 and it cannot be a polyester fiber having excellent anti-pill properties aimed at by the present invention.

より低いタフネスを得る為に好ましい固有粘度〔η〕
は0.59以下であり、更に好ましくは0.56以下である。
〔η〕の下限は特に限定されないが紡糸安定性から
〔η〕が0.40以上が好ましい。またδ(Δn)は45×10
-3以上が好ましく更に好ましくは50×10-3以上である。
〔η〕が0.56以下、δ(Δn)が50×10-3以上の組合せ
によってはTFが10以下も達成され、極めて抗ピル性の優
れたポリエステル繊維を得ることができる。固有粘度を
単に紡糸可能な下限である0.40まで低下させても、TF
高々20までしか下げ得ないことを鑑みれば、複屈折率差
との組み合わせによる効果ば、顕著である。
Preferred intrinsic viscosity [η] to obtain lower toughness
Is 0.59 or less, more preferably 0.56 or less.
The lower limit of [η] is not particularly limited, but is preferably 0.40 or more from the viewpoint of spinning stability. Δ (Δn) is 45 × 10
-3 or more, more preferably 50 × 10 -3 or more.
Depending on the combination of [η] of 0.56 or less and δ (Δn) of 50 × 10 −3 or more, TF of 10 or less can be achieved, and a polyester fiber having extremely excellent pill resistance can be obtained. In view of the fact that the TF can be reduced to at most 20 even when the intrinsic viscosity is simply reduced to the lower limit of spinning of 0.40, the effect of the combination with the birefringence difference is remarkable.

本発明において低タフネス繊維が得られるのは、繊維
断面内の複屈折率差が大きくなることで配向分布が生じ
低配向部分が繊維の強伸度低下に影響を及ぼしている故
と推案される。
It is supposed that the low toughness fiber is obtained in the present invention because the orientation distribution occurs due to a large birefringence index difference in the fiber cross section, and the low orientation portion affects the strong elongation of the fiber. You.

本発明の繊維は結晶完全性パラメーターCRが0.3以下
であることが必要である。
The fibers of the present invention need to have a crystal integrity parameter CR of 0.3 or less.

結晶安全性パラメーターCRは、X線回析により後述す
る方法によって測定される、結晶領域の成長度を表現す
る尺度である。CRの値が小さい程結晶の成長が進んでお
り、熱安定性が優れたものとなる。通常の低速紡糸一延
伸で得られたポリエステル繊維のCRは0.5以上であるこ
とから分かるように、本発明の繊維は、高度に成長した
結晶構造を有している。かかる結晶構造を有した本発明
の繊維は、例えば、沸水収縮率が5%以下と小さく、織
物とした際の湿潤加工工程に先立って行なわれるプレセ
ット工程を省略できる位である。このような理由から、
CRは0.3以下が必要であり、好ましくは0.25以下、更に
好ましくは0.2以下である。
Crystalline safety parameters C R is measured by a method described later by X-ray diffraction is a measure for expressing the growth of the crystal region. As the value of C R is small is advanced growth of the crystal, and that the thermal stability and excellent. As the C R of the polyester fibers obtained in the normal low speed spinning one drawing seen from is 0.5 or more, the fibers of the present invention has a highly grown crystal structure. The fiber of the present invention having such a crystal structure has a small boiling water shrinkage ratio of, for example, 5% or less, which is sufficient to omit the presetting step performed prior to the wet processing step in the case of fabric. For these reasons,
C R is required 0.3 or less, preferably 0.25 or less, more preferably 0.2 or less.

以下、本発明の繊維の製造方法について述べる。本発
明の繊維はポリエステルを溶融紡糸するに際し、固有粘
度〔η〕が0.65以下で紡出された繊維を紡口直下に紡糸
過程中に発生するネック点の位置が30〜100cmになるよ
うに加熱域を設け、次いで該加熱域を通過した繊維のネ
ック点の延伸比(ネック延伸比)を5.0以上として引取
ることにより得ることができる。
Hereinafter, the method for producing the fiber of the present invention will be described. When the fiber of the present invention is melt-spun polyester, a fiber spun with an intrinsic viscosity [η] of 0.65 or less is heated just below the spinneret so that the position of a neck point generated during the spinning process is 30 to 100 cm. A zone is provided, and then the drawing ratio of the neck point of the fiber that has passed through the heating zone (neck drawing ratio) is set to 5.0 or more, and the fiber can be obtained.

