JP3866843B2 - Spinneret for hollow fiber - Google Patents

Spinneret for hollow fiber Download PDF

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JP3866843B2
JP3866843B2 JP31506497A JP31506497A JP3866843B2 JP 3866843 B2 JP3866843 B2 JP 3866843B2 JP 31506497 A JP31506497 A JP 31506497A JP 31506497 A JP31506497 A JP 31506497A JP 3866843 B2 JP3866843 B2 JP 3866843B2
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Prior art keywords
hollow
circle
holes
spinneret
channel
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JPH11152615A (en
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嗣生 藤原
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Teijin Fibers Ltd
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Teijin Fibers Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は、繊維軸に直角方向の断面(以下、単に「繊維断面」と称する)でみた場合に、全繊維断面中に占める中空部の占有面積の割合(以下、「中空率」と称する)が高い繊維、即ち、中空率が50%以上である超高中空糸を溶融紡糸することのできる紡糸口金に関するものであり、軽量かつ保温性が高く、張り腰、シャリ感のある繊維を製造することができる紡糸口金に関する。
【0002】
【従来の技術】
従来、中空糸を溶融紡糸するに際しては、図3(a),(b)に示されるように、円弧状のスリット流路孔を有する吐出孔を同一の円周上に複数個穿設した中空糸用紡糸口金が一般に使用されていた。しかし、このような紡糸口金から紡出される中空糸の中空率は、たかだか30〜35%のものしか得ることができなかった。しかも、このような紡糸口金を使用して、更に高い中空率を持った中空糸を得ようとすると、図4(a)〜(c)に示すように、互いに隣り合ったスリット流路孔から吐出されるポリマーが接合される接合部に窪みが生じたり、接合に不具合が生じたりする問題を有していた。
【0003】
このような問題を解消して、しかも繊維断面の真円性を高めた中空糸を得るための紡糸口金が、特開昭58―169507号公報に提案されている。確かに、この紡糸口金によれば、中空率が20%以下の比較的中空率の小さいものに関しては、中空割れを発生させずに、繊維断面が略真円の中空糸を安定して得ることができる。しかしながら、30%を越えるような高中空率を有する糸を製造しようとすると、どうしても繊維断面の形に歪みが発生するため、このような糸を得ることは難しかった。即ち、繊維断面が真円に近い形を得ようとしても、真円になり難いという大きな問題を抱えていた。
【0004】
【発明が解決しようとする課題】
本発明は、このような従来技術における欠点を解消し、略真円で、かつ中空率が50%以上である中空糸を安定して製造するための紡糸口金を提供しようとするものである。もし、このような紡糸口金が提供されることになれば、略真円の繊維断面形状を有し、しかも、高中空率の中空糸を安定かつ確実に製造することが可能となり、従来より更に軽量性と保温性に優れた中空糸を得ることが出来る。
【0005】
【課題を解決するための手段】
ここに、本発明によれば、上記の課題を極めて巧妙に解決した下記の構成を有する紡糸口金が提供される。
【0006】
即ち、本発明は、1個の中空部を有する中空単繊維からなる中空マルチフィラメント糸を溶融紡糸するための、下記の要件a〜eを同時に満足する吐出孔を複数個有する中空糸用紡糸口金である。
a.同一円(C)の円周に外接して円弧状のスリット流路孔(H)が等配に4個以上、8個以下設けられ、かつ該スリット流路孔(H)はその内縁(Ei)部両端近傍に円(C)の略中心方向へ半円状に突出する突出流路孔(h)を有し、
b.口金のポリマー吐出面において、該スリット流路孔(H)群のポリマー濡れ縁によって囲繞されて形成される開口流路面積をS2とし、前記円(C)で囲繞される面積をS1とした場合に、これらのS1とS2との間に成立する、流路占有率(R)=(S2/S1)×100という関係式において、該流路占有率(%)が7%≦R≦10%であって、
c.前記円(C)の直径(D)が1.6mm以上、1.8mm以下であり、
d.互いに隣接する前記のスリット流路孔(H)間の間隔(t)が0.08mm以上、0.1mm以下であり、
e.突出流路孔(h)群のみで構成される、口金吐出面での全開口流路面積(S3)が前記開口流路面積(S2)に占める割合(S3/S2×100)が、2.0%以上、10.0%以下であること。
【0007】
なお、以下の本発明の記載において、「流路占有率(R)」とは、前記式、R=(S2/S1)×100で定義される値(%)を指すものとする。
【0008】
【実施例】
次に、前記の構成において、略真円の繊維断面形状を有し、しかも、高中空率の中空糸を得るための紡糸口金の実施例について、その作用とともに、以下に詳細に説明する。
