JPH05125609A - Spinneret - Google Patents
SpinneretInfo
- Publication number
- JPH05125609A JPH05125609A JP4095316A JP9531692A JPH05125609A JP H05125609 A JPH05125609 A JP H05125609A JP 4095316 A JP4095316 A JP 4095316A JP 9531692 A JP9531692 A JP 9531692A JP H05125609 A JPH05125609 A JP H05125609A
- Authority
- JP
- Japan
- Prior art keywords
- spinneret
- square lattice
- discharge
- discharge holes
- spinning
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は紡糸口金、特に細デニ−
ル多フィラメント用の溶融紡糸口金に関する。BACKGROUND OF THE INVENTION The present invention relates to a spinneret, particularly fine denier.
The present invention relates to a melt spinneret for multifilaments.
【0002】[0002]
【従来の技術】ポリエステル、ポリアミド等の合成繊維
は織物、編物あるいは不織布等の材料として幅広く使用
されているが、近年これらの布帛の風合、機能性を高め
る上で単繊維のデニ−ルを細くする傾向がある。2. Description of the Related Art Synthetic fibers such as polyester and polyamide are widely used as materials for woven fabrics, knitted fabrics, non-woven fabrics, etc., but in recent years, monofilament denier has been used to improve the texture and functionality of these fabrics. It tends to be thin.
【0003】例えば、50de/36filに代って5
0de/48fil,50de/72fil,50de
/96filが、あるいは75de/36filに代っ
て75de/72fil,75de/96fil,75
de/128filが望まれることも多くなつている。For example, 5 instead of 50 de / 36 fil
0de / 48fil, 50de / 72fil, 50de
/ 96fil, or 75de / 72fil, 75de / 96fil, 75 instead of 75de / 36fil
De / 128 fil is often desired.
【0004】これら細デニ−ル多フィラメントの糸条を
効率よく製造しようとすると一枚の口金に多数の吐出孔
を穿孔する必要がある。しかしながら、一枚の口金に9
0個以上の吐出孔を配置した場合、溶融吐出した糸条の
冷却が難しいため、繊維間の密着断糸が発生したり、得
られた糸条についても染斑が発生したりしてデニ−ルの
均一性が悪化するなどの欠点があった。In order to efficiently manufacture these fine denier multifilament yarns, it is necessary to perforate a large number of discharge holes in one die. However, it is 9
When 0 or more discharge holes are arranged, it is difficult to cool the melted and discharged yarns, so that a tight break between the fibers may occur, and the obtained yarns may also have uneven stains. However, there was a defect that the uniformity of the tool deteriorated.
【0005】図5は従来周知の正方格子形状に配列した
吐出孔1の配置を示す。この場合、吐出孔1の間隔はr
で示される。一般にrが4.0mm以上であるような場
合には冷却風は各吐出孔1の間、言い換えれば吐出フィ
ラメントの間を通り抜けることができるが、rが4.0
mm以下、特に3.0mmを切るような場合には、冷却
風の貫通が難しくなり、徒に吐出フィラメントを揺動さ
せる原因になる。FIG. 5 shows the arrangement of the discharge holes 1 arranged in a conventionally known square lattice shape. In this case, the distance between the discharge holes 1 is r
Indicated by. Generally, when r is 4.0 mm or more, the cooling air can pass between the discharge holes 1, in other words, between discharge filaments, but r is 4.0.
When the thickness is less than or equal to mm, particularly 3.0 mm, it becomes difficult for the cooling air to penetrate, which may cause the discharge filament to oscillate.
【0006】従って、周知の冷却風吹き出し面に近い方
の吐出フィラメントは冷却されるが揺れ易く、逆に遠い
側に位置する吐出フィラメントは冷却風が通り抜けてこ
ないため、全く強制冷却されないことになる。Therefore, the discharge filament closer to the well-known cooling air blowing surface is cooled but easily shakes, and conversely, the discharge filament located on the far side is not forcedly cooled because the cooling air does not pass through. ..
【0007】この結果、前記のように吐出フィラメント
は密着断糸したり、断糸に至らない迄も染斑が発生した
り、デニ−ルの均一性が悪化することは避けられなかっ
た。As a result, as described above, it is unavoidable that the discharge filament is subjected to close filament breakage, stain spots are generated even before filament breakage occurs, and the uniformity of denier is deteriorated.