本発明でいうネック点とは引取速度が6000m/分以上の
高速紡糸において観察される、紡糸過程中の急激な繊維
直径の細化が発生する位置のことである。(繊維学会誌
Vo138,No.11 1982 499頁〜507頁参照) 紡口より押出された固有粘度〔η〕が0.65以下の繊維
は、紡口直下に設けた加熱域を通過した後、冷却され
る。加熱域は単糸繊度、紡糸速度によって好適な長さ及
び温度が選ぶことができ、本発明においては長さ10〜80
cm、好ましくは20cm〜70cm、温度100℃〜300℃、好まし
くは150℃〜250℃の範囲の中から選ばれる。
The neck point referred to in the present invention is a position where a sharp reduction in fiber diameter occurs during the spinning process, which is observed in high-speed spinning at a take-up speed of 6000 m / min or more. (Journal of the Textile Society of Japan
Vo138, No. 11, 1982, pp. 499-507) The fiber extruded from the spinneret and having an intrinsic viscosity [η] of 0.65 or less is cooled after passing through a heating zone provided immediately below the spinneret. The heating zone can be selected to a suitable length and temperature depending on the fineness of the single yarn and the spinning speed, and in the present invention, the length is 10 to 80.
cm, preferably 20 cm to 70 cm, and a temperature in the range of 100 ° C to 300 ° C, preferably 150 ° C to 250 ° C.

本発明における加熱域の効果は本発明の繊維の構造を
決定する目的と安定した紡糸性を得る上で必須である。
即ち紡口直下に加熱域を設けずして本発明の繊維を得よ
うとしても安定した紡糸が困難である。
The effect of the heating zone in the present invention is essential for the purpose of determining the structure of the fiber of the present invention and for obtaining stable spinnability.
That is, stable spinning is difficult even if the fiber of the present invention is obtained without providing a heating zone immediately below the spinning port.

加熱域の具体的形状としては、角または円筒状の加熱
ヒーター等が採用できるが、これに限定されるものでは
ない。
As a specific shape of the heating zone, a square or cylindrical heater, etc. can be adopted, but it is not limited to this.

本発明の繊維の紡糸に於ては、加熱域の条件、具体的
には、加熱筒長、加熱域温度を適切に選定することによ
ってネック点を紡口面下30〜100cmとなる如く調整す
る。
In the spinning of the fiber of the present invention, the condition of the heating zone, specifically, the length of the heating cylinder, the temperature of the heating zone is appropriately selected to adjust the neck point to be 30 to 100 cm below the spinning surface. .

加熱域を有せず紡糸する方法では、このネック点の位
置が紡口面下30cm以内となってしまい安定した紡糸は困
難である。
In the spinning method without a heating zone, the position of the neck point is within 30 cm below the spinning surface, and stable spinning is difficult.

加熱域が長過ぎたり、温度が高すぎてネック点紡口面
下が100cm以上の位置になると得られた繊維の(δΔ
n)が40×10-3以下となり本発明が目的とするタフネル
TF=15以下の強度はえられない。従ってネック点の位置
調整は、良好な紡糸安定性とTFが15以下の繊維を得る上
で極めて重要である。両者を好ましくバランスさせるに
はネック点の位置が紡口面下40〜90cmであることが望ま
しい。
If the heating zone is too long or the temperature is too high and the position below the spout surface of the neck point is 100 cm or more, (δΔ
n) is 40 × 10 −3 or less and the tufnel targeted by the present invention
The strength below T F = 15 cannot be obtained. Therefore, the adjustment of the position of the neck point is extremely important for obtaining a fiber having good spinning stability and a TF of 15 or less. In order to preferably balance both, it is desirable that the position of the neck point is 40 to 90 cm below the spinning surface.

加熱域を出た繊維は冷却チャンバーからの冷却風によ
って室温まで冷却される。本発明に使用する冷却風は、
温度10〜40℃、湿度40〜80%RH、風速0.05〜0.5m/秒の
通常の溶融紡糸に採用される冷却風が適用され、低温や
高風速などの特殊な冷却条件である必要はない。チャン
バーの形状は通常の横吹タイプや紡糸口金の形状に合せ
た円周冷却タイプ等が採用される。
The fibers exiting the heating zone are cooled to room temperature by cooling air from a cooling chamber. The cooling air used in the present invention is
Cooling air adopted for normal melt spinning at a temperature of 10 to 40 ° C, humidity of 40 to 80% RH, and a wind speed of 0.05 to 0.5 m / sec is applied, and there is no need to use special cooling conditions such as low temperature or high wind speed . As the shape of the chamber, an ordinary horizontal blowing type, a circumferential cooling type adapted to the shape of the spinneret, or the like is adopted.