中空糸を含めて一般にポリマーから熱可塑性樹脂から成る繊維を溶融紡糸する場合において、紡糸口金から吐出されたポリマーは、吐出直後に膨らむ現象(いわゆる「バラス効果」)が生じ、その後、細化が始まる。このバラス効果は、得られる中空糸の中空率に極めて大きな役割を果たす。即ち、一般的にポリマーの溶融温度が低くなると、吐出孔より吐出されるポリマーのバラス効果が大きくなり、得られる中空糸の中空率は高くなる。しかしながら、一方では、中空率が高くなる程、吐出孔から吐出されたポリマーの吐出時の円弧状の形状は、そのままの円弧状に維持され難く、得られる糸条の繊維断面形態は、吐出条件に応じて種々に変形する。このような繊維断面形状の変形は、前記のように種々の要因によって左右される。ここで、これらの要因を図1に示した本発明の中空糸用紡糸口金を例にとって列挙すれば、円弧状のスリット流路孔(H)の数、該スリット流路孔の直径(D)、互いに隣り合うスリット流路孔間の間隔幅(t)、前記の流路占有率(R)、円(C)の面積中における突出流路孔面積占有割合、1ホール当たりのポリマー吐出孔がある。なお、図1は、紡糸口金に穿設された、一本の単繊維を紡糸するための基本単位となる一つの吐出孔の平面図を示す。
【0009】
以下、本発明の紡糸口金に設けられた吐出孔を具体的なパラメータと共に図面に基いて詳細に説明する。
なお、図1はマルチフィラメントを構成する中空単繊維(一つのフィラメント)を紡糸するための吐出孔を例示したものであって、マルチフィラメントを紡糸するためには、このような基本単位からなる吐出孔をフィラメント数に対応して穿設されている紡糸口金が使用されることは言うまでもない。なお、図2は、図1の紡糸口金で溶融紡糸して得られた中空糸の繊維断面を示したものであって、中空部が高中空率で形成されている例を示した繊維断面図である。
【0010】
なお、図1において、本発明の紡糸口金に穿設された吐出孔は、6個の円弧状のスリット流路孔(H)を有しており、該スリット流路孔(H)のそれぞれの外縁(Eo)は、円(C)に内接している。しかも、互いに隣り合うスリット流路孔(H)は僅かな間隔(t)を隔てて、円(C)上に等配されている。
【0011】
次に、図4に示したようなポリマーの貼り合わせが良くない糸条(図(a))や繊維断面形状が変形した糸条(図(b)及び(c))を形成させないために、各スリット流路孔(H)の両端部近傍の内縁(Ei)には、円(C)の略内向き法線方向に突出した突出流路孔(h)を設けることが肝要である。この突出流路孔(h)は、間隔(t)を置いて互いに隣接するスリット流路孔(H)に対して、互いに近接対向させて、線対称に対として設けることが重要である。また、スリット流路孔(H)の数は、ほぼ真円状の繊維断面形状を形成させるためには多い方が好ましいが、孔開け加工の精度や煩雑さ、あるいは加工コスト等の面から4〜8個が好ましい。
【0012】
更に、スリット流路孔(H)の外縁(Eo)に内接する内接円(C)によって囲繞された円(C)の内部領域の面積をS1とし、吐出孔のポリマーの濡れ縁に囲繞されて形成された全開口流路面積をS2と定義すると、これらのS1とS2が、7%≦R=(S2/S1)×100≦10%という関係式を満足することが必要である。なお、この関係式において、本発明ではRを「流路占有率」と称することは前述した通りである。この流路占有率(R)が7%未満であれば、図4(a)に示したようなポリマーの貼り合わせ部が不良の中空糸となり、10%より大きくなると、中空率が50%以上の高中空率の中空糸を得ることが難しくなる。
【0013】
但し、該流路占有率(R)は、互いに隣接する円弧形状のスリット流路孔(H)を離間する間隙幅(t)によって大きく左右される。この間隔幅(t)と流路占有率(R)との関係に関して更に付言すれば、一般に、tが小さい場合には、Rを小さな値に選定し、逆にtが大きい場合には、Rを大きな値に選定することが好ましい。しかしながら、50%以上の超高中空率を有する糸を得るためには、前記のように7%≦R≦10%という関係を有することが肝要であるため、この関係を前提として、間隔幅(t)が0.08mm以上、0.1mm以下とすることが好ましいことが実験により分かっている。もし、tが小さすぎると、吐出されたポリマーの接合が早く行われ、扁平な中空糸となりやすく、更には、紡糸口金がポリマーの吐出圧力で変形し易くなるため、口金の強度設計上好ましくない。また、tが大きくなりすぎると接合が遅れ、このために、ポリマーの貼り合わせが十分に行われず、中空割れの原因となる。
【0014】
また、内接円(C)の直径(D)は大きくする方が超中空糸となりやすいが、糸のデニール、口金面のスペース、紡糸の安定性等の制約から、1.6mm以上、1.8mm以下とすることが好ましい。
【0015】
次に、図4に示したようなポリマーの貼り合わせがよくない糸条を形成させないために、各スリット流路孔(H)の両端部の近傍の内縁(Ei)に円(C)の中心方向へ向かって半円状に突出した突出流路孔対(h)を設け、吐出孔(図1の場合、6個のスリット流路孔(H)と、12個の突出流路孔(h)とからなる)の全開口流路面積において、突出流路孔(h)が占有する口金吐出面での開口流路面積の割合が、2.0%以上、4.0%以下であることが好ましい。この場合、前記の割合が2.0%未満では、ポリマーの貼り合わせが不良となり易く、また、4.0%を越えると50%以上の高中空率を有する糸を得るのが難しくなる。
【0016】
更に、50%以上の高中空糸を安定して製造するためには、吐出孔からの1ホール当りのポリマー吐出量が2.0g/min以上、2.6g/min以下とすることが好ましい。何故ならば、吐出量が2.0g/min未満では、ポリマーの吐出線速度が下がり、吐出斑や冷却斑を誘発させ、ポリマーの貼り合わせが不良となり易く、また、糸切れも起こり易いからである。また、吐出量が2.6g/minを越えると、今度はポリマーの吐出線速度が上がり過ぎて、遅延冷却となって50%以上の高中空糸を得ることが困難となるからである。