【0008】図5は正方格子形状の例を示したが、やは
り周知のダイヤモンド格子形状であっても或いは多重の
同心円周配置の紡糸口金であっても事情は同じであり、
吐出孔が本質的に均等に分布配置している限り冷却風を
貫通させることができないため、以上の問題は解決され
ない。この問題を解決するためには紡糸口金の面積を広
げればよいが、今度は一定の吐出量のポリマ−を薄く広
く吐出孔に分配させることが技術的に難しくなるため限
度がある。FIG. 5 shows an example of a square lattice shape, but the situation is the same whether it is a well-known diamond lattice shape or a spinneret with multiple concentric circumferential arrangements.
As long as the discharge holes are essentially evenly distributed, the cooling air cannot pass through, so the above problem cannot be solved. In order to solve this problem, the area of the spinneret should be increased, but this time it is technically difficult to distribute a constant discharge amount of the polymer thinly and widely to the discharge holes, and there is a limit.
【0009】また、2個以上の紡糸口金から吐出した糸
条を合糸して巻取る方法もあるが、この方法においては
紡糸パック当りの吐出量が小さくなるため製糸生産性に
劣るほか、ポリマ−の溶融滞留時間が長くなり熱劣化が
進むため紡糸性の悪化が懸念される。There is also a method in which yarns discharged from two or more spinnerets are combined and wound up, but in this method, since the discharge amount per spinning pack becomes small, the yarn production productivity is deteriorated, and the polymer is used. Since the melt retention time of-becomes longer and thermal deterioration proceeds, there is a concern that spinnability will deteriorate.
【0010】[0010]
【発明が解決しようとする課題】このような従来の問題
に鑑み、本発明者らは生産性の低下を来たすことなく、
しかも紡糸調子を悪化させず品質的にも優れた細デニ−
ルマルチフィラメントを得るための紡糸口金について鋭
意検討の結果、吐出孔を従来報告のないある特定配置に
設計することによって本目的が可能であることを見い出
だし、本発明に至ったのである。In view of the above conventional problems, the inventors of the present invention have been able to reduce productivity without lowering productivity.
Moreover, fine denier that does not deteriorate the spinning condition and is excellent in quality
As a result of diligent studies on a spinneret for obtaining a rumultifilament, it was found that this object can be achieved by designing a discharge hole in a specific arrangement which has not been reported in the past, and the present invention has been completed.
【0011】[0011]
【課題を解決するための手段】すなわち、本発明は90
個以上の吐出孔を有する多ホ−ルの紡糸口金において、
吐出孔が全体として方形の格子形状に配置され、隣接の
対応する4個の吐出孔は間隔pの正方格子を形成し、該
正方格子と二重正方格子を形成する間隔qの正方格子位
置に穿設した吐出孔を設けるとともに、q≧2.5pと
なしたことを特徴とする紡糸口金である。That is, the present invention is 90
In a multi-hole spinneret having more than one discharge hole,
The discharge holes are arranged in a square lattice shape as a whole, and the corresponding four adjacent discharge holes form a square lattice with a space p, and at a square lattice position with a space q forming a double square lattice with the square lattice. The spinneret is characterized in that q ≧ 2.5p is established while providing a bored discharge hole.
【0012】以下、本発明を図面に基づいて具体的に説
明する。図1は本発明の実施例を示す吐出孔配置の部分
的拡大図、図2は図1の吐出孔の拡大断面図である。The present invention will be specifically described below with reference to the drawings. 1 is a partially enlarged view of an arrangement of discharge holes showing an embodiment of the present invention, and FIG. 2 is an enlarged sectional view of the discharge holes of FIG.
【0013】本発明に係る溶融紡糸口金は図に示すよう
に二重正方格子形状に配列した吐出孔配置にされてい
る。すなわち、隣接する4個の吐出孔11は間隔pの正
方格子を形成し、更に該正方格子は間隔qの正方格子を
形成しており、図1の場合は吐出孔11をこのような二
重正方格子形状に口金全面に配列している例である。こ
の配置において最も重要であることは冷却風が通り抜け
るべき通路を確保することである。The melt spinneret according to the present invention has discharge holes arranged in a double square lattice as shown in the figure. That is, four adjacent ejection holes 11 form a square lattice with a space p, and the square lattice also forms a square lattice with a space q. In the case of FIG. This is an example in which the bases are arranged in a square lattice shape over the entire surface. The most important thing in this arrangement is to ensure a passage for the cooling air to pass through.