加熱域を出た繊維は紡糸過程中で発生するネック点の
延伸比(ネック延伸比)を5.0以上として引取ることが
必要である。ネック延伸比が5.0未満では本発明の特長
とする、低強度や熱安定性はえられない。本発明の繊維
を得る為に好ましい引取速度は8500m/分以上である。
It is necessary that the fiber exiting the heating zone be drawn with a draw ratio (neck draw ratio) of a neck point generated in the spinning process of 5.0 or more. If the neck stretching ratio is less than 5.0, low strength and thermal stability, which are features of the present invention, cannot be obtained. The preferred take-off speed for obtaining the fibers of the present invention is 8500 m / min or more.

前述の製造方法により本発明の抗ピル性と熱安定性に
優れたポリエステル繊維を得ることが可能となった。
According to the above-mentioned production method, it became possible to obtain the polyester fiber of the present invention having excellent pill resistance and heat stability.

〔実施例〕〔Example〕

実施例をもって本発明を詳細に説明する。尚、本発明
のポリエステル繊維の特性の測定方法を以下に述べる。
The present invention will be described in detail with reference to examples. The method for measuring the properties of the polyester fiber of the present invention is described below.

◎固有粘度〔η〕 溶剤としてO−クロロフェノールを用い、ポリマー濃
度を種々変えてηsp/cを測定し、濃度0へ外挿した値を
固有粘度〔η〕とする。
固有 Intrinsic viscosity [η] Using O-chlorophenol as a solvent and variously changing the polymer concentration, ηsp / c is measured, and the value extrapolated to a concentration of 0 is defined as the intrinsic viscosity [η].

◎複屈折率 透過定量干渉顕微鏡(東独、カームツアイスイエナ社
製)を使用し、緑色光線(波長54.9mμ)を用い、繊維
軸に平行及び垂直な電場ベクトルに対する干渉縞パター
ンから下記の方法により繊維内半径方向の屈折率分布を
測定し求める。
◎ Birefringence Using a transmission quantitative interference microscope (manufactured by Kalmts Ice Jena, East Germany), using a green light beam (wavelength: 54.9 mμ), the fiber was obtained from the interference fringe pattern against the electric field vector parallel and perpendicular to the fiber axis by the following method. The refractive index distribution in the inner radial direction is measured and determined.

第1図に繊維の干渉縞のパターンの一例を示す。第1
図で、繊維の封入剤の屈折率をN、繊維の外周上の点
S′−S″間の屈折率をn(又はn)、S′−S″
間の厚みをt、使用光線の波長をλ、バックグラウンド
の平行干渉縞の間隔(1λに相当)をD、繊維による干
渉縞のずれをdとすると光路差Rは で表わされる。
FIG. 1 shows an example of a pattern of interference fringes of a fiber. First
In the figure, the refractive index of the encapsulant for the fiber is N, the refractive index between points S′-S ″ on the outer periphery of the fiber is n / (or nn ), and S′-S ″.
Assuming that the thickness between them is t, the wavelength of the light beam used is λ, the interval between parallel interference fringes in the background (corresponding to 1λ) is D, and the shift of the interference fringes due to the fiber is d, the optical path difference R is Is represented by

繊維の半径をRとすると、繊維の中心R0から外へRま
での各位置での光路差から各位置での繊維の屈折率n
(又はn)の分布を求めることができる。例えばrを
繊維の中心から各位置までの距離とした時、X=r/R=
0すなわち繊維の中心における屈折率をn/(0)(又
はn⊥(0))とし、X=0.8の点に於ける屈折率をn
/(0.8)(又はn⊥(0.8))とする。各位置の複屈折
率をΔ=n−nで求め、繊維の中心から半径の0.
8倍の繊維(X=0.8)にある複屈折率(Δn0.8)と繊
維の中心(X=0)の複屈折率(Δn0)との差をδΔn
する。
Assuming that the radius of the fiber is R, the refractive index n / of the fiber at each position is obtained from the optical path difference at each position from the center R 0 of the fiber to the outside R.
(Or n ) distribution can be obtained. For example, when r is the distance from the center of the fiber to each position, X = r / R =
0, that is, the refractive index at the center of the fiber is n / (0) (or n⊥ (0) ), and the refractive index at the point of X = 0.8 is n
/(0.8) (or n⊥ (0.8) ). Seeking birefringence of each position in the Δ n = n / -n ⊥, 0 from the center of the fiber radius.
Birefringence in the 8 times the fiber (X = 0.8) δΔn the difference between the birefringence ([Delta] n 0) of the ([Delta] n 0.8) and fiber center (X = 0)
I do.