【0017】
最後に、以上に述べた本発明の吐出孔を有する紡糸口金を使用した実験例について、以下に説明する。
円弧状スリット流路孔(H)を6個、0.09mmの間隔幅(t)をおいて、その外縁(Eo)を直径(D)が1.7mmの内接円(C)に内接させて、該円(C)上に等配に配置した。このとき、流路占有率(R)を8%とし、吐出孔の全開口流路面積中に突出流路孔(h)が占める面積の割合を3%として、常法にしたがってポリエステルから成る中空糸を紡糸した。得られた中空糸の繊維断面を観察したところ、その繊維断面形状は、ほぼ真円状であって、その中空率は55%であり、中空割れもなかった。
【0018】
また、流路占有率(R)を7%と10%とする以外は、前記と同一の条件を採用して、得られた中空糸の中空率は、それぞれ53%と51%であり、中空割れも発生せず、その繊維断面はほぼ真円に近かった。
【0019】
【発明の効果】
以上に説明の如く、本発明によれば、略真円であって、かつ50%以上の高中空率糸を安定かつ確実に紡糸することができ、これによって、軽量で保温性が高く、張り腰、シャリ感のある素材を得ることができる。また、紡糸するポリマーの粘度斑、張り合わせ不良がないため、糸切れが発生することなく、安定した紡糸が可能となる。このため、製糸パフォーマンスに優れ、しかも、超軽量な高品位の糸を得ることが可能になるという極めて顕著な効果を奏する。
【図面の簡単な説明】
【図1】本発明の中空糸用紡糸口金に穿設される吐出孔を例示した平面図である。
【図2】図1の吐出孔で得られた中空糸の繊維断面を例示した図である。
【図3】(a)及び(b) 従来の吐出孔を示す平面図である。
【図4】(a) 図3(a)に図示した吐出孔で得られた中空糸の繊維断面図である。
(b)及び(c) 図3(b)の吐出孔で得られた中空糸の繊維断面図である。
【符号の説明】
1 紡糸口金本体
C 内接円
Ei 内縁
Eo 外縁
H スリット流路孔
h 突出流路孔
D 内接円の直径
t 互いに隣接する吐出孔の間隔幅
[0001]
BACKGROUND OF THE INVENTION
The present invention, when viewed in a cross section perpendicular to the fiber axis (hereinafter simply referred to as “fiber cross section”), the ratio of the occupied area of the hollow portion in the entire fiber cross section (hereinafter referred to as “hollow ratio”) Is related to a spinneret capable of melt-spinning ultra-high hollow fiber having a hollow ratio of 50% or more, and produces a lightweight, highly heat-retaining fiber with tightness and sharpness. It relates to a spinneret.
[0002]
[Prior art]
Conventionally, when melt spinning a hollow fiber, as shown in FIGS. 3 (a) and 3 (b), a hollow in which a plurality of discharge holes having arc-shaped slit channel holes are formed on the same circumference. A spinneret for yarn was generally used. However, the hollow ratio of the hollow fiber spun from such a spinneret was only 30 to 35%. Moreover, using such a spinneret, when trying to obtain a hollow fiber having a higher hollow ratio, as shown in FIGS. 4 (a) to (c), from the slit channel holes adjacent to each other, There has been a problem in that a recess is formed in a bonded portion to which the discharged polymer is bonded, or a defect occurs in bonding.
[0003]
A spinneret for solving such a problem and obtaining a hollow fiber having an improved roundness of a fiber cross section has been proposed in Japanese Patent Laid-Open No. 58-169507. Certainly, according to this spinneret, a hollow fiber having a substantially round fiber cross-section can be stably obtained without causing a hollow crack in a relatively small hollow ratio of 20% or less. Can do. However, when a yarn having a high hollow ratio exceeding 30% is to be produced, it is difficult to obtain such a yarn because the shape of the fiber cross section is inevitably distorted. That is, even when trying to obtain a shape in which the fiber cross section is close to a perfect circle, it has a big problem that it is difficult to become a perfect circle.