【0014】すなわち、冷却風はpの間を貫通すること
なくq−pの間を通過する。従って、q−pはより大で
あることが必要であり、実際にはq≧2.5pが必須と
なる。qが2.5pより小さいばあいには図5のケ−ス
と同様に冷却風はどの吐出孔間にも侵入するが、どの孔
間も通り抜けられず、紡糸調子、得られる糸質を著しく
悪化させるのである。That is, the cooling air passes through q-p without passing through p. Therefore, q−p needs to be larger, and in practice q ≧ 2.5p is essential. When q is less than 2.5 p, the cooling air penetrates into any of the discharge holes as in the case of FIG. 5, but cannot pass through any of the holes, so that the spinning tone and the obtained yarn quality are remarkably increased. Make it worse.
【0015】更に詳しくはpは1.0mm以上、3.0
mm以下が好ましい。pが1.0mm以下の場合には隣
接する吐出フィラメントが過度に接近しているため、糸
揺れが少なくてもベイラス効果等で密着が起こる可能性
がある。逆に3.0mm以上になると冷却風がpの間に
侵入可能となり、糸揺れを生じさせる原因となる。More specifically, p is 1.0 mm or more and 3.0
mm or less is preferable. When p is 1.0 mm or less, the adjacent ejection filaments are excessively close to each other, and thus the close contact may occur due to the balus effect or the like even if the yarn shake is small. On the other hand, if it is 3.0 mm or more, the cooling air can enter during the interval p, which causes the yarn to shake.
【0016】また、q−pは2.5mm以上が好まし
く、更に4.0mm以上であることが好ましい。ここ
で、q−pが2.5mm以下の場合には冷却風の侵入が
なく、従って風の通路となり得ない。q−pが4.0m
m以上であると冷却風はより抵抗なく選択的にq−p間
を流れることができるので、吐出糸条を揺動させること
もより少なくなる。Further, q-p is preferably 2.5 mm or more, more preferably 4.0 mm or more. Here, when q-p is 2.5 mm or less, the cooling air does not enter, and therefore cannot serve as a wind passage. q-p is 4.0m
When it is m or more, the cooling air can selectively flow between q and p without any resistance, so that the discharge yarn is less likely to be swung.
【0017】本発明における紡糸口金は90個以上の吐
出孔を有することが必要である。吐出孔の数が90個未
満の場合には本発明によらずとも、従来から知られてい
る正方格子配列、ダイヤモンド格子配列、あるいは多重
同心円周配列の口金で設計して差支えない。The spinneret in the present invention is required to have 90 or more discharge holes. If the number of discharge holes is less than 90, it is possible to design with a conventionally known square lattice array, diamond lattice array, or multiple concentric circumferential array die, regardless of the present invention.
【0018】本発明における紡糸口金は冷却風が通り抜
ける通路が指定されているため、各吐出フィラメントは
全方向から冷却されるのではなく、一方向からのみ冷却
を受けることになる。これは紡糸後に得られる単繊維デ
ニ−ルが太い場合には好ましいことではないが、本発明
の目的とする単繊維の細い銘柄については特に問題な
い。In the spinneret of the present invention, since the passage through which the cooling air flows is specified, each discharge filament is not cooled in all directions but is cooled only in one direction. This is not preferable when the monofilament denier obtained after spinning is thick, but there is no particular problem for the thin monofilament brand targeted by the present invention.
【0019】従って、本発明の紡糸口金は1孔当りの吐
出量が0.7g/分以下であるような細デニ−ルマルチ
フィラメントの溶融紡糸に対して適用することが好まし
い。Therefore, the spinneret of the present invention is preferably applied to melt spinning of fine denier multifilaments in which the discharge rate per hole is 0.7 g / min or less.
【0020】本発明における吐出孔の縦断面方向の形状
は従来周知であるものの他、如何なる形状のものでも差
支えないが、より好ましいのは図2に示すように1個の
導入孔12に対し4個の吐出孔11を有するような形状
である。このように縦断面方向の形状に設計すると間隔
pの正方格子より吐出された隣接する4本の吐出フィラ
メントは平行して揺れる確率が高くなる。すなわち、糸
揺れの連動性が高くなるため密着断糸が少なくなるメリ
ットがある。The shape of the discharge hole in the vertical cross-sectional direction in the present invention may be any known shape in addition to the conventionally known shape, but as shown in FIG. The shape is such that it has individual discharge holes 11. By designing the shape in the direction of the vertical section in this way, the probability that four adjacent ejection filaments ejected from the square lattice with the interval p will sway in parallel increases. That is, since the interlocking property of the yarn shake becomes high, there is an advantage that the number of contact yarn breakage decreases.