すなわちδ(Δn)は δ(Δn)=Δn0.8−Δn0 である。That is, δ (Δn) is δ (Δn) = Δn 0.8 −Δn 0 .

◎結晶完全性パラメーターCR X線回析装置を用い、試料の厚みを約0.5mmとして以
下の条件で回析角2θが7゜から35゜までの回析強度曲
線を描いた。
◎ using crystalline integrity parameter C R X-ray diffractometer, the diffraction angle 2θ in the following conditions the thickness of the sample as approximately 0.5mm drew diffraction intensity curve at 35 DEG from 7 °.

30kV,80mA、スキャンニング速度1゜/分、チャート
速度10mm/分、タイムコンスタント1秒、レシービング
スリット0.3mmとした。
30 kV, 80 mA, scanning speed 1 mm / min, chart speed 10 mm / min, time constant 1 second, receiving slit 0.3 mm.

2θ=17゜〜26゜の範囲に描かれた3つの主要な反射
を低角度側から(100),(010),(10)とする。
2θ=7゜と35゜の間にある回析強度曲線を直線で結び
ベースラインとする。各ピークとベースラインの間に垂
線を引きこの垂線を回析強度とする。(010)と(110)
間の谷にあたる点での回析強度をI0とし、(10)の
ピークの回析強度をIとした時、結晶完全性パラメータ
・CRは次式で示される。
The three main reflections drawn in the range of 2θ = 17 ° to 26 ° are (100), (010), and (10) from the low angle side.
A diffraction intensity curve between 2θ = 7 ° and 35 ° is connected by a straight line to be a baseline. A perpendicular is drawn between each peak and the baseline, and this perpendicular is defined as the diffraction intensity. (010) and (110)
When the diffraction intensity at the point corresponding to the valley between is defined as I 0 and the diffraction intensity of the peak of (10) is defined as I, the crystal integrity parameter C R is represented by the following equation.

◎タフネス TF 東洋ボールドウィン社製TENSILON UTM−II−20型引張
試験機により初長20cm、引波速度20cm/分で、引波強度
(T・S)と引波伸度(T・E)を測定し次式により求
める。
◎ toughness T F Hatsucho 20cm by Toyo Baldwin Co. TENSILON UTM-II-20 type tensile tester at a引波speed 20cm / min,引波strength (T · S) and引波elongation (T · E) Measure and determine by the following formula.

タフネス(TF)=(T・S)×(T・E)1/2 ◎抗ピル性 得られた繊維の合糸し、トウ状として捲縮を付与し、
長さ38mmのステープルに切断して紡績用短繊維にする。
この短繊維を30番手の紡績糸とし、これを手編機(18ゲ
ージ)で編み立てたのち、JIS−L−1076(1967年)の
方法で試験する。評価は視覚判定によって行ない、ピル
の発生状況を下記の基準により判定する。
Toughness (T F ) = (T · S) × (T · E) 1/2 ◎ Anti-pill property The obtained fibers are plied and crimped as a tow.
It is cut into staples 38 mm long to make short fibers for spinning.
This short fiber is made into a spun yarn of 30th count, knitted with a hand knitting machine (18 gauge), and then tested by the method of JIS-L-1076 (1967). The evaluation is performed by visual judgment, and the occurrence state of the pill is judged according to the following criteria.

5級:ピルの発生、外観の変化がほとんど認められない
もの。
Grade 5: Pill formation and little change in appearance are recognized.

4級:ピルの発生及び外観の変化が軽度のもの。Grade 4: Mild pill generation and slight change in appearance.

3級:ピルの発生及び外観の変化が中程度のもの。Grade 3: Moderate pill generation and change in appearance.