[0004]
[Problems to be solved by the invention]
The present invention seeks to provide a spinneret for solving such drawbacks in the prior art and stably producing a hollow fiber having a substantially perfect circle and a hollow ratio of 50% or more. If such a spinneret is to be provided, it becomes possible to stably and surely produce a hollow fiber having a substantially circular fiber cross-sectional shape and having a high hollow ratio, which is more than conventional. A hollow fiber excellent in lightness and heat retention can be obtained.
[0005]
[Means for Solving the Problems]
Here, according to the present invention, there is provided a spinneret having the following configuration which has solved the above-mentioned problem very skillfully.
[0006]
That is, the present invention provides a spinneret for hollow fibers having a plurality of discharge holes simultaneously satisfying the following requirements a to e for melt spinning a hollow multifilament yarn composed of a hollow single fiber having one hollow portion. It is.
a. Four or more and eight or less arc-shaped slit channel holes (H) are circumscribed around the circumference of the same circle (C), and the slit channel holes (H) have inner edges (Ei). ) In the vicinity of the ends of the part has a projecting flow path hole (h) projecting in a semicircular shape toward the approximate center of the circle (C),
b. On the polymer discharge surface of the die, when the opening channel area formed by the polymer wetting edge of the slit channel hole (H) group is S2, and the area surrounded by the circle (C) is S1 In the relational expression (R) = (S2 / S1) × 100, which is established between S1 and S2, the flow path occupancy (%) is 7% ≦ R ≦ 10%. There,
c. The diameter (D) of the circle (C) is 1.6 mm or more and 1.8 mm or less,
d. The interval (t) between the slit channel holes (H) adjacent to each other is 0.08 mm or more and 0.1 mm or less,
e. The ratio (S3 / S2 × 100) of the total opening channel area (S3) on the die discharge surface, which is composed only of the protruding channel hole (h) group, to the opening channel area (S2) is 2. 0% or more and 10.0% or less.