【0021】以上は口金全体に吐出孔を分散して分布す
るように配置した例であるが、好ましくは図3に示すよ
うに口金中心Oから半径R(10mm以上)の範囲内に
は吐出孔11が存在せず格子が欠落した形状の吐出孔配
置にするのが更によい。図3では4個の吐出孔11は間
隔pの正方格子を形成し、更に該正方格子は間隔qの正
方格子を形成するが、口金中心Oの位置より特定範囲
内、すなわち半径10mmの範囲内に吐出孔11が全く
存在しない配置としている。これは冷却風の中央通路が
十分に確保されるため図1のような全面配置の場合より
その通り抜けが更に向上するためである。The above is an example in which the ejection holes are arranged so as to be dispersed and distributed over the entire die, but preferably the ejection holes are within a range of a radius R (10 mm or more) from the die center O as shown in FIG. It is more preferable to arrange the discharge holes in a shape in which 11 does not exist and the grid is missing. In FIG. 3, the four discharge holes 11 form a square lattice with a space p, and the square lattice also forms a square lattice with a space q, but within a specific range from the position of the center O of the die, that is, within a range of a radius of 10 mm. The discharge holes 11 do not exist at all. This is because the central passage of the cooling air is sufficiently secured, and the passage therethrough is further improved as compared with the case of the overall arrangement as shown in FIG.
【0022】すなわち、口金中央部の一定範囲に吐出孔
がない場合、上下方向に冷却風の中央通路が確保できる
ため、マルチフィラメント群の中に流入した冷却風は口
金中心部を下流に向かって進み、単繊維がやがて冷却さ
れた後フィラメント群の外へ排出される。これによりフ
ィラメント群の均一冷却効果は更に高められ、デニ−ル
斑、染斑は一段と良化する方向に進むのである。That is, when there is no discharge hole in a certain area in the center of the die, a central passage for cooling air can be secured in the vertical direction, so that the cooling air flowing into the multifilament group is directed downstream from the center of the die. Then, the single fibers are cooled and discharged to the outside of the filament group. As a result, the uniform cooling effect of the filament group is further enhanced, and denier spots and dye spots are further improved.
【0023】[0023]
【実施例】以下、実施例により更に具体的に説明する。EXAMPLES Hereinafter, the present invention will be described more specifically by way of examples.
【0024】[0024]
【実施例1、比較例1】図1に示すような配置で吐出孔
を口金全面に配列した全面配置において、p=2.0m
m、q=7.5mmの二重正方格子配列に従って配置し
た円形吐出孔(孔径0.15mm、ランド長0.60m
m)を全体として144(4×36)個有する紡糸口金
(直径64mm、厚み15mm)を作製した。[Example 1 and Comparative Example 1] p = 2.0 m in the overall arrangement in which the ejection holes are arranged on the entire surface of the die in the arrangement as shown in FIG.
Circular ejection holes (hole diameter 0.15 mm, land length 0.60 m) arranged according to a double square lattice arrangement of m and q = 7.5 mm.
A spinneret (diameter 64 mm, thickness 15 mm) having 144 (4 × 36) m) as a whole was produced.
【0025】また、比較のため図5において、r=3.
75mmの正方格子口金を同様に作製した。For comparison, in FIG. 5, r = 3.
A 75 mm square lattice base was similarly prepared.
【0026】これらの紡糸口金を使用して、固有粘度
0.64で酸化チタン含有量が0.3重量%のポリエス
テルチップを紡糸温度295℃、紡速3300m/分で
溶融紡糸し、75de/144filの細デニ−ルマル
チフィラメントを得た。Using these spinnerets, polyester chips having an intrinsic viscosity of 0.64 and a titanium oxide content of 0.3% by weight were melt-spun at a spinning temperature of 295 ° C. and a spinning speed of 3300 m / min, and 75 de / 144 fil. Fine denier multifilaments of
【0027】この時の冷却は片面横吹き冷却紡糸筒を使
用し、口金下4cmから64cmの間で吹出し風速15
cm/sec、風量0.6Nm3 /分の条件の下に冷却
を行った。For cooling at this time, a single-sided horizontal-blow cooling spinning tube was used, and the blowing air velocity was 15 at a distance of 4 cm to 64 cm below the spinneret.
Cooling was performed under the conditions of cm / sec and air volume of 0.6 Nm 3 / min.
【0028】このときの紡糸調子、得られた細デニ−ル
マルチフィラメントのデニ−ル斑、染斑を表1に示す。Table 1 shows the spinning tone, the denier spots and the dye spots of the obtained fine denier multifilament.