2級:ピルの発生及び外観の変化が相当認められるも
の。
Second grade: Generation of pills and change in appearance are considerably recognized.

1級:ピルの発生及び外観の変化が極めて顕著に認めら
れるもの。
Primary: Those in which generation of pills and changes in appearance are extremely remarkable.

なお上記等級に於いて4級以上であれば抗ピル性は良
好であると判定できる。
In addition, if it is a quaternary or higher in the above grades, it can be determined that the anti-pill property is good.

◎ネック点の位置 Zimmer社製線径測定器460A/2型により紡糸過程中の糸
径の変化を測定し、急激な変化を呈している箇所をネッ
ク点とし紡口面からの距離であらわした。また、肉眼観
察でも確認した。
◎ Neck point position The change in the yarn diameter during the spinning process was measured using a wire diameter measuring instrument 460A / 2 made by Zimmer, and the point where the sudden change was exhibited was taken as the neck point and expressed as the distance from the spinning surface. . It was also confirmed by visual observation.

◎ネック延伸比 紡糸過程中の糸径の変化をZimmer社製線形測定器によ
り測定し、ネック点直前の糸径(d1)とネック点直後の
糸径(d2)より求めた。
◎ Neck stretching ratio The change in the yarn diameter during the spinning process was measured by a linear measuring device manufactured by Zimmer, and the yarn diameter (d 1 ) immediately before the neck point and the yarn diameter (d 2 ) immediately after the neck point were determined.

実施例1 繊維の固有粘度〔η〕が第1表に示される各種ポリエ
チレンレフタレートを紡糸温度310℃で孔径0.35mmφ孔
数24個の紡糸口金より押出した。紡口直下には内径100m
mφ、長さ35cmのアルミ鋳込みヒーター加熱方式の加熱
筒を紡口面と該加熱筒の間隙がない状態で設定し、加熱
域を設けた。尚、加熱域は、230℃とした。
Example 1 Various polyethylene phthalates having an intrinsic viscosity [η] of fibers shown in Table 1 were extruded at a spinning temperature of 310 ° C. from a spinneret having a hole diameter of 0.35 mmφ and 24 holes. 100m inside diameter just below the spout
A heating cylinder of mφ and a length of 35 cm of an aluminum casting heater heating method was set without a gap between the spinning surface and the heating cylinder, and a heating area was provided. The heating area was 230 ° C.

加熱域を出た繊維は、通常の横吹チャンバーにより冷
風温度20℃、湿度60%RH、風速0.1m/秒の冷却風で室温
まで冷却し油剤付与後、引取速度9500m/分で50d/24fの
繊維を得た。
After exiting the heating zone, the fiber is cooled to room temperature with a cooling air at a cold air temperature of 20 ° C, a humidity of 60% RH, and a wind speed of 0.1 m / sec. Fiber was obtained.

得られた繊維の性能を第1表に示す。 Table 1 shows the performance of the obtained fibers.

第1表から明らかな様に、固有粘度〔η〕が0.65以下
で、(δΔn)が40×10-3以上とならば、タフネス15以
下の繊維を得ることができる。
As is apparent from Table 1, if the intrinsic viscosity [η] is 0.65 or less and (δΔn) is 40 × 10 −3 or more, fibers having a toughness of 15 or less can be obtained.

尚、得られた繊維を一口編地にし精練・染色したサン
プルの染色斑を視覚評価したところNo.1〜4とも、染色
斑は、ほとんどなかった。
In addition, when the obtained fiber was made into a single-piece knitted fabric and scouring and dyeing of the sample was visually evaluated, no staining spot was found in any of Nos. 1 to 4.

実施例2 固有粘度〔η〕0.59のポリエチレンテレフタレートを
用い、紡糸温度300℃、孔径0.35mmφ、孔数24個の紡糸
口金より押出した。紡口直下にアルミ鋳込みヒーター加
熱方式の加熱筒を紡口面と間隙がないように設置し、20
0℃の温度の加熱域を設けた。加熱筒は内径110mmφで長
さを第2表に示す如く変化させた。
Example 2 Polyethylene terephthalate having an intrinsic viscosity [η] of 0.59 was extruded from a spinneret having a spinning temperature of 300 ° C., a hole diameter of 0.35 mmφ, and 24 holes. A heating cylinder with an aluminum casting heater heating system is installed just below the spinneret so that there is no gap with the spinning surface.
A heating zone at a temperature of 0 ° C. was provided. The heating cylinder had an inner diameter of 110 mm and the length was changed as shown in Table 2.