[0007]
In the following description of the present invention, “channel occupation ratio (R)” refers to a value (%) defined by the above formula, R = (S2 / S1) × 100.
[0008]
【Example】
Next, an embodiment of a spinneret for obtaining a hollow fiber having a substantially perfect fiber cross section with the above-described configuration and having a high hollow ratio will be described in detail below along with its function.
In the case of melt spinning a fiber made of a thermoplastic resin from a polymer including a hollow fiber, the polymer discharged from the spinneret is swelled immediately after discharge (so-called “ballus effect”), and then thinning occurs. Begins. This ballast effect plays a very important role in the hollowness of the hollow fiber obtained. That is, generally, when the melting temperature of the polymer is lowered, the ballast effect of the polymer discharged from the discharge hole is increased, and the hollow ratio of the obtained hollow fiber is increased. However, on the other hand, the higher the hollow ratio is, the harder the arcuate shape at the time of discharging the polymer discharged from the discharge hole is to be maintained as it is. Various modifications are made depending on the situation. Such deformation of the fiber cross-sectional shape depends on various factors as described above. Here, if these factors are enumerated taking the spinneret for hollow fibers of the present invention shown in FIG. 1 as an example, the number of arc-shaped slit channel holes (H), the diameter (D) of the slit channel holes , spacing width between the slits passage holes adjacent to each other (t), the flow path occupancy of the (R), occupancy of the protruding flow path hole area during the area of a circle (C), 1 polymer discharge hole per hole There is. FIG. 1 is a plan view of one discharge hole, which is a basic unit for spinning one single fiber, which is formed in the spinneret .
[0009]
It will be described in detail with reference to FIG surface discharge hole provided in the spinneret of the present invention to the specific parameters and co.
FIG. 1 exemplifies a discharge hole for spinning a hollow single fiber (single filament) constituting a multifilament . In order to spin a multifilament, a discharge composed of such basic units is shown. Needless to say, a spinneret having holes corresponding to the number of filaments is used. 2 shows a fiber cross section of a hollow fiber obtained by melt spinning with the spinneret of FIG. 1, and a fiber cross section showing an example in which the hollow portion is formed with a high hollow ratio. It is.
[0010]
In FIG. 1 , the discharge hole formed in the spinneret of the present invention has six arc-shaped slit channel holes (H), and each of the slit channel holes (H) The outer edge (Eo) is inscribed in the circle (C). In addition, the slit channel holes (H) adjacent to each other are equally arranged on the circle (C) with a slight interval (t).
[0011]
Next, in order not to form the yarn (Fig. (A)) and the yarn (Fig. (B) and (c)) in which the fiber cross-sectional shape is deformed as shown in FIG. It is important to provide a projecting channel hole (h) projecting in a substantially inward normal direction of the circle (C) at the inner edge (Ei) in the vicinity of both ends of each slit channel hole (H). It is important that the protruding flow path holes (h) are provided in pairs symmetrically opposite to each other and adjacent to the slit flow path holes (H) adjacent to each other with an interval (t). The number of slit channel holes (H) is preferably large in order to form a substantially circular fiber cross-sectional shape. ~ 8 are preferred.
[0012]
Furthermore, the area of the inner region of the circle (C) surrounded by the inscribed circle (C) inscribed in the outer edge (Eo) of the slit flow path hole (H) is S1, and is surrounded by the polymer wetting edge of the discharge hole. When the formed total opening channel area is defined as S2, it is necessary that these S1 and S2 satisfy the relational expression of 7% ≦ R = (S2 / S1) × 100 ≦ 10%. In this relational expression, in the present invention, R is referred to as “channel occupation ratio” as described above. If this channel occupation ratio (R) is less than 7%, the polymer bonded portion as shown in FIG. 4 (a) becomes a defective hollow fiber, and if it exceeds 10%, the hollow ratio is 50% or more. It becomes difficult to obtain a hollow fiber having a high hollow ratio.