【0029】[0029]
【表1】 [Table 1]
【0030】比較例1の紡調、デニ−ル斑、染斑が不良
であるに対し、本発明による紡糸口金を使用した場合
(実施例1)には良好な結果が得られた。In contrast to the poor spinning, denier spots and dye spots of Comparative Example 1, good results were obtained when the spinneret according to the present invention was used (Example 1).
【0031】[0031]
【実施例2、比較例2】図1において、p=1.5m
m、q=5.2mmの二重正方格子配列に従って配置し
た円形吐出孔(孔径0.08mm、ランド長0.48m
m)を全体として384(4×96)個有する紡糸口金
(直径72mm、厚み15mm)を作製した。Example 2 and Comparative Example 2 In FIG. 1, p = 1.5 m
Circular discharge holes (hole diameter 0.08 mm, land length 0.48 m) arranged according to a double square lattice arrangement of m and q = 5.2 mm.
A spinneret (diameter 72 mm, thickness 15 mm) having 384 (4 × 96) m) as a whole was produced.
【0032】また、比較のため図5において、r=2.
6mmの正方格子口金を同様に作製した。For comparison, in FIG. 5, r = 2.
A 6 mm square lattice base was similarly prepared.
【0033】これらの紡糸口金を使用して、実施例1と
同様にして溶融紡糸し、75de/384filの細デ
ニ−ルマルチフィラメントを得た。Using these spinnerets, melt spinning was carried out in the same manner as in Example 1 to obtain fine denier multifilaments of 75 de / 384 fil.
【0034】この時の冷却は片面横吹き冷却紡糸筒を使
用し、口金下3cmから43cmの間で風速8cm/s
ecにて冷却を行った。For cooling at this time, a single-sided horizontal-blow cooling spinning cylinder was used, and the wind speed was 8 cm / s between 3 cm and 43 cm below the spinneret.
It cooled at ec.
【0035】このときの紡糸調子、得られた細デニ−ル
マルチフィラメントのデニ−ル斑、染斑を表2に示す。Table 2 shows the spinning tone, the denier spots and the dye spots of the obtained fine denier multifilaments.
【0036】[0036]
【表2】 [Table 2]
【0037】比較例2の場合、紡糸不可であるに対し、
本発明による紡糸口金を使用した場合(実施例2)には
良好な結果が得られた。In the case of Comparative Example 2, spinning is not possible, whereas
Good results were obtained when using the spinneret according to the invention (Example 2).
【0038】[0038]
【実施例3〜4、比較例3】図3において、p=2.0
mm,q=9.0mmの二重正方格子配列に従って配置
した円形吐出孔(孔径0.15mm,ランド長0.6m
m)を全体として128個(4×32)有する中心から
半径R(10mm以上)の範囲内に吐出孔11を有しな
い紡糸口金を作製した。また、p=2.0mm,q=
9.9mmの二重正方格子配列に従って配置した同様の
吐出孔を128個有する図4に示すような中心部にも吐
出孔11を有する紡糸口金を作製した。更に、比較のた
め図5において、r=4.3mmの正方格子口金を同様
に作製した。Examples 3 to 4 and Comparative Example 3 In FIG. 3, p = 2.0
mm, q = 9.0 mm circular ejection holes arranged according to a double square lattice arrangement (hole diameter 0.15 mm, land length 0.6 m)
A spinneret having no discharge holes 11 within a radius R (10 mm or more) from the center having 128 (4 × 32) m) was produced. Also, p = 2.0 mm, q =
A spinneret having a discharge hole 11 in the central portion as shown in FIG. 4 having 128 similar discharge holes arranged according to a double square lattice array of 9.9 mm was produced. Further, for comparison, in FIG. 5, a square lattice die with r = 4.3 mm was similarly produced.
【0039】これらの紡糸口金を用いて固有粘度が0.
64で酸化チタン量が0.3%のポリエステルチップを
紡糸温度295℃、紡速3300m/分で溶融紡糸し、
75de/128filの細デニ−ルマルチフィラメン
トを得た。Using these spinnerets, the intrinsic viscosity was 0.
A polyester chip having a titanium oxide content of 0.3% at 64 was melt-spun at a spinning temperature of 295 ° C. and a spinning speed of 3300 m / min.
A fine denier multifilament of 75 de / 128 fil was obtained.