加熱域を出た繊維は、実施例1と同じ条件で例極固化
させ、油剤付与後10,000m/分の取引速度で50d/24fの繊
維を得た。
The fiber exiting the heating zone was solidified under the same conditions as in Example 1 to obtain 50d / 24f fibers at a transaction speed of 10,000 m / min after the oil agent was applied.

得られた繊維の性能を第2表に示す。 Table 2 shows the performance of the obtained fibers.

第2表から明らかな様にネック点が100cm以下であれ
ば、タフネス15以下の繊維となり、抗ピル性も良好であ
る。
As is clear from Table 2, if the neck point is 100 cm or less, the fiber has a toughness of 15 or less, and the pill resistance is good.

〔発明の効果〕 本発明の高速紡糸引取法によって製造されるポリエス
テル繊維は抗ピル性と熱安定に優れ、均染性の良好なポ
リエステル繊維である。
[Effects of the Invention] The polyester fiber produced by the high-speed spinning take-off method of the present invention is a polyester fiber having excellent pill resistance and heat stability and good levelness.

また、得られた繊維を編織物に供すると、ピルの発生
が極めて少なく、良好な均染性がえられた。
In addition, when the obtained fiber was subjected to a knitted fabric, generation of pills was extremely small, and good levelness was obtained.

【図面の簡単な説明】[Brief description of the drawings]

第1図は繊維の複屈折率を測定する際用いた繊維の断面
内半径方向屈折率(n/又はn)分布を求める為の干渉
縞パターンの一例である。図においては(a)は繊維の
断面図、(b)は干渉縞パターンで、1は繊維、2は封
入剤による干渉縞、3は繊維により干渉縞である。
FIG. 1 is an example of an interference fringe pattern for obtaining a radial refractive index (n / or n ) distribution in a cross section of a fiber used for measuring the birefringence of the fiber. In the figure, (a) is a cross-sectional view of the fiber, (b) is an interference fringe pattern, 1 is a fiber, 2 is an interference fringe by an encapsulating agent, and 3 is an interference fringe by a fiber.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】固有粘度〔η〕が0.65以下、繊維の中心か
ら半径の0.8倍の距離にある複屈折率と繊維の中心の複
屈折率との差(δ(Δn))が40×10-3以上であり、結
晶完全パラメーター(CR)が0.3以下であり、かつ下記
式で表される繊維のタフネス(TF)が15以下であること
を特徴とするポリエステル繊維 TF=(T・S)×(T・E)1/2 (上式中、T・S及びT・Eは引張強度及び引張伸度を
それぞれ表す)。
The difference (δ (Δn)) between the birefringence at a distance of 0.8 times the radius from the center of the fiber and the birefringence at the center of the fiber (δ (Δn)) is 40 × 10 or less. and at -3, the crystalline perfection parameters (C R) is 0.3 or less, and polyester fiber toughness of the fiber represented by the following formula (T F) is characterized in that at most 15 T F = (T S) x (TE) 1/2 (where TS and TE represent tensile strength and tensile elongation, respectively).
JP63101340A 1988-04-26 1988-04-26 Polyester fiber Expired - Fee Related JP2636879B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63101340A JP2636879B2 (en) 1988-04-26 1988-04-26 Polyester fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63101340A JP2636879B2 (en) 1988-04-26 1988-04-26 Polyester fiber

Publications (2)

Publication Number Publication Date
JPH01272816A JPH01272816A (en) 1989-10-31
JP2636879B2 true JP2636879B2 (en) 1997-07-30

Family

ID=14298110

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63101340A Expired - Fee Related JP2636879B2 (en) 1988-04-26 1988-04-26 Polyester fiber

Country Status (1)

Country Link
JP (1) JP2636879B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105908273B (en) * 2016-07-05 2018-04-17 雷鸣 A kind of bi-component composite fiber of high anti-fluffing and anti-pilling and high abrasion and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61245306A (en) * 1985-04-22 1986-10-31 Asahi Chem Ind Co Ltd Polyester raw material yarn for providing napped cloth
JPS62104942A (en) * 1985-07-16 1987-05-15 旭化成株式会社 Raised pile fabric and knitted fabric

Also Published As

Publication number Publication date
JPH01272816A (en) 1989-10-31

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