[0013]
However, the channel occupation ratio (R) is greatly influenced by the gap width (t) separating the arc-shaped slit channel holes (H) adjacent to each other. In further remarks regarding the relationship between the interval width (t) and the channel occupation ratio (R), generally, when t is small, R is selected to be a small value, and conversely, when t is large, R is selected. It is preferable to select a large value. However, in order to obtain a yarn having an ultrahigh hollow ratio of 50% or more, it is important to have a relationship of 7% ≦ R ≦ 10% as described above. Experiments have shown that t) is preferably 0.08 mm or more and 0.1 mm or less. If t is too small, the discharged polymer is joined quickly, and it becomes easy to form a flat hollow fiber. Further, the spinneret is easily deformed by the discharge pressure of the polymer, which is not preferable in terms of the strength design of the die. . Moreover, when t becomes too large, joining is delayed, and therefore, the polymer is not sufficiently bonded to cause hollow cracking.
[0014]
Further, the diameter (D) of the inscribed circle (C) is more likely to be a super hollow fiber. However, due to constraints such as yarn denier, cap surface space, and spinning stability, 1.6 mm or more. It is preferable to be 8 mm or less.
[0015]
Next, in order not to form a yarn with poor polymer bonding as shown in FIG. 4, the center of the circle (C) is formed on the inner edge (Ei) in the vicinity of both ends of each slit channel hole (H). Protruding channel hole pairs (h) projecting in a semicircular shape toward the direction are provided, and discharge holes (in the case of FIG. 1, six slit channel holes (H) and twelve projecting channel holes (h The ratio of the open channel area on the nozzle discharge surface occupied by the projecting channel hole (h) is 2.0% or more and 4.0% or less. Is preferred. In this case, when the ratio is less than 2.0%, polymer bonding tends to be poor, and when it exceeds 4.0%, it is difficult to obtain a yarn having a high hollow ratio of 50% or more.
[0016]
Furthermore, in order to stably produce a high hollow fiber of 50% or more, it is preferable that the polymer discharge amount per hole from the discharge hole is 2.0 g / min or more and 2.6 g / min or less. This is because when the discharge rate is less than 2.0 g / min, the discharge linear velocity of the polymer is lowered, causing discharge spots and cooling spots, the polymer is likely to be stuck poorly, and yarn breakage is likely to occur. is there. Moreover, if the discharge amount exceeds 2.6 g / min, the discharge linear velocity of the polymer is increased too much, and it becomes difficult to obtain a high hollow fiber of 50% or more due to delayed cooling.
[0017]
Finally, an experimental example using the spinneret having the discharge holes of the present invention described above will be described below.
Six arc-shaped slit channel holes (H) with an interval width (t) of 0.09 mm and the outer edge (Eo) inscribed in an inscribed circle (C) with a diameter (D) of 1.7 mm And arranged equally on the circle (C). At this time, the flow rate occupation ratio (R) is 8%, and the ratio of the area occupied by the protruding flow passage holes (h) to the total opening flow passage area of the discharge holes is 3%. The yarn was spun. When the fiber cross section of the obtained hollow fiber was observed, the fiber cross sectional shape was almost perfect circle, the hollow ratio was 55%, and there was no hollow crack.
[0018]
Moreover, the hollow ratio of the obtained hollow fiber is 53% and 51%, respectively, except that the channel occupation ratio (R) is 7% and 10%. No cracks occurred, and the fiber cross section was almost a perfect circle.
[0019]
【The invention's effect】
As described above, according to the present invention, it is possible to stably and reliably spin a high-hollow-ratio yarn having a substantially perfect circle and 50% or more. A material with a sense of waist and sharpness can be obtained. Further, since there is no viscosity unevenness or poor lamination of the polymer to be spun, stable spinning can be performed without causing yarn breakage. For this reason, there is an extremely remarkable effect that it is possible to obtain a high-quality yarn that is excellent in yarn production performance and that is ultralight.