【0040】この際、冷却は片面横吹き冷却紡糸筒を使
用し、口金下4cmから64cmの間で吹出し風速15
cm/sec、風量0.6Nm3 /分の条件の下で冷却
を行った。At this time, for cooling, a single-sided horizontal-blow-cooling spinning cylinder was used, and the blowing air velocity was 15 from 4 cm to 64 cm below the spinneret.
Cooling was performed under the conditions of cm / sec and air volume of 0.6 Nm 3 / min.
【0041】このときの紡糸調子、得られた細デニ−ル
フィラメントのデニ−ル斑、染斑を表3に示す。Table 3 shows the spinning tone, denier spots and dye spots of the obtained fine denier filaments.
【0042】[0042]
【表3】 [Table 3]
【0043】[0043]
【発明の効果】以上に説明の如く、本発明によれば細デ
ニ−ル多フィラメント糸条を効率良くかつ工程調子も良
好で、品質の優れ製品を安定して得ることが可能になる
という顕著な効果を奏する。As described above, according to the present invention, it is possible to obtain a fine denier multifilament yarn efficiently and with a good process condition, and to stably obtain a product of excellent quality. Has a great effect.
【図1】本発明の実施例を示す吐出孔配置の部分的拡大
図である。FIG. 1 is a partially enlarged view of a discharge hole arrangement showing an embodiment of the present invention.
【図2】本発明の実施例を示す吐出孔の拡大断面図であ
る。FIG. 2 is an enlarged sectional view of a discharge hole showing an embodiment of the present invention.
【図3】本発明の他の実施例を示す吐出孔配置図であ
る。FIG. 3 is a discharge hole arrangement view showing another embodiment of the present invention.
【図4】本発明の他の実施例を示す吐出孔配置図であ
る。FIG. 4 is a discharge hole arrangement view showing another embodiment of the present invention.
【図5】従来の吐出孔配置の部分的拡大図である。FIG. 5 is a partially enlarged view of a conventional discharge hole arrangement.
11 吐出孔 12 導入孔 11 discharge hole 12 introduction hole
Claims (3)
紡糸口金において、吐出孔が全体として方形の格子形状
に配置され、隣接の対応する4個の吐出孔は間隔pの正
方格子を形成し、該正方格子と二重正方格子を形成する
間隔qの正方格子位置に穿設した吐出孔を設けるととも
に、q≧2.5pとなしたことを特徴とする紡糸口金。1. In a multi-hole spinneret having 90 or more discharge holes, the discharge holes are arranged in a square lattice shape as a whole, and adjacent four corresponding discharge holes are square lattices with a spacing p. And a discharge hole is provided at a square lattice position with an interval q forming the double lattice and the square lattice, and q ≧ 2.5p is established, and the spinneret is characterized in that
が穿孔されてない請求項1記載の紡糸口金。2. The spinneret according to claim 1, wherein the discharge holes are not bored within a radius of 10 mm from the center of the spinneret.
−pが2.5mm以上である請求項1又は2記載の紡糸
口金。3. p is 1.0 mm or more and 3.0 mm or less, q
The spinneret according to claim 1 or 2, wherein -p is 2.5 mm or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4095316A JP2790567B2 (en) | 1991-05-17 | 1992-04-15 | Spinneret |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14066291 | 1991-05-17 | ||
JP3-140662 | 1991-05-17 | ||
JP4095316A JP2790567B2 (en) | 1991-05-17 | 1992-04-15 | Spinneret |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05125609A true JPH05125609A (en) | 1993-05-21 |
JP2790567B2 JP2790567B2 (en) | 1998-08-27 |
Family
ID=26436566
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4095316A Expired - Fee Related JP2790567B2 (en) | 1991-05-17 | 1992-04-15 | Spinneret |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2790567B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007009368A (en) * | 2005-06-30 | 2007-01-18 | Toray Ind Inc | Spinneret and method for producing ultrafine fiber |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60110908A (en) * | 1983-11-15 | 1985-06-17 | Toray Ind Inc | Spinneret part device |
-
1992
- 1992-04-15 JP JP4095316A patent/JP2790567B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60110908A (en) * | 1983-11-15 | 1985-06-17 | Toray Ind Inc | Spinneret part device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007009368A (en) * | 2005-06-30 | 2007-01-18 | Toray Ind Inc | Spinneret and method for producing ultrafine fiber |
JP4725213B2 (en) * | 2005-06-30 | 2011-07-13 | 東レ株式会社 | Spinneret and method for producing ultrafine fiber |
Also Published As
Publication number | Publication date |
---|---|
JP2790567B2 (en) | 1998-08-27 |
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