[Brief description of the drawings]
FIG. 1 is a plan view illustrating a discharge hole formed in a spinneret for hollow fibers of the present invention.
FIG. 2 is a view illustrating a fiber cross section of a hollow fiber obtained at the discharge hole of FIG. 1;
FIGS. 3A and 3B are plan views showing conventional ejection holes. FIGS.
4A is a fiber cross-sectional view of a hollow fiber obtained by the discharge hole illustrated in FIG.
(B) And (c) It is a fiber sectional view of the hollow fiber obtained with the discharge hole of Drawing 3 (b).
[Explanation of symbols]
1 Spinneret Main Body C Inscribed Circle Ei Inner Edge Eo Outer Edge H Slit Channel Hole h Projected Channel Hole D Diameter of Inscribed Circle t Distance between Discharge Holes Adjacent to each other

Claims (1)

1個の中空部を有する中空単繊維からなる中空マルチフィラメント糸を溶融紡糸するための、下記の要件a〜eを同時に満足する吐出孔を複数個有する中空糸用紡糸口金。
a.同一円(C)の円周に外接して円弧状のスリット流路孔(H)が等配に4個以上、8個以下設けられ、かつ該スリット流路孔(H)はその内縁(Ei)部両端近傍に円(C)の略中心方向へ半円状に突出する突出流路孔(h)を有し、
b.口金のポリマー吐出面において、該スリット流路孔(H)群のポリマー濡れ縁によって囲繞されて形成される開口流路面積をS2とし、前記円(C)で囲繞される面積をS1とした場合に、これらのS1とS2との間に成立する、流路占有率(R)=(S2/S1)×100という関係式において、該流路占有率(%)が7%≦R≦10%であって、
c.前記円(C)の直径(D)が1.6mm以上、1.8mm以下であり、
d.互いに隣接する前記のスリット流路孔(H)間の間隔(t)が0.08mm以上、0.1mm以下であり、
e.突出流路孔(h)群のみで構成される、口金吐出面での全開口流路面積(S3)が前記開口流路面積(S2)に占める割合(S3/S2×100)が、2.0%以上、10.0%以下であること。
A spinneret for hollow fibers having a plurality of discharge holes simultaneously satisfying the following requirements a to e for melt spinning a hollow multifilament yarn composed of a hollow single fiber having one hollow portion .
a. Four or more and eight or less arc-shaped slit channel holes (H) are circumscribed around the circumference of the same circle (C), and the slit channel holes (H) have inner edges (Ei). ) In the vicinity of the ends of the part has a projecting flow path hole (h) projecting in a semicircular shape toward the approximate center of the circle (C),
b. On the polymer discharge surface of the die, when the opening channel area formed by the polymer wetting edge of the slit channel hole (H) group is S2, and the area surrounded by the circle (C) is S1 In the relational expression (R) = (S2 / S1) × 100, which is established between S1 and S2, the flow path occupancy (%) is 7% ≦ R ≦ 10%. There,
c. The diameter (D) of the circle (C) is 1.6 mm or more and 1.8 mm or less,
d. The interval (t) between the slit channel holes (H) adjacent to each other is 0.08 mm or more and 0.1 mm or less,
e. The ratio (S3 / S2 × 100) of the total opening channel area (S3) on the die discharge surface, which is composed only of the protruding channel hole (h) group, to the opening channel area (S2) is 2. 0% or more and 10.0% or less.
JP31506497A 1997-11-17 1997-11-17 Spinneret for hollow fiber Expired - Fee Related JP3866843B2 (en)

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KR20010028164A (en) * 1999-09-18 2001-04-06 조민호 Sinneret for hollow fiber having high hollowness
WO2010045430A2 (en) * 2008-10-15 2010-04-22 National University Of Singapore Dual-layer hollow fibers with enhanced flux as forward osmosis membranes for water reuses and protein enrichment
CN113122939A (en) * 2021-03-19 2021-07-16 江苏永银化纤有限公司 Preparation method of regenerated hollow yarn with moisture absorption and breathability and spinneret plate for production

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